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David Price
a448949a 1 parent 2c406fe3

Checked split files from DPR2 ASGARD test file

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Showing 14 changed files with 2761 additions and 1339 deletions
...@@ -779,6 +779,237 @@ dpr-tables:OperationInformation ...@@ -779,6 +779,237 @@ dpr-tables:OperationInformation
779 ] ; 779 ] ;
780 rhspin:tableHeaders ("Facility"^^xsd:string "Incident Type"^^xsd:string "Count"^^xsd:string) . 780 rhspin:tableHeaders ("Facility"^^xsd:string "Incident Type"^^xsd:string "Count"^^xsd:string) .
781 781
782 +dpr-tables:OtherVolumes
783 + rdf:type rhspin:TableTemplate ;
784 + rdfs:label "Consume, Import, Export, Other Volume List"^^xsd:string ;
785 + rdfs:subClassOf rhspin:DPRTableTemplates ;
786 + spin:body
787 + [ rdf:type sp:Select ;
788 + sp:orderBy ([ sp:varName "flowPurposeName"^^xsd:string
789 + ] [ sp:varName "flowInOutFacilityName"^^xsd:string
790 + ] [ sp:varName "flowDefinitionName"^^xsd:string
791 + ]) ;
792 + sp:resultVariables ([ sp:varName "containingWholeFacilityName"^^xsd:string
793 + ] [ sp:varName "flowInOutFacilityName"^^xsd:string
794 + ] [ sp:varName "flowPurposeName"^^xsd:string
795 + ] [ sp:varName "flowDefinitionName"^^xsd:string
796 + ] [ sp:varName "densityValue"^^xsd:string
797 + ] [ sp:varName "pressureValue"^^xsd:string
798 + ] [ sp:varName "temperatureValue"^^xsd:string
799 + ]) ;
800 + sp:where ([ sp:object <http://www.reportinghub.no/ep/schema/report#ProductionReport> ;
801 + sp:predicate rdf:type ;
802 + sp:subject
803 + [ sp:varName "report"^^xsd:string
804 + ]
805 + ] [ sp:object
806 + [ sp:varName "report"^^xsd:string
807 + ] ;
808 + sp:predicate <http://www.reportinghub.no/ep/schema/core#partOf> ;
809 + sp:subject
810 + [ sp:varName "productvolumereport"^^xsd:string
811 + ]
812 + ] [ sp:object <http://www.reportinghub.no/ep/schema/report#ProductVolumeReport> ;
813 + sp:predicate rdf:type ;
814 + sp:subject
815 + [ sp:varName "productvolumereport"^^xsd:string
816 + ]
817 + ] [ sp:object
818 + [ sp:varName "productionflownetwork"^^xsd:string
819 + ] ;
820 + sp:predicate <http://www.reportinghub.no/ep/schema/report#reportOn> ;
821 + sp:subject
822 + [ sp:varName "productvolumereport"^^xsd:string
823 + ]
824 + ] [ sp:object <http://www.reportinghub.no/ep/schema/flow#ProductionFlowNetwork> ;
825 + sp:predicate rdf:type ;
826 + sp:subject
827 + [ sp:varName "productionflownetwork"^^xsd:string
828 + ]
829 + ] [ sp:object
830 + [ sp:varName "flow"^^xsd:string
831 + ] ;
832 + sp:predicate <http://www.reportinghub.no/ep/schema/flow#hasNetworkPart> ;
833 + sp:subject
834 + [ sp:varName "productionflownetwork"^^xsd:string
835 + ]
836 + ] [ sp:object <http://www.reportinghub.no/ep/schema/flow#ProductionFlow> ;
837 + sp:predicate rdf:type ;
838 + sp:subject
839 + [ sp:varName "flow"^^xsd:string
840 + ]
841 + ] [ sp:object
842 + [ sp:varName "productionflownetwork"^^xsd:string
843 + ] ;
844 + sp:predicate <http://www.reportinghub.no/ep/schema/flow#facilityContainsFlow> ;
845 + sp:subject
846 + [ sp:varName "productionflownetworkFacility"^^xsd:string
847 + ]
848 + ] [ sp:object
849 + [ sp:varName "containingWholeFacility"^^xsd:string
850 + ] ;
851 + sp:predicate <http://www.reportinghub.no/ep/schema/core#temporalPartOf> ;
852 + sp:subject
853 + [ sp:varName "productionflownetworkFacility"^^xsd:string
854 + ]
855 + ] [ sp:object
856 + [ sp:varName "containingWholeFacilityName"^^xsd:string
857 + ] ;
858 + sp:predicate <http://www.reportinghub.no/np/schema/npd#name> ;
859 + sp:subject
860 + [ sp:varName "containingWholeFacility"^^xsd:string
861 + ]
862 + ] [ sp:object
863 + [ sp:varName "flowWhole"^^xsd:string
864 + ] ;
865 + sp:predicate <http://www.reportinghub.no/ep/schema/core#temporalPartOf> ;
866 + sp:subject
867 + [ sp:varName "flow"^^xsd:string
868 + ]
869 + ] [ sp:object <http://www.reportinghub.no/ep/schema/flow#WholeLifeProductionFlow> ;
870 + sp:predicate rdf:type ;
871 + sp:subject
872 + [ sp:varName "flowWhole"^^xsd:string
873 + ]
874 + ] [ sp:object
875 + [ sp:varName "flowInOutFacility"^^xsd:string
876 + ] ;
877 + sp:predicate <http://www.reportinghub.no/ep/schema/flow#flowIntoOrOutOf> ;
878 + sp:subject
879 + [ sp:varName "flowWhole"^^xsd:string
880 + ]
881 + ] [ rdf:type sp:TriplePath ;
882 + sp:object
883 + [ sp:varName "flowInOutFacilityName"^^xsd:string
884 + ] ;
885 + sp:path [ rdf:type sp:AltPath ;
886 + sp:path1 <http://www.reportinghub.no/ep/schema/core#name> ;
887 + sp:path2 <http://www.reportinghub.no/np/schema/npd#name>
888 + ] ;
889 + sp:subject
890 + [ sp:varName "flowInOutFacility"^^xsd:string
891 + ]
892 + ] [ sp:object
893 + [ sp:varName "flowPurpose"^^xsd:string
894 + ] ;
895 + sp:predicate rdf:type ;
896 + sp:subject
897 + [ sp:varName "flowWhole"^^xsd:string
898 + ]
899 + ] [ sp:object <http://www.reportinghub.no/ep/schema/flow#ProductionFlowPurposeType> ;
900 + sp:predicate rdf:type ;
901 + sp:subject
902 + [ sp:varName "flowPurpose"^^xsd:string
903 + ]
904 + ] [ rdf:type sp:Filter ;
905 + sp:expression
906 + [ rdf:type sp:ne ;
907 + sp:arg1 [ sp:varName "flowPurpose"^^xsd:string
908 + ] ;
909 + sp:arg2 <http://www.reportinghub.no/ep/schema/flow#Injection>
910 + ]
911 + ] [ rdf:type sp:Filter ;
912 + sp:expression
913 + [ rdf:type sp:ne ;
914 + sp:arg1 [ sp:varName "flowPurpose"^^xsd:string
915 + ] ;
916 + sp:arg2 <http://www.reportinghub.no/ep/schema/flow#Production>
917 + ]
918 + ] [ sp:object
919 + [ sp:varName "flowPurposeName"^^xsd:string
920 + ] ;
921 + sp:predicate rdfs:label ;
922 + sp:subject
923 + [ sp:varName "flowPurpose"^^xsd:string
924 + ]
925 + ] [ sp:object
926 + [ sp:varName "flowDefinition"^^xsd:string
927 + ] ;
928 + sp:predicate rdf:type ;
929 + sp:subject
930 + [ sp:varName "flowWhole"^^xsd:string
931 + ]
932 + ] [ sp:object <http://www.reportinghub.no/ep/schema/flow#ProductionFlowDefinitionType> ;
933 + sp:predicate rdf:type ;
934 + sp:subject
935 + [ sp:varName "flowDefinition"^^xsd:string
936 + ]
937 + ] [ sp:object
938 + [ sp:varName "flowDefinitionName"^^xsd:string
939 + ] ;
940 + sp:predicate rdfs:label ;
941 + sp:subject
942 + [ sp:varName "flowDefinition"^^xsd:string
943 + ]
944 + ] [ rdf:type sp:Optional ;
945 + sp:elements ([ sp:object
946 + [ sp:varName "temperature"^^xsd:string
947 + ] ;
948 + sp:predicate rdf:type ;
949 + sp:subject
950 + [ sp:varName "flow"^^xsd:string
951 + ]
952 + ] [ sp:object
953 + [ sp:varName "density"^^xsd:string
954 + ] ;
955 + sp:predicate rdf:type ;
956 + sp:subject
957 + [ sp:varName "flow"^^xsd:string
958 + ]
959 + ] [ sp:object
960 + [ sp:varName "pressure"^^xsd:string
961 + ] ;
962 + sp:predicate rdf:type ;
963 + sp:subject
964 + [ sp:varName "flow"^^xsd:string
965 + ]
966 + ] [ sp:object <http://www.reportinghub.no/ep/schema/core#Pressure> ;
967 + sp:predicate rdf:type ;
968 + sp:subject
969 + [ sp:varName "pressure"^^xsd:string
970 + ]
971 + ] [ sp:object <http://www.reportinghub.no/ep/schema/core#Density> ;
972 + sp:predicate rdf:type ;
973 + sp:subject
974 + [ sp:varName "density"^^xsd:string
975 + ]
976 + ] [ sp:object <http://www.reportinghub.no/ep/schema/core#Temperature> ;
977 + sp:predicate rdf:type ;
978 + sp:subject
979 + [ sp:varName "temperature"^^xsd:string
980 + ]
981 + ] [ rdf:type sp:Bind ;
982 + sp:expression
983 + [ rdf:type ep-spin-lib:normalizePropertyUnitAndValue ;
984 + sp:arg1 [ sp:varName "temperature"^^xsd:string
985 + ]
986 + ] ;
987 + sp:variable
988 + [ sp:varName "temperatureValue"^^xsd:string
989 + ]
990 + ] [ rdf:type sp:Bind ;
991 + sp:expression
992 + [ rdf:type ep-spin-lib:normalizePropertyUnitAndValue ;
993 + sp:arg1 [ sp:varName "pressure"^^xsd:string
994 + ]
995 + ] ;
996 + sp:variable
997 + [ sp:varName "pressureValue"^^xsd:string
998 + ]
999 + ] [ rdf:type sp:Bind ;
1000 + sp:expression
1001 + [ rdf:type ep-spin-lib:normalizePropertyUnitAndValue ;
1002 + sp:arg1 [ sp:varName "density"^^xsd:string
1003 + ]
1004 + ] ;
1005 + sp:variable
1006 + [ sp:varName "densityValue"^^xsd:string
1007 + ]
1008 + ])
1009 + ])
1010 + ] ;
1011 + rhspin:tableHeaders ("Field"^^xsd:string "Facility Name"^^xsd:string "Flow Purpose"^^xsd:string "Flow Definition"^^xsd:string "Flow Density"^^xsd:string "Flow Pressure"^^xsd:string "Flow Temperature"^^xsd:string) .
1012 +
782 dpr-tables:PersonnelInformation 1013 dpr-tables:PersonnelInformation
783 rdf:type rhspin:TableTemplate ; 1014 rdf:type rhspin:TableTemplate ;
784 rdfs:label "Personnel Information"^^xsd:string ; 1015 rdfs:label "Personnel Information"^^xsd:string ;
...@@ -801,98 +1032,648 @@ dpr-tables:PersonnelInformation ...@@ -801,98 +1032,648 @@ dpr-tables:PersonnelInformation
801 ] ; 1032 ] ;
802 sp:predicate <http://www.reportinghub.no/ep/schema/core#partOf> ; 1033 sp:predicate <http://www.reportinghub.no/ep/schema/core#partOf> ;
803 sp:subject 1034 sp:subject
804 - [ sp:varName "productionOperationReport"^^xsd:string 1035 + [ sp:varName "productionOperationReport"^^xsd:string
1036 + ]
1037 + ] [ sp:object <http://www.reportinghub.no/ep/schema/report#ProductionOperationReport> ;
1038 + sp:predicate rdf:type ;
1039 + sp:subject
1040 + [ sp:varName "productionOperationReport"^^xsd:string
1041 + ]
1042 + ] [ sp:object
1043 + [ sp:varName "temporalPartOfFacility"^^xsd:string
1044 + ] ;
1045 + sp:predicate <http://www.reportinghub.no/ep/schema/report#reportOn> ;
1046 + sp:subject
1047 + [ sp:varName "productionOperationReport"^^xsd:string
1048 + ]
1049 + ] [ sp:object
1050 + [ sp:varName "productionFacility"^^xsd:string
1051 + ] ;
1052 + sp:predicate <http://www.reportinghub.no/ep/schema/core#temporalPartOf> ;
1053 + sp:subject
1054 + [ sp:varName "temporalPartOfFacility"^^xsd:string
1055 + ]
1056 + ] [ sp:object <http://www.reportinghub.no/ep/schema/facility#Field> ;
1057 + sp:predicate rdf:type ;
1058 + sp:subject
1059 + [ sp:varName "productionFacility"^^xsd:string
1060 + ]
1061 + ] [ sp:object
1062 + [ sp:varName "facilityName"^^xsd:string
1063 + ] ;
1064 + sp:predicate <http://www.reportinghub.no/np/schema/npd#name> ;
1065 + sp:subject
1066 + [ sp:varName "productionFacility"^^xsd:string
1067 + ]
1068 + ] [ sp:object
1069 + [ sp:varName "productionOperationReport"^^xsd:string
1070 + ] ;
1071 + sp:predicate <http://www.reportinghub.no/ep/schema/core#partOf> ;
1072 + sp:subject
1073 + [ sp:varName "productionOperationInstallationReport"^^xsd:string
1074 + ]
1075 + ] [ sp:object <http://www.reportinghub.no/ep/schema/report#ProductionOperationInstallationReport> ;
1076 + sp:predicate rdf:type ;
1077 + sp:subject
1078 + [ sp:varName "productionOperationInstallationReport"^^xsd:string
1079 + ]
1080 + ] [ sp:object
1081 + [ sp:varName "installationPart"^^xsd:string
1082 + ] ;
1083 + sp:predicate <http://www.reportinghub.no/ep/schema/report#reportOn> ;
1084 + sp:subject
1085 + [ sp:varName "productionOperationInstallationReport"^^xsd:string
1086 + ]
1087 + ] [ sp:object
1088 + [ sp:varName "crew"^^xsd:string
1089 + ] ;
1090 + sp:predicate <http://www.reportinghub.no/ep/schema/organization#hasCrew> ;
1091 + sp:subject
1092 + [ sp:varName "installationPart"^^xsd:string
1093 + ]
1094 + ] [ sp:object
1095 + [ sp:varName "crewNumber"^^xsd:string
1096 + ] ;
1097 + sp:predicate <http://www.reportinghub.no/ep/schema/organization#numberInCrew> ;
1098 + sp:subject
1099 + [ sp:varName "crew"^^xsd:string
1100 + ]
1101 + ] [ sp:object
1102 + [ sp:varName "crewType"^^xsd:string
1103 + ] ;
1104 + sp:predicate rdf:type ;
1105 + sp:subject
1106 + [ sp:varName "crew"^^xsd:string
1107 + ]
1108 + ] [ sp:object <http://www.reportinghub.no/ep/schema/organization#CrewType> ;
1109 + sp:predicate rdf:type ;
1110 + sp:subject
1111 + [ sp:varName "crewType"^^xsd:string
1112 + ]
1113 + ] [ sp:object
1114 + [ sp:varName "crewTypename"^^xsd:string
1115 + ] ;
1116 + sp:predicate rdfs:label ;
1117 + sp:subject
1118 + [ sp:varName "crewType"^^xsd:string
1119 + ]
1120 + ])
1121 + ] ;
1122 + rhspin:tableHeaders ("Facility"^^xsd:string "Crew"^^xsd:string "Crew Type"^^xsd:string) .
1123 +
1124 +dpr-tables:ProductFlows
1125 + rdf:type rhspin:TableTemplate ;
1126 + rdfs:label "Product Flow Details"^^xsd:string ;
1127 + rdfs:subClassOf rhspin:DPRTableTemplates ;
1128 + spin:body
1129 + [ rdf:type sp:Select ;
1130 + sp:orderBy ([ sp:varName "flowInOutFacilityName"^^xsd:string
1131 + ] [ sp:varName "flowPurposeName"^^xsd:string
1132 + ] [ sp:varName "flowDefinitionName"^^xsd:string
1133 + ] [ sp:varName "productMaterialName"^^xsd:string
1134 + ]) ;
1135 + sp:resultVariables ([ sp:varName "containingWholeFacilityName"^^xsd:string
1136 + ] [ sp:varName "flowInOutFacilityName"^^xsd:string
1137 + ] [ sp:varName "flowPurposeName"^^xsd:string
1138 + ] [ sp:varName "flowDefinitionName"^^xsd:string
1139 + ] [ sp:varName "productMaterialName"^^xsd:string
1140 + ] [ sp:varName "densityValue"^^xsd:string
1141 + ] [ sp:varName "temperatureValue"^^xsd:string
1142 + ] [ sp:varName "pressureValue"^^xsd:string
1143 + ]) ;
1144 + sp:where ([ sp:object <http://www.reportinghub.no/ep/schema/report#ProductionReport> ;
1145 + sp:predicate rdf:type ;
1146 + sp:subject
1147 + [ sp:varName "report"^^xsd:string
1148 + ]
1149 + ] [ sp:object
1150 + [ sp:varName "report"^^xsd:string
1151 + ] ;
1152 + sp:predicate <http://www.reportinghub.no/ep/schema/core#partOf> ;
1153 + sp:subject
1154 + [ sp:varName "productvolumereport"^^xsd:string
1155 + ]
1156 + ] [ sp:object <http://www.reportinghub.no/ep/schema/report#ProductVolumeReport> ;
1157 + sp:predicate rdf:type ;
1158 + sp:subject
1159 + [ sp:varName "productvolumereport"^^xsd:string
1160 + ]
1161 + ] [ sp:object
1162 + [ sp:varName "productionflownetwork"^^xsd:string
1163 + ] ;
1164 + sp:predicate <http://www.reportinghub.no/ep/schema/report#reportOn> ;
1165 + sp:subject
1166 + [ sp:varName "productvolumereport"^^xsd:string
1167 + ]
1168 + ] [ sp:object <http://www.reportinghub.no/ep/schema/flow#ProductionFlowNetwork> ;
1169 + sp:predicate rdf:type ;
1170 + sp:subject
1171 + [ sp:varName "productionflownetwork"^^xsd:string
1172 + ]
1173 + ] [ sp:object
1174 + [ sp:varName "flow"^^xsd:string
1175 + ] ;
1176 + sp:predicate <http://www.reportinghub.no/ep/schema/flow#hasNetworkPart> ;
1177 + sp:subject
1178 + [ sp:varName "productionflownetwork"^^xsd:string
1179 + ]
1180 + ] [ sp:object <http://www.reportinghub.no/ep/schema/flow#ProductionFlow> ;
1181 + sp:predicate rdf:type ;
1182 + sp:subject
1183 + [ sp:varName "flow"^^xsd:string
1184 + ]
1185 + ] [ sp:object
1186 + [ sp:varName "productionflownetwork"^^xsd:string
1187 + ] ;
1188 + sp:predicate <http://www.reportinghub.no/ep/schema/flow#facilityContainsFlow> ;
1189 + sp:subject
1190 + [ sp:varName "productionflownetworkFacility"^^xsd:string
1191 + ]
1192 + ] [ sp:object
1193 + [ sp:varName "containingWholeFacility"^^xsd:string
1194 + ] ;
1195 + sp:predicate <http://www.reportinghub.no/ep/schema/core#temporalPartOf> ;
1196 + sp:subject
1197 + [ sp:varName "productionflownetworkFacility"^^xsd:string
1198 + ]
1199 + ] [ sp:object
1200 + [ sp:varName "containingWholeFacilityName"^^xsd:string
1201 + ] ;
1202 + sp:predicate <http://www.reportinghub.no/np/schema/npd#name> ;
1203 + sp:subject
1204 + [ sp:varName "containingWholeFacility"^^xsd:string
1205 + ]
1206 + ] [ sp:object
1207 + [ sp:varName "flowWhole"^^xsd:string
1208 + ] ;
1209 + sp:predicate <http://www.reportinghub.no/ep/schema/core#temporalPartOf> ;
1210 + sp:subject
1211 + [ sp:varName "flow"^^xsd:string
1212 + ]
1213 + ] [ sp:object <http://www.reportinghub.no/ep/schema/flow#WholeLifeProductionFlow> ;
1214 + sp:predicate rdf:type ;
1215 + sp:subject
1216 + [ sp:varName "flowWhole"^^xsd:string
1217 + ]
1218 + ] [ sp:object
1219 + [ sp:varName "flowInOutFacility"^^xsd:string
1220 + ] ;
1221 + sp:predicate <http://www.reportinghub.no/ep/schema/flow#flowIntoOrOutOf> ;
1222 + sp:subject
1223 + [ sp:varName "flowWhole"^^xsd:string
1224 + ]
1225 + ] [ rdf:type sp:TriplePath ;
1226 + sp:object
1227 + [ sp:varName "flowInOutFacilityName"^^xsd:string
1228 + ] ;
1229 + sp:path [ rdf:type sp:AltPath ;
1230 + sp:path1 <http://www.reportinghub.no/ep/schema/core#name> ;
1231 + sp:path2 <http://www.reportinghub.no/np/schema/npd#name>
1232 + ] ;
1233 + sp:subject
1234 + [ sp:varName "flowInOutFacility"^^xsd:string
1235 + ]
1236 + ] [ sp:object
1237 + [ sp:varName "flowPurpose"^^xsd:string
1238 + ] ;
1239 + sp:predicate rdf:type ;
1240 + sp:subject
1241 + [ sp:varName "flowWhole"^^xsd:string
1242 + ]
1243 + ] [ sp:object <http://www.reportinghub.no/ep/schema/flow#ProductionFlowPurposeType> ;
1244 + sp:predicate rdf:type ;
1245 + sp:subject
1246 + [ sp:varName "flowPurpose"^^xsd:string
1247 + ]
1248 + ] [ rdf:type sp:Filter ;
1249 + sp:expression
1250 + [ rdf:type sp:eq ;
1251 + sp:arg1 [ sp:varName "flowPurpose"^^xsd:string
1252 + ] ;
1253 + sp:arg2 <http://www.reportinghub.no/ep/schema/flow#Production>
1254 + ]
1255 + ] [ sp:object
1256 + [ sp:varName "flowPurposeName"^^xsd:string
1257 + ] ;
1258 + sp:predicate rdfs:label ;
1259 + sp:subject
1260 + [ sp:varName "flowPurpose"^^xsd:string
1261 + ]
1262 + ] [ sp:object
1263 + [ sp:varName "flowDefinition"^^xsd:string
1264 + ] ;
1265 + sp:predicate rdf:type ;
1266 + sp:subject
1267 + [ sp:varName "flowWhole"^^xsd:string
1268 + ]
1269 + ] [ sp:object <http://www.reportinghub.no/ep/schema/flow#ProductionFlowDefinitionType> ;
1270 + sp:predicate rdf:type ;
1271 + sp:subject
1272 + [ sp:varName "flowDefinition"^^xsd:string
1273 + ]
1274 + ] [ sp:object
1275 + [ sp:varName "flowDefinitionName"^^xsd:string
1276 + ] ;
1277 + sp:predicate rdfs:label ;
1278 + sp:subject
1279 + [ sp:varName "flowDefinition"^^xsd:string
1280 + ]
1281 + ] [ rdf:type sp:Optional ;
1282 + sp:elements ([ sp:object
1283 + [ sp:varName "productFlow"^^xsd:string
1284 + ] ;
1285 + sp:predicate <http://www.reportinghub.no/ep/schema/flow#hasMixedPart> ;
1286 + sp:subject
1287 + [ sp:varName "flow"^^xsd:string
1288 + ]
1289 + ] [ sp:object <http://www.reportinghub.no/ep/schema/flow#ProductFlow> ;
1290 + sp:predicate rdf:type ;
1291 + sp:subject
1292 + [ sp:varName "productFlow"^^xsd:string
1293 + ]
1294 + ] [ sp:object
1295 + [ sp:varName "productFlowWholeLife"^^xsd:string
1296 + ] ;
1297 + sp:predicate <http://www.reportinghub.no/ep/schema/core#temporalPartOf> ;
1298 + sp:subject
1299 + [ sp:varName "productFlow"^^xsd:string
1300 + ]
1301 + ] [ sp:object <http://www.reportinghub.no/ep/schema/flow#WholeLifeProductFlow> ;
1302 + sp:predicate rdf:type ;
1303 + sp:subject
1304 + [ sp:varName "productFlowWholeLife"^^xsd:string
1305 + ]
1306 + ] [ sp:object
1307 + [ sp:varName "productMaterialType"^^xsd:string
1308 + ] ;
1309 + sp:predicate rdf:type ;
1310 + sp:subject
1311 + [ sp:varName "productFlowWholeLife"^^xsd:string
1312 + ]
1313 + ] [ sp:object <http://www.reportinghub.no/ep/schema/flow#ProductMaterialType> ;
1314 + sp:predicate rdf:type ;
1315 + sp:subject
1316 + [ sp:varName "productMaterialType"^^xsd:string
1317 + ]
1318 + ] [ sp:object
1319 + [ sp:varName "productMaterialName"^^xsd:string
1320 + ] ;
1321 + sp:predicate rdfs:label ;
1322 + sp:subject
1323 + [ sp:varName "productMaterialType"^^xsd:string
1324 + ]
1325 + ] [ rdf:type sp:Optional ;
1326 + sp:elements ([ sp:object
1327 + [ sp:varName "pressure"^^xsd:string
1328 + ] ;
1329 + sp:predicate rdf:type ;
1330 + sp:subject
1331 + [ sp:varName "productFlow"^^xsd:string
1332 + ]
1333 + ] [ sp:object <http://www.reportinghub.no/ep/schema/core#Pressure> ;
1334 + sp:predicate rdf:type ;
1335 + sp:subject
1336 + [ sp:varName "pressure"^^xsd:string
1337 + ]
1338 + ] [ rdf:type sp:Bind ;
1339 + sp:expression
1340 + [ rdf:type ep-spin-lib:normalizePropertyUnitAndValue ;
1341 + sp:arg1 [ sp:varName "pressure"^^xsd:string
1342 + ]
1343 + ] ;
1344 + sp:variable
1345 + [ sp:varName "pressureValue"^^xsd:string
1346 + ]
1347 + ])
1348 + ] [ rdf:type sp:Optional ;
1349 + sp:elements ([ sp:object
1350 + [ sp:varName "temperature"^^xsd:string
1351 + ] ;
1352 + sp:predicate rdf:type ;
1353 + sp:subject
1354 + [ sp:varName "productFlow"^^xsd:string
1355 + ]
1356 + ] [ sp:object <http://www.reportinghub.no/ep/schema/core#Temperature> ;
1357 + sp:predicate rdf:type ;
1358 + sp:subject
1359 + [ sp:varName "temperature"^^xsd:string
1360 + ]
1361 + ] [ rdf:type sp:Bind ;
1362 + sp:expression
1363 + [ rdf:type ep-spin-lib:normalizePropertyUnitAndValue ;
1364 + sp:arg1 [ sp:varName "temperature"^^xsd:string
1365 + ]
1366 + ] ;
1367 + sp:variable
1368 + [ sp:varName "temperatureValue"^^xsd:string
1369 + ]
1370 + ])
1371 + ] [ rdf:type sp:Optional ;
1372 + sp:elements ([ sp:object
1373 + [ sp:varName "density"^^xsd:string
1374 + ] ;
1375 + sp:predicate rdf:type ;
1376 + sp:subject
1377 + [ sp:varName "productFlow"^^xsd:string
1378 + ]
1379 + ] [ sp:object <http://www.reportinghub.no/ep/schema/core#Density> ;
1380 + sp:predicate rdf:type ;
1381 + sp:subject
1382 + [ sp:varName "density"^^xsd:string
1383 + ]
1384 + ] [ rdf:type sp:Bind ;
1385 + sp:expression
1386 + [ rdf:type ep-spin-lib:normalizePropertyUnitAndValue ;
1387 + sp:arg1 [ sp:varName "density"^^xsd:string
1388 + ]
1389 + ] ;
1390 + sp:variable
1391 + [ sp:varName "densityValue"^^xsd:string
1392 + ]
1393 + ])
1394 + ])
1395 + ])
1396 + ] ;
1397 + rhspin:tableHeaders ("Field"^^xsd:string "Facility Name"^^xsd:string "Flow Purpose"^^xsd:string "Flow Definition"^^xsd:string "Material"^^xsd:string "Flow Density"^^xsd:string "Flow Temperature"^^xsd:string "Flow Pressure"^^xsd:string) .
1398 +
1399 +dpr-tables:ProductFlowsInjection
1400 + rdf:type rhspin:TableTemplate ;
1401 + rdfs:label "Injection Product Flow Details"^^xsd:string ;
1402 + rdfs:subClassOf rhspin:DPRTableTemplates ;
1403 + spin:body
1404 + [ rdf:type sp:Select ;
1405 + sp:orderBy ([ sp:varName "flowInOutFacilityName"^^xsd:string
1406 + ] [ sp:varName "flowPurposeName"^^xsd:string
1407 + ] [ sp:varName "flowDefinitionName"^^xsd:string
1408 + ] [ sp:varName "productMaterialName"^^xsd:string
1409 + ]) ;
1410 + sp:resultVariables ([ sp:varName "containingWholeFacilityName"^^xsd:string
1411 + ] [ sp:varName "flowInOutFacilityName"^^xsd:string
1412 + ] [ sp:varName "flowPurposeName"^^xsd:string
1413 + ] [ sp:varName "flowDefinitionName"^^xsd:string
1414 + ] [ sp:varName "productMaterialName"^^xsd:string
1415 + ] [ sp:varName "densityValue"^^xsd:string
1416 + ] [ sp:varName "temperatureValue"^^xsd:string
1417 + ] [ sp:varName "pressureValue"^^xsd:string
1418 + ]) ;
1419 + sp:where ([ sp:object <http://www.reportinghub.no/ep/schema/report#ProductionReport> ;
1420 + sp:predicate rdf:type ;
1421 + sp:subject
1422 + [ sp:varName "report"^^xsd:string
1423 + ]
1424 + ] [ sp:object
1425 + [ sp:varName "report"^^xsd:string
1426 + ] ;
1427 + sp:predicate <http://www.reportinghub.no/ep/schema/core#partOf> ;
1428 + sp:subject
1429 + [ sp:varName "productvolumereport"^^xsd:string
805 ] 1430 ]
806 - ] [ sp:object <http://www.reportinghub.no/ep/schema/report#ProductionOperationReport> ; 1431 + ] [ sp:object <http://www.reportinghub.no/ep/schema/report#ProductVolumeReport> ;
807 sp:predicate rdf:type ; 1432 sp:predicate rdf:type ;
808 sp:subject 1433 sp:subject
809 - [ sp:varName "productionOperationReport"^^xsd:string 1434 + [ sp:varName "productvolumereport"^^xsd:string
810 ] 1435 ]
811 ] [ sp:object 1436 ] [ sp:object
812 - [ sp:varName "temporalPartOfFacility"^^xsd:string 1437 + [ sp:varName "productionflownetwork"^^xsd:string
813 ] ; 1438 ] ;
814 sp:predicate <http://www.reportinghub.no/ep/schema/report#reportOn> ; 1439 sp:predicate <http://www.reportinghub.no/ep/schema/report#reportOn> ;
815 sp:subject 1440 sp:subject
816 - [ sp:varName "productionOperationReport"^^xsd:string 1441 + [ sp:varName "productvolumereport"^^xsd:string
1442 + ]
1443 + ] [ sp:object <http://www.reportinghub.no/ep/schema/flow#ProductionFlowNetwork> ;
1444 + sp:predicate rdf:type ;
1445 + sp:subject
1446 + [ sp:varName "productionflownetwork"^^xsd:string
817 ] 1447 ]
818 ] [ sp:object 1448 ] [ sp:object
819 - [ sp:varName "productionFacility"^^xsd:string 1449 + [ sp:varName "flow"^^xsd:string
820 ] ; 1450 ] ;
821 - sp:predicate <http://www.reportinghub.no/ep/schema/core#temporalPartOf> ; 1451 + sp:predicate <http://www.reportinghub.no/ep/schema/flow#hasNetworkPart> ;
822 sp:subject 1452 sp:subject
823 - [ sp:varName "temporalPartOfFacility"^^xsd:string 1453 + [ sp:varName "productionflownetwork"^^xsd:string
824 ] 1454 ]
825 - ] [ sp:object <http://www.reportinghub.no/ep/schema/facility#Field> ; 1455 + ] [ sp:object <http://www.reportinghub.no/ep/schema/flow#ProductionFlow> ;
826 sp:predicate rdf:type ; 1456 sp:predicate rdf:type ;
827 sp:subject 1457 sp:subject
828 - [ sp:varName "productionFacility"^^xsd:string 1458 + [ sp:varName "flow"^^xsd:string
829 ] 1459 ]
830 ] [ sp:object 1460 ] [ sp:object
831 - [ sp:varName "facilityName"^^xsd:string 1461 + [ sp:varName "productionflownetwork"^^xsd:string
1462 + ] ;
1463 + sp:predicate <http://www.reportinghub.no/ep/schema/flow#facilityContainsFlow> ;
1464 + sp:subject
1465 + [ sp:varName "productionflownetworkFacility"^^xsd:string
1466 + ]
1467 + ] [ sp:object
1468 + [ sp:varName "containingWholeFacility"^^xsd:string
1469 + ] ;
1470 + sp:predicate <http://www.reportinghub.no/ep/schema/core#temporalPartOf> ;
1471 + sp:subject
1472 + [ sp:varName "productionflownetworkFacility"^^xsd:string
1473 + ]
1474 + ] [ sp:object
1475 + [ sp:varName "containingWholeFacilityName"^^xsd:string
832 ] ; 1476 ] ;
833 sp:predicate <http://www.reportinghub.no/np/schema/npd#name> ; 1477 sp:predicate <http://www.reportinghub.no/np/schema/npd#name> ;
834 sp:subject 1478 sp:subject
835 - [ sp:varName "productionFacility"^^xsd:string 1479 + [ sp:varName "containingWholeFacility"^^xsd:string
836 ] 1480 ]
837 ] [ sp:object 1481 ] [ sp:object
838 - [ sp:varName "productionOperationReport"^^xsd:string 1482 + [ sp:varName "flowWhole"^^xsd:string
839 ] ; 1483 ] ;
840 - sp:predicate <http://www.reportinghub.no/ep/schema/core#partOf> ; 1484 + sp:predicate <http://www.reportinghub.no/ep/schema/core#temporalPartOf> ;
841 sp:subject 1485 sp:subject
842 - [ sp:varName "productionOperationInstallationReport"^^xsd:string 1486 + [ sp:varName "flow"^^xsd:string
843 ] 1487 ]
844 - ] [ sp:object <http://www.reportinghub.no/ep/schema/report#ProductionOperationInstallationReport> ; 1488 + ] [ sp:object <http://www.reportinghub.no/ep/schema/flow#WholeLifeProductionFlow> ;
845 sp:predicate rdf:type ; 1489 sp:predicate rdf:type ;
846 sp:subject 1490 sp:subject
847 - [ sp:varName "productionOperationInstallationReport"^^xsd:string 1491 + [ sp:varName "flowWhole"^^xsd:string
848 ] 1492 ]
849 ] [ sp:object 1493 ] [ sp:object
850 - [ sp:varName "installationPart"^^xsd:string 1494 + [ sp:varName "flowInOutFacility"^^xsd:string
851 ] ; 1495 ] ;
852 - sp:predicate <http://www.reportinghub.no/ep/schema/report#reportOn> ; 1496 + sp:predicate <http://www.reportinghub.no/ep/schema/flow#flowIntoOrOutOf> ;
853 sp:subject 1497 sp:subject
854 - [ sp:varName "productionOperationInstallationReport"^^xsd:string 1498 + [ sp:varName "flowWhole"^^xsd:string
1499 + ]
1500 + ] [ rdf:type sp:TriplePath ;
1501 + sp:object
1502 + [ sp:varName "flowInOutFacilityName"^^xsd:string
1503 + ] ;
1504 + sp:path [ rdf:type sp:AltPath ;
1505 + sp:path1 <http://www.reportinghub.no/ep/schema/core#name> ;
1506 + sp:path2 <http://www.reportinghub.no/np/schema/npd#name>
1507 + ] ;
1508 + sp:subject
1509 + [ sp:varName "flowInOutFacility"^^xsd:string
855 ] 1510 ]
856 ] [ sp:object 1511 ] [ sp:object
857 - [ sp:varName "crew"^^xsd:string 1512 + [ sp:varName "flowPurpose"^^xsd:string
858 ] ; 1513 ] ;
859 - sp:predicate <http://www.reportinghub.no/ep/schema/organization#hasCrew> ; 1514 + sp:predicate rdf:type ;
860 sp:subject 1515 sp:subject
861 - [ sp:varName "installationPart"^^xsd:string 1516 + [ sp:varName "flowWhole"^^xsd:string
1517 + ]
1518 + ] [ sp:object <http://www.reportinghub.no/ep/schema/flow#ProductionFlowPurposeType> ;
1519 + sp:predicate rdf:type ;
1520 + sp:subject
1521 + [ sp:varName "flowPurpose"^^xsd:string
1522 + ]
1523 + ] [ rdf:type sp:Filter ;
1524 + sp:expression
1525 + [ rdf:type sp:eq ;
1526 + sp:arg1 [ sp:varName "flowPurpose"^^xsd:string
1527 + ] ;
1528 + sp:arg2 <http://www.reportinghub.no/ep/schema/flow#Injection>
862 ] 1529 ]
863 ] [ sp:object 1530 ] [ sp:object
864 - [ sp:varName "crewNumber"^^xsd:string 1531 + [ sp:varName "flowPurposeName"^^xsd:string
865 ] ; 1532 ] ;
866 - sp:predicate <http://www.reportinghub.no/ep/schema/organization#numberInCrew> ; 1533 + sp:predicate rdfs:label ;
867 sp:subject 1534 sp:subject
868 - [ sp:varName "crew"^^xsd:string 1535 + [ sp:varName "flowPurpose"^^xsd:string
869 ] 1536 ]
870 ] [ sp:object 1537 ] [ sp:object
871 - [ sp:varName "crewType"^^xsd:string 1538 + [ sp:varName "flowDefinition"^^xsd:string
872 ] ; 1539 ] ;
873 sp:predicate rdf:type ; 1540 sp:predicate rdf:type ;
874 sp:subject 1541 sp:subject
875 - [ sp:varName "crew"^^xsd:string 1542 + [ sp:varName "flowWhole"^^xsd:string
876 ] 1543 ]
877 - ] [ sp:object <http://www.reportinghub.no/ep/schema/organization#CrewType> ; 1544 + ] [ sp:object <http://www.reportinghub.no/ep/schema/flow#ProductionFlowDefinitionType> ;
878 sp:predicate rdf:type ; 1545 sp:predicate rdf:type ;
879 sp:subject 1546 sp:subject
880 - [ sp:varName "crewType"^^xsd:string 1547 + [ sp:varName "flowDefinition"^^xsd:string
881 ] 1548 ]
882 ] [ sp:object 1549 ] [ sp:object
883 - [ sp:varName "crewTypename"^^xsd:string 1550 + [ sp:varName "flowDefinitionName"^^xsd:string
884 ] ; 1551 ] ;
885 sp:predicate rdfs:label ; 1552 sp:predicate rdfs:label ;
886 sp:subject 1553 sp:subject
887 - [ sp:varName "crewType"^^xsd:string 1554 + [ sp:varName "flowDefinition"^^xsd:string
1555 + ]
1556 + ] [ rdf:type sp:Optional ;
1557 + sp:elements ([ sp:object
1558 + [ sp:varName "productFlow"^^xsd:string
1559 + ] ;
1560 + sp:predicate <http://www.reportinghub.no/ep/schema/flow#hasMixedPart> ;
1561 + sp:subject
1562 + [ sp:varName "flow"^^xsd:string
1563 + ]
1564 + ] [ sp:object <http://www.reportinghub.no/ep/schema/flow#ProductFlow> ;
1565 + sp:predicate rdf:type ;
1566 + sp:subject
1567 + [ sp:varName "productFlow"^^xsd:string
1568 + ]
1569 + ] [ sp:object
1570 + [ sp:varName "productFlowWholeLife"^^xsd:string
1571 + ] ;
1572 + sp:predicate <http://www.reportinghub.no/ep/schema/core#temporalPartOf> ;
1573 + sp:subject
1574 + [ sp:varName "productFlow"^^xsd:string
1575 + ]
1576 + ] [ sp:object <http://www.reportinghub.no/ep/schema/flow#WholeLifeProductFlow> ;
1577 + sp:predicate rdf:type ;
1578 + sp:subject
1579 + [ sp:varName "productFlowWholeLife"^^xsd:string
1580 + ]
1581 + ] [ sp:object
1582 + [ sp:varName "productMaterialType"^^xsd:string
1583 + ] ;
1584 + sp:predicate rdf:type ;
1585 + sp:subject
1586 + [ sp:varName "productFlowWholeLife"^^xsd:string
1587 + ]
1588 + ] [ sp:object <http://www.reportinghub.no/ep/schema/flow#ProductMaterialType> ;
1589 + sp:predicate rdf:type ;
1590 + sp:subject
1591 + [ sp:varName "productMaterialType"^^xsd:string
1592 + ]
1593 + ] [ sp:object
1594 + [ sp:varName "productMaterialName"^^xsd:string
1595 + ] ;
1596 + sp:predicate rdfs:label ;
1597 + sp:subject
1598 + [ sp:varName "productMaterialType"^^xsd:string
1599 + ]
1600 + ] [ rdf:type sp:Optional ;
1601 + sp:elements ([ sp:object
1602 + [ sp:varName "pressure"^^xsd:string
1603 + ] ;
1604 + sp:predicate rdf:type ;
1605 + sp:subject
1606 + [ sp:varName "productFlow"^^xsd:string
1607 + ]
1608 + ] [ sp:object <http://www.reportinghub.no/ep/schema/core#Pressure> ;
1609 + sp:predicate rdf:type ;
1610 + sp:subject
1611 + [ sp:varName "pressure"^^xsd:string
1612 + ]
1613 + ] [ rdf:type sp:Bind ;
1614 + sp:expression
1615 + [ rdf:type ep-spin-lib:normalizePropertyUnitAndValue ;
1616 + sp:arg1 [ sp:varName "pressure"^^xsd:string
1617 + ]
1618 + ] ;
1619 + sp:variable
1620 + [ sp:varName "pressureValue"^^xsd:string
888 ] 1621 ]
889 ]) 1622 ])
1623 + ] [ rdf:type sp:Optional ;
1624 + sp:elements ([ sp:object
1625 + [ sp:varName "temperature"^^xsd:string
890 ] ; 1626 ] ;
891 - rhspin:tableHeaders ("Facility"^^xsd:string "Crew"^^xsd:string "Crew Type"^^xsd:string) . 1627 + sp:predicate rdf:type ;
1628 + sp:subject
1629 + [ sp:varName "productFlow"^^xsd:string
1630 + ]
1631 + ] [ sp:object <http://www.reportinghub.no/ep/schema/core#Temperature> ;
1632 + sp:predicate rdf:type ;
1633 + sp:subject
1634 + [ sp:varName "temperature"^^xsd:string
1635 + ]
1636 + ] [ rdf:type sp:Bind ;
1637 + sp:expression
1638 + [ rdf:type ep-spin-lib:normalizePropertyUnitAndValue ;
1639 + sp:arg1 [ sp:varName "temperature"^^xsd:string
1640 + ]
1641 + ] ;
1642 + sp:variable
1643 + [ sp:varName "temperatureValue"^^xsd:string
1644 + ]
1645 + ])
1646 + ] [ rdf:type sp:Optional ;
1647 + sp:elements ([ sp:object
1648 + [ sp:varName "density"^^xsd:string
1649 + ] ;
1650 + sp:predicate rdf:type ;
1651 + sp:subject
1652 + [ sp:varName "productFlow"^^xsd:string
1653 + ]
1654 + ] [ sp:object <http://www.reportinghub.no/ep/schema/core#Density> ;
1655 + sp:predicate rdf:type ;
1656 + sp:subject
1657 + [ sp:varName "density"^^xsd:string
1658 + ]
1659 + ] [ rdf:type sp:Bind ;
1660 + sp:expression
1661 + [ rdf:type ep-spin-lib:normalizePropertyUnitAndValue ;
1662 + sp:arg1 [ sp:varName "density"^^xsd:string
1663 + ]
1664 + ] ;
1665 + sp:variable
1666 + [ sp:varName "densityValue"^^xsd:string
1667 + ]
1668 + ])
1669 + ])
1670 + ])
1671 + ] ;
1672 + rhspin:tableHeaders ("Field"^^xsd:string "Facility Name"^^xsd:string "Flow Purpose"^^xsd:string "Flow Definition"^^xsd:string "Material"^^xsd:string "Flow Density"^^xsd:string "Flow Temperature"^^xsd:string "Flow Pressure"^^xsd:string) .
892 1673
893 -dpr-tables:ProductFlows 1674 +dpr-tables:ProductFlowsOther
894 rdf:type rhspin:TableTemplate ; 1675 rdf:type rhspin:TableTemplate ;
895 - rdfs:label "Product Flow Details"^^xsd:string ; 1676 + rdfs:label "Import, Export, Consumet and Other Product Flow Details"^^xsd:string ;
896 rdfs:subClassOf rhspin:DPRTableTemplates ; 1677 rdfs:subClassOf rhspin:DPRTableTemplates ;
897 spin:body 1678 spin:body
898 [ rdf:type sp:Select ; 1679 [ rdf:type sp:Select ;
...@@ -1014,6 +1795,20 @@ dpr-tables:ProductFlows ...@@ -1014,6 +1795,20 @@ dpr-tables:ProductFlows
1014 sp:subject 1795 sp:subject
1015 [ sp:varName "flowPurpose"^^xsd:string 1796 [ sp:varName "flowPurpose"^^xsd:string
1016 ] 1797 ]
1798 + ] [ rdf:type sp:Filter ;
1799 + sp:expression
1800 + [ rdf:type sp:eq ;
1801 + sp:arg1 [ sp:varName "flowPurpose"^^xsd:string
1802 + ] ;
1803 + sp:arg2 <http://www.reportinghub.no/ep/schema/flow#Injection>
1804 + ]
1805 + ] [ rdf:type sp:Filter ;
1806 + sp:expression
1807 + [ rdf:type sp:eq ;
1808 + sp:arg1 [ sp:varName "flowPurpose"^^xsd:string
1809 + ] ;
1810 + sp:arg2 <http://www.reportinghub.no/ep/schema/flow#Production>
1811 + ]
1017 ] [ sp:object 1812 ] [ sp:object
1018 [ sp:varName "flowPurposeName"^^xsd:string 1813 [ sp:varName "flowPurposeName"^^xsd:string
1019 ] ; 1814 ] ;
...@@ -1316,8 +2111,8 @@ dpr-tables:ProductionVolumes ...@@ -1316,8 +2111,8 @@ dpr-tables:ProductionVolumes
1316 rdfs:subClassOf rhspin:DPRTableTemplates ; 2111 rdfs:subClassOf rhspin:DPRTableTemplates ;
1317 spin:body 2112 spin:body
1318 [ rdf:type sp:Select ; 2113 [ rdf:type sp:Select ;
1319 - sp:orderBy ([ sp:varName "flowInOutFacilityName"^^xsd:string 2114 + sp:orderBy ([ sp:varName "flowPurposeName"^^xsd:string
1320 - ] [ sp:varName "flowPurposeName"^^xsd:string 2115 + ] [ sp:varName "flowInOutFacilityName"^^xsd:string
1321 ] [ sp:varName "flowDefinitionName"^^xsd:string 2116 ] [ sp:varName "flowDefinitionName"^^xsd:string
1322 ]) ; 2117 ]) ;
1323 sp:resultVariables ([ sp:varName "containingWholeFacilityName"^^xsd:string 2118 sp:resultVariables ([ sp:varName "containingWholeFacilityName"^^xsd:string
...@@ -1432,6 +2227,13 @@ dpr-tables:ProductionVolumes ...@@ -1432,6 +2227,13 @@ dpr-tables:ProductionVolumes
1432 sp:subject 2227 sp:subject
1433 [ sp:varName "flowPurpose"^^xsd:string 2228 [ sp:varName "flowPurpose"^^xsd:string
1434 ] 2229 ]
2230 + ] [ rdf:type sp:Filter ;
2231 + sp:expression
2232 + [ rdf:type sp:eq ;
2233 + sp:arg1 [ sp:varName "flowPurpose"^^xsd:string
2234 + ] ;
2235 + sp:arg2 <http://www.reportinghub.no/ep/schema/flow#Production>
2236 + ]
1435 ] [ sp:object 2237 ] [ sp:object
1436 [ sp:varName "flowPurposeName"^^xsd:string 2238 [ sp:varName "flowPurposeName"^^xsd:string
1437 ] ; 2239 ] ;
......
...@@ -55,9 +55,17 @@ WHERE { ...@@ -55,9 +55,17 @@ WHERE {
55 <dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:ProductionOperationActivity" /> 55 <dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:ProductionOperationActivity" />
56 56
57 <dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:ProductionVolumes" /> 57 <dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:ProductionVolumes" />
58 + <dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:ProductFlows" />
58 <dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:InjectionVolumes" /> 59 <dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:InjectionVolumes" />
60 + <dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:ProductFlowsInjection" />
61 +
62 +
63 + <dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:OtherVolumes" />
64 + <dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:ProductFlowsOther" />
65 +
66 +
67 +
59 68
60 - <dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:ProductFlows" />
61 69
62 70
63 71
......
1 +<?xml version="1.0" encoding="UTF-8" standalone="no"?><objects xmlns="http://www.epim.no/schemas/mprml/1" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" version="1.0(MPRML)"><documentInfo>
2 + <DocumentName namingSystem="EC">ÅSGARD March 2012</DocumentName>
3 + <DocumentAlias namingSystem="EC">ÅSGARD Copex Report</DocumentAlias>
4 + <DocumentDate>2012-03-06T00:00:00.0Z</DocumentDate>
5 + <documentClass namingSystem="EC">Statoil Petroleum AS</documentClass>
6 + <documentClass namingSystem="EC">DPR 2.0</documentClass>
7 + <documentClass namingSystem="ERH">dpr2</documentClass><FileCreationInformation>
8 +
9 + <FileCreationDate>2012-03-16T00:00:00.0Z</FileCreationDate>
10 +
11 + <SoftwareName>Energy Components</SoftwareName>
12 + <FileCreator>Statoil Petroleum AS</FileCreator>
13 + <Comment>NA</Comment>
14 + </FileCreationInformation>
15 + <Owner>Statoil Petroleum AS</Owner>
16 + </documentInfo><context xsi:type="obj_report">
17 + <kind>DPR 2.0</kind>
18 +
19 + <title>ÅSGARD</title>
20 + <date>2012-03-01</date>
21 + <dateEnd>2012-03-01</dateEnd>
22 + <month>2012-03</month>
23 + <year>2012</year>
24 + <reportVersion>1.2</reportVersion>
25 + <reportStatus>final</reportStatus>
26 + <installation kind="field" namingSystem="NPD" uidRef="43765">ÅSGARD</installation>
27 + <operator>
28 + <name>Statoil Petroleum AS</name>
29 + <role>Operating company</role>
30 + </operator>
31 + </context><object xsi:type="obj_productionOperation">
32 + <name>ÅSGARD operation report</name>
33 + <installation kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</installation>
34 + <periodKind>day</periodKind>
35 + <dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
36 + <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
37 + <operator>
38 + <name>Statoil Petroleum AS</name>
39 + <role>Operator</role>
40 + <personName>
41 + <prefix>Mr</prefix>
42 + <first>Test</first>
43 + <last>Dong</last>
44 + </personName>
45 + <address>
46 + <name>Statoil Petroleum AS</name>
47 + <street>Rosenberggate 99</street>
48 + <city>Stavanger</city>
49 + <country>Norway</country>
50 + <postalCode>4002</postalCode>
51 + </address>
52 + </operator>
53 + <title>ÅSGARD operation report</title>
54 + <geographicContext>
55 + <country>Norway</country>
56 + <field namingSystem="DONG">ÅSGARD</field>
57 +
58 + </geographicContext>
59 + <issueDate>2012-03-02</issueDate>
60 + <issuedBy>
61 + <name>Statoil Petroleum AS</name>
62 + <role>Operator</role>
63 + <personName>
64 + <prefix>Mr</prefix>
65 + <first>Test</first>
66 + <last>Dong</last>
67 + </personName>
68 + </issuedBy>
69 + <approvalDate>2012-03-02</approvalDate>
70 + <approver>
71 + <name>Statoil Petroleum AS</name>
72 + <role>Platformssjef</role>
73 + <personName>
74 + <prefix>Mr</prefix>
75 + <first>Test</first>
76 + <last>Dong</last>
77 + </personName>
78 + </approver>
79 + <installationReport uid="b13e8911-f359-11e1-a8ee-d067e534860e">
80 + <installation kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</installation>
81 + <bedsAvailable>10</bedsAvailable>
82 + <crewCount type="catering crew">1</crewCount>
83 + <crewCount type="contractor crew">4</crewCount>
84 + <crewCount type="own crew">5</crewCount>
85 + <work uom="h">23</work>
86 + <workMonthToDate uom="d">15</workMonthToDate>
87 + <workYearToDate uom="d">67</workYearToDate>
88 + <operationalHSE>
89 + <IncidentCount>1</IncidentCount>
90 + <sinceLostTime uom="d">10</sinceLostTime>
91 + <sincePreventionExercise uom="d">21</sincePreventionExercise>
92 + <sinceDefinedSituation uom="d">4</sinceDefinedSituation>
93 + <alarmCount>0</alarmCount>
94 + <safetyIntroCount>0</safetyIntroCount>
95 + <safetyDescription>It must be emphasized, once ag</safetyDescription>
96 + <safety>
97 + <meantimeIncident uom="d">0</meantimeIncident>
98 + <safetyCount period="day" type="lost time incident">1</safetyCount>
99 + <safetyCount period="day" type="sick on board">1</safetyCount>
100 + <comment>
101 + <dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
102 + <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
103 + <remark>Furthermore, an important property of these three types of EC is not to be considered in determining</remark>
104 + </comment>
105 + </safety>
106 + <weather>
107 + <dTim>2012-03-01T00:00:00.0Z</dTim>
108 + <agency>Weather agency</agency>
109 + <barometricPressure uom="Pa">58.32</barometricPressure>
110 + <beaufortScaleNumber>10</beaufortScaleNumber>
111 + <tempSurfaceMn uom="degC">15</tempSurfaceMn>
112 + <tempSurfaceMx uom="degC">19</tempSurfaceMx>
113 + <tempWindChill uom="degC">19</tempWindChill>
114 + <tempsea uom="degC">13</tempsea>
115 + <visibility uom="m">638</visibility>
116 + <aziWave uom="rad">1</aziWave>
117 + <htWave uom="m">5</htWave>
118 + <significantWave uom="m">3</significantWave>
119 + <maxWave uom="m">7</maxWave>
120 + <periodWave uom="s">6</periodWave>
121 + <aziWind uom="rad">4</aziWind>
122 + <velWind uom="m/s">6</velWind>
123 + <typePrecip>rain</typePrecip>
124 + <amtPrecip uom="m">5</amtPrecip>
125 + <coverCloud>459</coverCloud>
126 + <ceilingCloud uom="m">178</ceilingCloud>
127 + <currentSea uom="m/s">1</currentSea>
128 + <aziCurrentSea uom="rad">1</aziCurrentSea>
129 + <comments>For one thing, the appearance of parasitic gaps in domains relatively inaccessible to ordinary extra</comments>
130 + </weather>
131 +
132 + </operationalHSE>
133 +
134 + <productionActivity>
135 + <lostProduction>
136 + <volumeAndReason reasonLost="extended maint turnaround export" uom="m3">1515.91</volumeAndReason>
137 + <volumeAndReason reasonLost="extended maint turnaround" uom="m3">1407.18</volumeAndReason>
138 + <thirdPartyProcessing>
139 + <installation kind="platform">Ekofisk</installation>
140 + <oilStdTempPres uom="m3">1246.33</oilStdTempPres>
141 + <gasStdTempPres uom="m3">1897.53</gasStdTempPres>
142 + </thirdPartyProcessing>
143 +
144 + </lostProduction>
145 + <waterCleaningQuality>
146 + <samplePoint>Sample 1</samplePoint>
147 + <oilInWaterProduced uom="Euc">195.36</oilInWaterProduced>
148 + <amountOfOil uom="kg">109.73</amountOfOil>
149 + <ammonium uom="kg/m3">4.31</ammonium>
150 + <totalOrganicCarbon uom="Euc">91.2</totalOrganicCarbon>
151 + <phenol uom="kg/m3">95.62</phenol>
152 + <glycol uom="kg/m3">49.54</glycol>
153 + <phValue>6.17</phValue>
154 + <waterTemperature uom="degC">10.87</waterTemperature>
155 + <residualChloride uom="Euc">168.63</residualChloride>
156 + <oxygen uom="Euc">37.37</oxygen>
157 + <turbidity>118.69</turbidity>
158 + <coulterCounter uom="Euc">51.55</coulterCounter>
159 +
160 + <comment>
161 + <dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
162 + <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
163 + <remark>If the position of the trace in (99c) were only relatively inaccessible to movement, this selectiona</remark>
164 + </comment>
165 + </waterCleaningQuality>
166 + <shutdown>
167 + <installation kind="well">String</installation>
168 + <description>Preventive maintenance</description>
169 + <dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
170 + <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
171 + <volumetricDownTime uom="h">22</volumetricDownTime>
172 + <lossOilStdTempPres uom="m3">973.87</lossOilStdTempPres>
173 + <lossGasStdTempPres uom="m3">7360.4</lossGasStdTempPres>
174 + <activity>
175 + <dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
176 + <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
177 + <remark>It appears that the speaker-hearer's linguistic intuition cannot be arbitrary in the ultimate standa</remark>
178 + </activity>
179 +
180 + </shutdown>
181 +
182 + <alarm>
183 + <dTim>2012-03-01T00:00:00.0Z</dTim>
184 + <area>Area A</area>
185 + <type>Gas Alarm</type>
186 + <reason>Faulty alarm</reason>
187 + <comment>Nevertheless, the descriptive power of the base component raises serious doubts about a corpus of ut</comment>
188 + </alarm>
189 +
190 + <marineOperation>
191 + <dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
192 + <dTimEnd>2012-03-01T02:00:00.0Z</dTimEnd>
193 + <generalComment>Clearly, a descriptively adequate grammar is not quite equivalent to a general convention regarding </generalComment>
194 + <supplyShip>Supply 1</supplyShip>
195 + <standbyVessel>Standby 1</standbyVessel>
196 + <supplyShipComment>
197 +
198 + <dTimStart>2012-03-01T01:00:00.0Z</dTimStart>
199 + <dTimEnd>2012-03-01T06:00:00.0Z</dTimEnd>
200 + <remark>From C1, it follows that the speaker-hearer's linguistic intuition delimits the requirement that bra</remark>
201 + </supplyShipComment>
202 + <supplyShipComment>
203 +
204 + <dTimStart>2012-03-01T06:00:00.0Z</dTimStart>
205 + <dTimEnd>2012-03-01T08:00:00.0Z</dTimEnd>
206 + <remark>If the position of the trace in (99c) were only relatively inaccessible to movement, most of the met</remark>
207 + </supplyShipComment>
208 +
209 + <standbyVesselComment>
210 + <dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
211 + <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
212 + <remark>I suggested that these results would follow from the assumption that the theory of syntactic feature</remark>
213 + </standbyVesselComment>
214 +
215 + <basketMovement>
216 + <dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
217 + <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
218 + <remark>With this clarification, this selectionally introduced contextual feature raises serious doubts abou</remark>
219 + </basketMovement>
220 + <basketMovement>
221 + <dTimStart>2012-03-01T02:00:00.0Z</dTimStart>
222 + <dTimEnd>2012-03-01T04:00:00.0Z</dTimEnd>
223 + <remark>Notice, incidentally, that relational information delimits the extended c-command discussed in conne</remark>
224 + </basketMovement>
225 + <activity>
226 + <dTimStart>2012-03-01T06:00:00.0Z</dTimStart>
227 + <dTimEnd>2012-03-01T08:00:00.0Z</dTimEnd>
228 + <remark>I suggested that these results would follow from the assumption that the notion of level of grammati</remark>
229 + </activity>
230 + <activity>
231 + <dTimStart>2012-03-01T09:00:00.0Z</dTimStart>
232 + <dTimEnd>2012-03-01T11:00:00.0Z</dTimEnd>
233 + <remark>However, this assumption is not correct, since the descriptive power of the base component is necess</remark>
234 + </activity>
235 + </marineOperation>
236 +
237 + <cargoShipOperation>
238 + <vesselName>Cargo 1</vesselName>
239 + <dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
240 + <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
241 + <captain>Captain 1</captain>
242 + <cargo>Oil</cargo>
243 + <oilGrossStdTempPres uom="m3">6349.63</oilGrossStdTempPres>
244 + <oilGrossTotalStdTempPres uom="m3">6383.1</oilGrossTotalStdTempPres>
245 + <oilNetStdTempPres uom="m3">9682.53</oilNetStdTempPres>
246 + <oilNetMonthToDateStdTempPres uom="m3">6330.86</oilNetMonthToDateStdTempPres>
247 + <densityStdTempPres uom="kg/m3">720.98</densityStdTempPres>
248 +
249 + <rvp uom="Pa">167.33</rvp>
250 + <bsw uom="Euc">119.96</bsw>
251 + <salt uom="kg/m3">181.07</salt>
252 + <comment>
253 + <dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
254 + <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
255 + <remark>We will bring evidence in favor of the following thesis: relational information suffices to account </remark>
256 + </comment>
257 + <comment>
258 + <dTimStart>2012-03-01T01:00:00.0Z</dTimStart>
259 + <dTimEnd>2012-03-01T02:00:00.0Z</dTimEnd>
260 + <remark>I suggested that these results would follow from the assumption that the speaker-hearer's linguistic</remark>
261 + </comment>
262 + </cargoShipOperation>
263 + <operationalComment>
264 + <type>production</type>
265 + <dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
266 + <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
267 + <comment>To provide a constituent structure for T(Z,K), the speaker-hearer's linguistic intuition is rather d</comment>
268 + </operationalComment>
269 + <operationalComment>
270 + <type>production</type>
271 + <dTimStart>2012-03-01T06:00:00.0Z</dTimStart>
272 + <dTimEnd>2012-03-01T12:00:00.0Z</dTimEnd>
273 + <comment>From C1, it follows that the fundamental error of regarding functional notions as categorial appears</comment>
274 + </operationalComment>
275 + </productionActivity>
276 + </installationReport>
277 +</object><object xsi:type="obj_fluidSample">
278 + <name>TYRIHANS-LIQUID-CHARACTERISTICS-1</name>
279 + <sampleType>separator oil</sampleType>
280 + <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
281 + <acquisitionDate>2012-02-12</acquisitionDate>
282 + <customData>
283 + <extensionNameValue>
284 + <name>ValidFrom</name>
285 + <value>2012-02-12T00:00:00.0Z</value>
286 + <dataType>dateTime</dataType>
287 + </extensionNameValue>
288 + <extensionNameValue>
289 + <name>ValidTo</name>
290 + <value>2012-02-21T00:00:00.0Z</value>
291 + <dataType>dateTime</dataType>
292 + </extensionNameValue>
293 + </customData>
294 + </object><object xsi:type="obj_fluidSample">
295 + <name>TYRIHANS-GAS-CHARACTERISTICS-1</name>
296 + <sampleType>separator gas</sampleType>
297 + <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
298 + <acquisitionDate>2012-02-11</acquisitionDate>
299 + <customData>
300 + <extensionNameValue>
301 + <name>ValidFrom</name>
302 + <value>2012-02-11T00:00:00.0Z</value>
303 + <dataType>dateTime</dataType>
304 + </extensionNameValue>
305 + <extensionNameValue>
306 + <name>ValidTo</name>
307 + <value>2012-02-21T00:00:00.0Z</value>
308 + <dataType>dateTime</dataType>
309 + </extensionNameValue>
310 + </customData>
311 + </object><object xsi:type="obj_fluidSample">
312 + <name>TYRIHANS-LIQUID-CHARACTERISTICS-2</name>
313 + <sampleType>separator oil</sampleType>
314 + <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
315 + <acquisitionDate>2012-02-11</acquisitionDate>
316 + <customData>
317 + <extensionNameValue>
318 + <name>ValidFrom</name>
319 + <value>2012-02-11T00:00:00.0Z</value>
320 + <dataType>dateTime</dataType>
321 + </extensionNameValue>
322 + <extensionNameValue>
323 + <name>ValidTo</name>
324 + <value>2012-02-24T00:00:00.0Z</value>
325 + <dataType>dateTime</dataType>
326 + </extensionNameValue>
327 + </customData>
328 + </object><object xsi:type="obj_fluidSample">
329 + <name>TYRIHANS-GAS-CHARACTERISTICS-2</name>
330 + <sampleType>separator gas</sampleType>
331 + <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
332 + <acquisitionDate>2012-02-15</acquisitionDate>
333 + <customData>
334 + <extensionNameValue>
335 + <name>ValidFrom</name>
336 + <value>2012-02-15T00:00:00.0Z</value>
337 + <dataType>dateTime</dataType>
338 + </extensionNameValue>
339 + <extensionNameValue>
340 + <name>ValidTo</name>
341 + <value>2012-02-28T00:00:00.0Z</value>
342 + <dataType>dateTime</dataType>
343 + </extensionNameValue>
344 + </customData>
345 + </object><object xsi:type="obj_fluidSample">
346 + <name>TYRIHANS-LIQUID-CHARACTERISTICS-3</name>
347 + <sampleType>separator oil</sampleType>
348 + <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
349 + <acquisitionDate>2012-02-12</acquisitionDate>
350 + <customData>
351 + <extensionNameValue>
352 + <name>ValidFrom</name>
353 + <value>2012-02-12T00:00:00.0Z</value>
354 + <dataType>dateTime</dataType>
355 + </extensionNameValue>
356 + <extensionNameValue>
357 + <name>ValidTo</name>
358 + <value>2012-02-23T00:00:00.0Z</value>
359 + <dataType>dateTime</dataType>
360 + </extensionNameValue>
361 + </customData>
362 + </object><object xsi:type="obj_fluidSample">
363 + <name>TYRIHANS-GAS-CHARACTERISTICS-3</name>
364 + <sampleType>separator gas</sampleType>
365 + <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
366 + <acquisitionDate>2012-02-12</acquisitionDate>
367 + <customData>
368 + <extensionNameValue>
369 + <name>ValidFrom</name>
370 + <value>2012-02-12T00:00:00.0Z</value>
371 + <dataType>dateTime</dataType>
372 + </extensionNameValue>
373 + <extensionNameValue>
374 + <name>ValidTo</name>
375 + <value>2012-02-22T00:00:00.0Z</value>
376 + <dataType>dateTime</dataType>
377 + </extensionNameValue>
378 + </customData>
379 + </object><object xsi:type="obj_fluidSample">
380 + <name>TYRIHANS-LIQUID-CHARACTERISTICS-1</name>
381 + <sampleType>separator oil</sampleType>
382 + <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
383 + <acquisitionDate>2012-02-13</acquisitionDate>
384 + <customData>
385 + <extensionNameValue>
386 + <name>ValidFrom</name>
387 + <value>2012-02-13T00:00:00.0Z</value>
388 + <dataType>dateTime</dataType>
389 + </extensionNameValue>
390 + <extensionNameValue>
391 + <name>ValidTo</name>
392 + <value>2012-02-24T00:00:00.0Z</value>
393 + <dataType>dateTime</dataType>
394 + </extensionNameValue>
395 + </customData>
396 + </object><object xsi:type="obj_fluidSample">
397 + <name>TYRIHANS-GAS-CHARACTERISTICS-1</name>
398 + <sampleType>separator gas</sampleType>
399 + <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
400 + <acquisitionDate>2012-02-14</acquisitionDate>
401 + <customData>
402 + <extensionNameValue>
403 + <name>ValidFrom</name>
404 + <value>2012-02-14T00:00:00.0Z</value>
405 + <dataType>dateTime</dataType>
406 + </extensionNameValue>
407 + <extensionNameValue>
408 + <name>ValidTo</name>
409 + <value>2012-02-26T00:00:00.0Z</value>
410 + <dataType>dateTime</dataType>
411 + </extensionNameValue>
412 + </customData>
413 + </object><object xsi:type="obj_fluidSample">
414 + <name>TYRIHANS-LIQUID-CHARACTERISTICS-2</name>
415 + <sampleType>separator oil</sampleType>
416 + <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
417 + <acquisitionDate>2012-02-15</acquisitionDate>
418 + <customData>
419 + <extensionNameValue>
420 + <name>ValidFrom</name>
421 + <value>2012-02-15T00:00:00.0Z</value>
422 + <dataType>dateTime</dataType>
423 + </extensionNameValue>
424 + <extensionNameValue>
425 + <name>ValidTo</name>
426 + <value>2012-02-23T00:00:00.0Z</value>
427 + <dataType>dateTime</dataType>
428 + </extensionNameValue>
429 + </customData>
430 + </object><object xsi:type="obj_fluidSample">
431 + <name>TYRIHANS-GAS-CHARACTERISTICS-2</name>
432 + <sampleType>separator gas</sampleType>
433 + <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
434 + <acquisitionDate>2012-02-13</acquisitionDate>
435 + <customData>
436 + <extensionNameValue>
437 + <name>ValidFrom</name>
438 + <value>2012-02-13T00:00:00.0Z</value>
439 + <dataType>dateTime</dataType>
440 + </extensionNameValue>
441 + <extensionNameValue>
442 + <name>ValidTo</name>
443 + <value>2012-02-27T00:00:00.0Z</value>
444 + <dataType>dateTime</dataType>
445 + </extensionNameValue>
446 + </customData>
447 + </object><object xsi:type="obj_fluidSample">
448 + <name>TYRIHANS-LIQUID-CHARACTERISTICS-3</name>
449 + <sampleType>separator oil</sampleType>
450 + <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
451 + <acquisitionDate>2012-02-11</acquisitionDate>
452 + <customData>
453 + <extensionNameValue>
454 + <name>ValidFrom</name>
455 + <value>2012-02-11T00:00:00.0Z</value>
456 + <dataType>dateTime</dataType>
457 + </extensionNameValue>
458 + <extensionNameValue>
459 + <name>ValidTo</name>
460 + <value>2012-02-23T00:00:00.0Z</value>
461 + <dataType>dateTime</dataType>
462 + </extensionNameValue>
463 + </customData>
464 + </object><object xsi:type="obj_fluidSample">
465 + <name>TYRIHANS-GAS-CHARACTERISTICS-3</name>
466 + <sampleType>separator gas</sampleType>
467 + <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
468 + <acquisitionDate>2012-02-13</acquisitionDate>
469 + <customData>
470 + <extensionNameValue>
471 + <name>ValidFrom</name>
472 + <value>2012-02-13T00:00:00.0Z</value>
473 + <dataType>dateTime</dataType>
474 + </extensionNameValue>
475 + <extensionNameValue>
476 + <name>ValidTo</name>
477 + <value>2012-02-21T00:00:00.0Z</value>
478 + <dataType>dateTime</dataType>
479 + </extensionNameValue>
480 + </customData>
481 + </object><object xsi:type="obj_fluidSample">
482 + <name>TYRIHANS-LIQUID-CHARACTERISTICS-1</name>
483 + <sampleType>separator oil</sampleType>
484 + <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
485 + <acquisitionDate>2012-02-13</acquisitionDate>
486 + <customData>
487 + <extensionNameValue>
488 + <name>ValidFrom</name>
489 + <value>2012-02-13T00:00:00.0Z</value>
490 + <dataType>dateTime</dataType>
491 + </extensionNameValue>
492 + <extensionNameValue>
493 + <name>ValidTo</name>
494 + <value>2012-02-24T00:00:00.0Z</value>
495 + <dataType>dateTime</dataType>
496 + </extensionNameValue>
497 + </customData>
498 + </object><object xsi:type="obj_fluidSample">
499 + <name>TYRIHANS-GAS-CHARACTERISTICS-1</name>
500 + <sampleType>separator gas</sampleType>
501 + <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
502 + <acquisitionDate>2012-02-13</acquisitionDate>
503 + <customData>
504 + <extensionNameValue>
505 + <name>ValidFrom</name>
506 + <value>2012-02-13T00:00:00.0Z</value>
507 + <dataType>dateTime</dataType>
508 + </extensionNameValue>
509 + <extensionNameValue>
510 + <name>ValidTo</name>
511 + <value>2012-02-27T00:00:00.0Z</value>
512 + <dataType>dateTime</dataType>
513 + </extensionNameValue>
514 + </customData>
515 + </object><object xsi:type="obj_fluidSample">
516 + <name>TYRIHANS-LIQUID-CHARACTERISTICS-2</name>
517 + <sampleType>separator oil</sampleType>
518 + <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
519 + <acquisitionDate>2012-02-11</acquisitionDate>
520 + <customData>
521 + <extensionNameValue>
522 + <name>ValidFrom</name>
523 + <value>2012-02-11T00:00:00.0Z</value>
524 + <dataType>dateTime</dataType>
525 + </extensionNameValue>
526 + <extensionNameValue>
527 + <name>ValidTo</name>
528 + <value>2012-02-25T00:00:00.0Z</value>
529 + <dataType>dateTime</dataType>
530 + </extensionNameValue>
531 + </customData>
532 + </object><object xsi:type="obj_fluidSample">
533 + <name>TYRIHANS-GAS-CHARACTERISTICS-2</name>
534 + <sampleType>separator gas</sampleType>
535 + <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
536 + <acquisitionDate>2012-02-15</acquisitionDate>
537 + <customData>
538 + <extensionNameValue>
539 + <name>ValidFrom</name>
540 + <value>2012-02-15T00:00:00.0Z</value>
541 + <dataType>dateTime</dataType>
542 + </extensionNameValue>
543 + <extensionNameValue>
544 + <name>ValidTo</name>
545 + <value>2012-02-26T00:00:00.0Z</value>
546 + <dataType>dateTime</dataType>
547 + </extensionNameValue>
548 + </customData>
549 + </object><object xsi:type="obj_fluidSample">
550 + <name>TYRIHANS-LIQUID-CHARACTERISTICS-3</name>
551 + <sampleType>separator oil</sampleType>
552 + <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
553 + <acquisitionDate>2012-02-14</acquisitionDate>
554 + <customData>
555 + <extensionNameValue>
556 + <name>ValidFrom</name>
557 + <value>2012-02-14T00:00:00.0Z</value>
558 + <dataType>dateTime</dataType>
559 + </extensionNameValue>
560 + <extensionNameValue>
561 + <name>ValidTo</name>
562 + <value>2012-02-22T00:00:00.0Z</value>
563 + <dataType>dateTime</dataType>
564 + </extensionNameValue>
565 + </customData>
566 + </object><object xsi:type="obj_fluidSample">
567 + <name>TYRIHANS-GAS-CHARACTERISTICS-3</name>
568 + <sampleType>separator gas</sampleType>
569 + <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
570 + <acquisitionDate>2012-02-12</acquisitionDate>
571 + <customData>
572 + <extensionNameValue>
573 + <name>ValidFrom</name>
574 + <value>2012-02-12T00:00:00.0Z</value>
575 + <dataType>dateTime</dataType>
576 + </extensionNameValue>
577 + <extensionNameValue>
578 + <name>ValidTo</name>
579 + <value>2012-02-24T00:00:00.0Z</value>
580 + <dataType>dateTime</dataType>
581 + </extensionNameValue>
582 + </customData>
583 + </object><object xsi:type="obj_productVolume">
584 + <name>TYRIHANS</name>
585 + <installation kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</installation>
586 + <facility>
587 + <name kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</name>
588 + <facilityParent1 kind="block valve" namingSystem="String" uidRef="x">String</facilityParent1>
589 + <facilityParent2 kind="block valve" namingSystem="String" uidRef="x">String</facilityParent2>
590 + <facilityAlias namingSystem="String">String</facilityAlias>
591 + <facilityAlias namingSystem="String">String</facilityAlias>
592 + <contextFacility kind="block valve" namingSystem="String" uidRef="x">String</contextFacility>
593 + <contextFacility kind="block valve" namingSystem="String" uidRef="x">String</contextFacility>
594 +
595 +
596 + <downtimeReason uid="b15b5fde-f359-11e1-a318-d067e534860e">
597 + <who>MR Who</who>
598 + <role>Platform manager</role>
599 + <dTimStart>2012-03-01T02:00:00.0Z</dTimStart>
600 + <dTimEnd>2012-03-01T04:00:00.0Z</dTimEnd>
601 + <remark>Let us continue to suppose that any associated supporting element is unspecified with respect to an </remark>
602 + </downtimeReason>
603 + <downtimeReason uid="b15b86ee-f359-11e1-a386-d067e534860e">
604 + <who>Mr Who2</who>
605 + <role>Platform manager 2</role>
606 + <dTimStart>2012-03-01T06:00:00.0Z</dTimStart>
607 + <dTimEnd>2012-03-01T14:00:00.0Z</dTimEnd>
608 + <remark>It appears that the descriptive power of the base component does not readily tolerate an abstract un</remark>
609 + </downtimeReason>
610 + <flow>
611 + <kind>production</kind>
612 + <qualifier>saleable</qualifier>
613 + <version>2012-03-01T16:00:00.0Z</version>
614 + <versionSource>version src 71</versionSource>
615 + <gor uom="Euc">75.46</gor>
616 + <gorMTD uom="m3/m3">57.69</gorMTD>
617 + <waterConcMass uom="%">35.9</waterConcMass>
618 + <waterConcVol uom="ppm">86.59</waterConcVol>
619 + <atmosphere uom="Pa">28.71</atmosphere>
620 + <volumeValue>
621 + <volume status="bad calibration" uom="m3">834.26</volume>
622 + <grossCalorificValue uom="J/m3">613.16</grossCalorificValue>
623 + <temp uom="K">47.11</temp>
624 + <pres uom="Pa">12.89</pres>
625 + </volumeValue>
626 + <volume status="bad calibration" uom="m3">19.72</volume>
627 + <volumeStd status="bad calibration" uom="m3">89.01</volumeStd>
628 + <flowRate status="bad calibration" uom="m3/s">71.85</flowRate>
629 + <temp uom="K">98.42</temp>
630 + <pres uom="Pa">68.45</pres>
631 + <absoluteMinPres uom="Pa">29.8</absoluteMinPres>
632 + <portDiff uid="b15b86ef-f359-11e1-a5d7-d067e534860e">
633 + <port uidRef="b15b86f0-f359-11e1-9bf6-d067e534860e">Port 1</port>
634 + <presDiff uom="Pa">91.4</presDiff>
635 + <tempDiff uom="K">70.32</tempDiff>
636 + <chokeSize uom="in/32">68.22</chokeSize>
637 + <chokeRelative uom="%">95.71</chokeRelative>
638 + </portDiff>
639 + <portDiff uid="b15b86f1-f359-11e1-8fc8-d067e534860e">
640 + <port uidRef="b15b86f2-f359-11e1-8f01-d067e534860e">Port 2</port>
641 + <presDiff uom="Pa">97.94</presDiff>
642 + <tempDiff uom="K">98.68</tempDiff>
643 + <chokeSize uom="in/32">45.3</chokeSize>
644 + <chokeRelative uom="%">24.82</chokeRelative>
645 + </portDiff>
646 + <mass uom="kg">485.46</mass>
647 + <work uom="MJ">464.84</work>
648 + <efficiency uom="%">70.77</efficiency>
649 + <rvp uom="Pa">262.77</rvp>
650 + <tvp uom="bar">527.14</tvp>
651 + <bsw uom="%">80.9</bsw>
652 + <bswPrevious uom="m3/m3">18.13</bswPrevious>
653 + <densityValue>
654 + <density uom="kg/m3">34.68</density>
655 + <temp uom="K">48.15</temp>
656 + <pres uom="Pa">36.68</pres>
657 + </densityValue>
658 + <density uom="kg/m3">642.61</density>
659 + <densityFlowRate uom="Mg/a">495.01</densityFlowRate>
660 + <densityStd uom="kg/m3">303.76</densityStd>
661 + <concentration uom="ppm">49.74</concentration>
662 + <molecularWeight>42.55</molecularWeight>
663 + <weightPercent uom="%">67.96</weightPercent>
664 + <molePercent uom="%">41.57</molePercent>
665 + <moleAmt uom="kmol">98.22</moleAmt>
666 + <sg uom="Euc">87.09</sg>
667 + <hcDewpoint uom="K">229.53</hcDewpoint>
668 + <waterDewpoint uom="K">880.59</waterDewpoint>
669 + <wobbeIndex uom="J/m3">897.79</wobbeIndex>
670 + <grossCalorificValueStd uom="J/m3">27.92</grossCalorificValueStd>
671 + <rvpStabilizedCrude uom="Pa">574.9</rvpStabilizedCrude>
672 + <bswStabilizedCrude uom="Euc">541.59</bswStabilizedCrude>
673 + <densityStabilizedCrude uom="kg/m3">716.88</densityStabilizedCrude>
674 + <product>
675 + <kind>oil - net</kind>
676 + <name namingSystem="TEST954">Test product name 622</name>
677 + <splitFactor>0.65</splitFactor>
678 + <gor uom="Euc">98.73</gor>
679 + <gorMTD uom="m3/m3">84.85</gorMTD>
680 + <waterConcMass uom="%">73.24</waterConcMass>
681 + <waterConcVol uom="ppm">98.74</waterConcVol>
682 + <atmosphere uom="Pa">58.79</atmosphere>
683 + <volumeValue>
684 + <volume status="range limit" uom="m3">880.44</volume>
685 + <grossCalorificValue uom="J/m3">494.48</grossCalorificValue>
686 + <temp uom="K">75.73</temp>
687 + <pres uom="Pa">75.0</pres>
688 + </volumeValue>
689 + <volume status="bad calibration" uom="m3">44.97</volume>
690 + <volumeStd status="bad calibration" uom="m3">92.29</volumeStd>
691 + <flowRate status="bad calibration" uom="m3/s">62.29</flowRate>
692 + <temp uom="K">90.95</temp>
693 + <pres uom="Pa">27.05</pres>
694 + <absoluteMinPres uom="Pa">99.82</absoluteMinPres>
695 + <portDiff uid="b15bae00-f359-11e1-8073-d067e534860e">
696 + <port uidRef="b15bae01-f359-11e1-8368-d067e534860e">Port 1</port>
697 + <presDiff uom="Pa">26.55</presDiff>
698 + <tempDiff uom="K">70.35</tempDiff>
699 + <chokeSize uom="in/32">47.5</chokeSize>
700 + <chokeRelative uom="%">68.21</chokeRelative>
701 + </portDiff>
702 + <portDiff uid="b15bae02-f359-11e1-96c3-d067e534860e">
703 + <port uidRef="b15bae03-f359-11e1-a6c2-d067e534860e">Port 2</port>
704 + <presDiff uom="Pa">61.59</presDiff>
705 + <tempDiff uom="K">94.72</tempDiff>
706 + <chokeSize uom="in/32">75.58</chokeSize>
707 + <chokeRelative uom="%">44.09</chokeRelative>
708 + </portDiff>
709 + <mass uom="kg">388.85</mass>
710 + <work uom="MJ">154.17</work>
711 + <efficiency uom="%">70.62</efficiency>
712 + <rvp uom="Pa">684.1</rvp>
713 + <tvp uom="bar">419.71</tvp>
714 + <bsw uom="%">12.38</bsw>
715 + <bswPrevious uom="m3/m3">40.59</bswPrevious>
716 + <densityValue>
717 + <density uom="kg/m3">373.41</density>
718 + <temp uom="K">36.61</temp>
719 + <pres uom="Pa">80.1</pres>
720 + </densityValue>
721 + <density uom="kg/m3">419.96</density>
722 + <densityFlowRate uom="Mg/a">472.06</densityFlowRate>
723 + <densityStd uom="kg/m3">25.67</densityStd>
724 + <concentration uom="ppm">41.01</concentration>
725 + <molecularWeight>61.05</molecularWeight>
726 + <weightPercent uom="%">80.88</weightPercent>
727 + <molePercent uom="%">55.97</molePercent>
728 + <moleAmt uom="kmol">34.75</moleAmt>
729 + <sg uom="Euc">89.59</sg>
730 + <hcDewpoint uom="K">42.61</hcDewpoint>
731 + <waterDewpoint uom="K">861.58</waterDewpoint>
732 + <wobbeIndex uom="J/m3">994.75</wobbeIndex>
733 + <grossCalorificValueStd uom="J/m3">661.77</grossCalorificValueStd>
734 + <rvpStabilizedCrude uom="Pa">903.29</rvpStabilizedCrude>
735 + <bswStabilizedCrude uom="Euc">802.46</bswStabilizedCrude>
736 + <densityStabilizedCrude uom="kg/m3">732.34</densityStabilizedCrude>
737 + <componentContent uid="b15bae04-f359-11e1-928c-d067e534860e">
738 + <kind>diesel</kind>
739 + <referenceKind>aqueous</referenceKind>
740 + <gor uom="Euc">57.74</gor>
741 + <gorMTD uom="m3/m3">76.27</gorMTD>
742 + <waterConcMass uom="%">30.42</waterConcMass>
743 + <waterConcVol uom="ppm">43.48</waterConcVol>
744 + <atmosphere uom="Pa">17.04</atmosphere>
745 + <volumeValue>
746 + <volume status="device failure" uom="m3">825.44</volume>
747 + <grossCalorificValue uom="J/m3">928.39</grossCalorificValue>
748 + <temp uom="K">72.1</temp>
749 + <pres uom="Pa">65.0</pres>
750 + </volumeValue>
751 + <volume status="bad calibration" uom="m3">13.92</volume>
752 + <volumeStd status="bad calibration" uom="m3">30.25</volumeStd>
753 + <flowRate status="bad calibration" uom="m3/s">40.77</flowRate>
754 + <temp uom="K">21.06</temp>
755 + <pres uom="Pa">27.33</pres>
756 + <absoluteMinPres uom="Pa">17.25</absoluteMinPres>
757 + <portDiff uid="b15bd50f-f359-11e1-9159-d067e534860e">
758 + <port uidRef="b15bd510-f359-11e1-9333-d067e534860e">Port 1</port>
759 + <presDiff uom="Pa">19.8</presDiff>
760 + <tempDiff uom="K">24.95</tempDiff>
761 + <chokeSize uom="in/32">34.22</chokeSize>
762 + <chokeRelative uom="%">50.23</chokeRelative>
763 + </portDiff>
764 + <portDiff uid="b15bd511-f359-11e1-a2ee-d067e534860e">
765 + <port uidRef="b15bd512-f359-11e1-b5a7-d067e534860e">Port 2</port>
766 + <presDiff uom="Pa">25.76</presDiff>
767 + <tempDiff uom="K">29.53</tempDiff>
768 + <chokeSize uom="in/32">76.31</chokeSize>
769 + <chokeRelative uom="%">36.08</chokeRelative>
770 + </portDiff>
771 + <mass uom="kg">749.09</mass>
772 + <work uom="MJ">343.14</work>
773 + <efficiency uom="%">36.97</efficiency>
774 + <rvp uom="Pa">677.75</rvp>
775 + <tvp uom="bar">316.01</tvp>
776 + <bsw uom="%">82.71</bsw>
777 + <bswPrevious uom="m3/m3">54.68</bswPrevious>
778 + <densityValue>
779 + <density uom="kg/m3">425.32</density>
780 + <temp uom="K">13.6</temp>
781 + <pres uom="Pa">45.04</pres>
782 + </densityValue>
783 + <density uom="kg/m3">233.23</density>
784 + <densityFlowRate uom="Mg/a">329.23</densityFlowRate>
785 + <densityStd uom="kg/m3">487.14</densityStd>
786 + <concentration uom="ppm">37.94</concentration>
787 + <molecularWeight>47.64</molecularWeight>
788 + <weightPercent uom="%">84.25</weightPercent>
789 + <molePercent uom="%">83.28</molePercent>
790 + <moleAmt uom="kmol">42.97</moleAmt>
791 + <sg uom="Euc">41.5</sg>
792 + <hcDewpoint uom="K">790.71</hcDewpoint>
793 + <waterDewpoint uom="K">877.18</waterDewpoint>
794 + <wobbeIndex uom="J/m3">691.74</wobbeIndex>
795 + <grossCalorificValueStd uom="J/m3">667.72</grossCalorificValueStd>
796 + <rvpStabilizedCrude uom="Pa">114.98</rvpStabilizedCrude>
797 + <bswStabilizedCrude uom="Euc">61.25</bswStabilizedCrude>
798 + <densityStabilizedCrude uom="kg/m3">367.63</densityStabilizedCrude>
799 + </componentContent>
800 + <period>
801 + <kind>day</kind>
802 + <dateStart>2012-03-01</dateStart>
803 + <dateEnd>2012-03-01</dateEnd>
804 + <gor uom="Euc">52.02</gor>
805 + <gorMTD uom="m3/m3">59.95</gorMTD>
806 + <waterConcMass uom="%">37.44</waterConcMass>
807 + <waterConcVol uom="ppm">78.68</waterConcVol>
808 + <atmosphere uom="Pa">82.5</atmosphere>
809 + <volumeValue>
810 +
811 + <volume uom="m3">2696.85</volume><temp uom="degC">15</temp>
812 + <pres uom="atm">1</pres>
813 + </volumeValue>
814 + <volume status="bad calibration" uom="m3">43.45</volume>
815 + <volumeStd status="bad calibration" uom="m3">41.94</volumeStd>
816 + <flowRate status="bad calibration" uom="m3/s">30.44</flowRate>
817 + <temp uom="K">17.45</temp>
818 + <pres uom="Pa">60.12</pres>
819 + <absoluteMinPres uom="Pa">29.16</absoluteMinPres>
820 +
821 + <mass uom="kg">259.85</mass>
822 + <work uom="J">80.56</work>
823 + <efficiency uom="%">73.47</efficiency>
824 + <rvp uom="bar">964.46</rvp>
825 + <tvp uom="bar">759.53</tvp>
826 + <bsw uom="%">35.01</bsw>
827 + <bswPrevious uom="m3/m3">19.09</bswPrevious>
828 + <densityValue>
829 +
830 + <density uom="kg/m3">778.74</density>
831 + <temp uom="degC">15</temp>
832 + <pres uom="atm">1</pres>
833 + </densityValue>
834 + <density uom="kg/m3">637.68</density>
835 + <densityFlowRate uom="Mg/a">113.92</densityFlowRate>
836 + <densityStd uom="kg/m3">455.32</densityStd>
837 + <concentration uom="ppm">78.91</concentration>
838 + <molecularWeight>19.7</molecularWeight>
839 + <weightPercent uom="%">79.84</weightPercent>
840 + <molePercent uom="%">72.58</molePercent>
841 + <moleAmt uom="kmol">83.36</moleAmt>
842 + <sg uom="Euc">51.11</sg>
843 + <hcDewpoint uom="K">664.37</hcDewpoint>
844 + <waterDewpoint uom="K">105.18</waterDewpoint>
845 + <wobbeIndex uom="J/m3">847.7</wobbeIndex>
846 + <grossCalorificValueStd uom="J/m3">427.91</grossCalorificValueStd>
847 + <rvpStabilizedCrude uom="Pa">273.24</rvpStabilizedCrude>
848 + <bswStabilizedCrude uom="Euc">744.11</bswStabilizedCrude>
849 + <densityStabilizedCrude uom="kg/m3">859.26</densityStabilizedCrude>
850 + </period>
851 +
852 + </product>
853 + </flow>
854 +
855 +
856 +
857 + <flow>
858 + <kind>consume - fuel</kind>
859 + <qualifier>allocated</qualifier>
860 + <version>2012-03-01T01:00:00.0Z</version>
861 + <versionSource>version src 623</versionSource>
862 + <gor uom="Euc">68.83</gor>
863 + <gorMTD uom="m3/m3">97.3</gorMTD>
864 + <waterConcMass uom="%">98.72</waterConcMass>
865 + <waterConcVol uom="ppm">91.68</waterConcVol>
866 + <atmosphere uom="Pa">27.77</atmosphere>
867 + <volumeValue>
868 + <volume status="device failure" uom="m3">80.69</volume>
869 + <grossCalorificValue uom="J/m3">582.24</grossCalorificValue>
870 + <temp uom="K">74.63</temp>
871 + <pres uom="Pa">29.01</pres>
872 + </volumeValue>
873 + <volume status="bad calibration" uom="m3">20.84</volume>
874 + <volumeStd status="bad calibration" uom="m3">45.1</volumeStd>
875 + <flowRate status="bad calibration" uom="m3/s">48.81</flowRate>
876 + <temp uom="K">20.51</temp>
877 + <pres uom="Pa">48.91</pres>
878 + <absoluteMinPres uom="Pa">94.27</absoluteMinPres>
879 + <portDiff uid="b15bfc1e-f359-11e1-b6e9-d067e534860e">
880 + <port uidRef="b15bfc1f-f359-11e1-b41f-d067e534860e">Port 1</port>
881 + <presDiff uom="Pa">53.35</presDiff>
882 + <tempDiff uom="K">35.64</tempDiff>
883 + <chokeSize uom="in/32">95.67</chokeSize>
884 + <chokeRelative uom="%">88.74</chokeRelative>
885 + </portDiff>
886 + <portDiff uid="b15bfc20-f359-11e1-8833-d067e534860e">
887 + <port uidRef="b15bfc21-f359-11e1-86ec-d067e534860e">Port 2</port>
888 + <presDiff uom="Pa">81.34</presDiff>
889 + <tempDiff uom="K">79.54</tempDiff>
890 + <chokeSize uom="in/32">85.86</chokeSize>
891 + <chokeRelative uom="%">32.62</chokeRelative>
892 + </portDiff>
893 + <mass uom="kg">524.18</mass>
894 + <work uom="MJ">122.33</work>
895 + <efficiency uom="%">91.84</efficiency>
896 + <rvp uom="Pa">789.55</rvp>
897 + <tvp uom="bar">602.6</tvp>
898 + <bsw uom="%">22.89</bsw>
899 + <bswPrevious uom="m3/m3">49.54</bswPrevious>
900 + <densityValue>
901 + <density uom="kg/m3">506.75</density>
902 + <temp uom="K">26.87</temp>
903 + <pres uom="Pa">32.79</pres>
904 + </densityValue>
905 + <density uom="kg/m3">344.63</density>
906 + <densityFlowRate uom="Mg/a">229.21</densityFlowRate>
907 + <densityStd uom="kg/m3">522.81</densityStd>
908 + <concentration uom="ppm">72.37</concentration>
909 + <molecularWeight>52.41</molecularWeight>
910 + <weightPercent uom="%">67.02</weightPercent>
911 + <molePercent uom="%">62.95</molePercent>
912 + <moleAmt uom="kmol">77.62</moleAmt>
913 + <sg uom="Euc">25.65</sg>
914 + <hcDewpoint uom="K">339.47</hcDewpoint>
915 + <waterDewpoint uom="K">383.0</waterDewpoint>
916 + <wobbeIndex uom="J/m3">324.3</wobbeIndex>
917 + <grossCalorificValueStd uom="J/m3">913.96</grossCalorificValueStd>
918 + <rvpStabilizedCrude uom="Pa">237.3</rvpStabilizedCrude>
919 + <bswStabilizedCrude uom="Euc">289.09</bswStabilizedCrude>
920 + <densityStabilizedCrude uom="kg/m3">209.51</densityStabilizedCrude>
921 + <product>
922 + <kind>diesel</kind>
923 + <name namingSystem="TEST949">Test product name 536</name>
924 + <splitFactor>0.11</splitFactor>
925 + <gor uom="Euc">95.69</gor>
926 + <gorMTD uom="m3/m3">32.66</gorMTD>
927 + <waterConcMass uom="%">58.1</waterConcMass>
928 + <waterConcVol uom="ppm">19.2</waterConcVol>
929 + <atmosphere uom="Pa">92.1</atmosphere>
930 + <volumeValue>
931 + <volume status="range limit" uom="m3">366.3</volume>
932 + <grossCalorificValue uom="J/m3">570.6</grossCalorificValue>
933 + <temp uom="K">41.33</temp>
934 + <pres uom="Pa">50.99</pres>
935 + </volumeValue>
936 + <volume status="bad calibration" uom="m3">12.59</volume>
937 + <volumeStd status="bad calibration" uom="m3">63.05</volumeStd>
938 + <flowRate status="bad calibration" uom="m3/s">98.13</flowRate>
939 + <temp uom="K">68.37</temp>
940 + <pres uom="Pa">23.28</pres>
941 + <absoluteMinPres uom="Pa">92.22</absoluteMinPres>
942 + <portDiff uid="b15bfc22-f359-11e1-af66-d067e534860e">
943 + <port uidRef="b15bfc23-f359-11e1-b17d-d067e534860e">Port 1</port>
944 + <presDiff uom="Pa">33.31</presDiff>
945 + <tempDiff uom="K">84.21</tempDiff>
946 + <chokeSize uom="in/32">13.44</chokeSize>
947 + <chokeRelative uom="%">97.63</chokeRelative>
948 + </portDiff>
949 + <portDiff uid="b15c2330-f359-11e1-add9-d067e534860e">
950 + <port uidRef="b15c2331-f359-11e1-ad46-d067e534860e">Port 2</port>
951 + <presDiff uom="Pa">75.85</presDiff>
952 + <tempDiff uom="K">89.75</tempDiff>
953 + <chokeSize uom="in/32">40.06</chokeSize>
954 + <chokeRelative uom="%">70.16</chokeRelative>
955 + </portDiff>
956 + <mass uom="kg">733.99</mass>
957 + <work uom="MJ">835.71</work>
958 + <efficiency uom="%">70.64</efficiency>
959 + <rvp uom="Pa">675.65</rvp>
960 + <tvp uom="bar">532.88</tvp>
961 + <bsw uom="%">38.79</bsw>
962 + <bswPrevious uom="m3/m3">32.91</bswPrevious>
963 + <densityValue>
964 + <density uom="kg/m3">35.09</density>
965 + <temp uom="K">56.34</temp>
966 + <pres uom="Pa">76.01</pres>
967 + </densityValue>
968 + <density uom="kg/m3">160.37</density>
969 + <densityFlowRate uom="Mg/a">420.95</densityFlowRate>
970 + <densityStd uom="kg/m3">548.86</densityStd>
971 + <concentration uom="ppm">25.46</concentration>
972 + <molecularWeight>76.55</molecularWeight>
973 + <weightPercent uom="%">32.03</weightPercent>
974 + <molePercent uom="%">90.69</molePercent>
975 + <moleAmt uom="kmol">82.36</moleAmt>
976 + <sg uom="Euc">22.8</sg>
977 + <hcDewpoint uom="K">986.14</hcDewpoint>
978 + <waterDewpoint uom="K">490.97</waterDewpoint>
979 + <wobbeIndex uom="J/m3">215.6</wobbeIndex>
980 + <grossCalorificValueStd uom="J/m3">939.64</grossCalorificValueStd>
981 + <rvpStabilizedCrude uom="Pa">62.37</rvpStabilizedCrude>
982 + <bswStabilizedCrude uom="Euc">580.57</bswStabilizedCrude>
983 + <densityStabilizedCrude uom="kg/m3">445.39</densityStabilizedCrude>
984 + <componentContent uid="b15c2332-f359-11e1-be17-d067e534860e">
985 + <kind>C6-</kind>
986 + <referenceKind>propane</referenceKind>
987 + <gor uom="Euc">94.3</gor>
988 + <gorMTD uom="m3/m3">49.21</gorMTD>
989 + <waterConcMass uom="%">42.65</waterConcMass>
990 + <waterConcVol uom="ppm">95.55</waterConcVol>
991 + <atmosphere uom="Pa">98.22</atmosphere>
992 + <volumeValue>
993 + <volume status="range limit" uom="m3">872.16</volume>
994 + <grossCalorificValue uom="J/m3">292.66</grossCalorificValue>
995 + <temp uom="K">30.17</temp>
996 + <pres uom="Pa">87.79</pres>
997 + </volumeValue>
998 + <volume status="bad calibration" uom="m3">36.67</volume>
999 + <volumeStd status="bad calibration" uom="m3">83.65</volumeStd>
1000 + <flowRate status="bad calibration" uom="m3/s">47.6</flowRate>
1001 + <temp uom="K">59.59</temp>
1002 + <pres uom="Pa">74.77</pres>
1003 + <absoluteMinPres uom="Pa">50.9</absoluteMinPres>
1004 + <portDiff uid="b15c2333-f359-11e1-bf87-d067e534860e">
1005 + <port uidRef="b15c2334-f359-11e1-b1b1-d067e534860e">Port 1</port>
1006 + <presDiff uom="Pa">10.46</presDiff>
1007 + <tempDiff uom="K">82.76</tempDiff>
1008 + <chokeSize uom="in/32">15.31</chokeSize>
1009 + <chokeRelative uom="%">45.42</chokeRelative>
1010 + </portDiff>
1011 + <portDiff uid="b15c2335-f359-11e1-8296-d067e534860e">
1012 + <port uidRef="b15c2336-f359-11e1-af3c-d067e534860e">Port 2</port>
1013 + <presDiff uom="Pa">20.64</presDiff>
1014 + <tempDiff uom="K">24.55</tempDiff>
1015 + <chokeSize uom="in/32">90.41</chokeSize>
1016 + <chokeRelative uom="%">13.97</chokeRelative>
1017 + </portDiff>
1018 + <mass uom="kg">486.03</mass>
1019 + <work uom="MJ">667.54</work>
1020 + <efficiency uom="%">55.01</efficiency>
1021 + <rvp uom="Pa">539.8</rvp>
1022 + <tvp uom="bar">983.91</tvp>
1023 + <bsw uom="%">85.95</bsw>
1024 + <bswPrevious uom="m3/m3">69.42</bswPrevious>
1025 + <densityValue>
1026 + <density uom="kg/m3">83.37</density>
1027 + <temp uom="K">27.62</temp>
1028 + <pres uom="Pa">74.95</pres>
1029 + </densityValue>
1030 + <density uom="kg/m3">431.44</density>
1031 + <densityFlowRate uom="Mg/a">462.15</densityFlowRate>
1032 + <densityStd uom="kg/m3">75.11</densityStd>
1033 + <concentration uom="ppm">15.2</concentration>
1034 + <molecularWeight>83.02</molecularWeight>
1035 + <weightPercent uom="%">28.9</weightPercent>
1036 + <molePercent uom="%">40.99</molePercent>
1037 + <moleAmt uom="kmol">18.78</moleAmt>
1038 + <sg uom="Euc">69.2</sg>
1039 + <hcDewpoint uom="K">535.24</hcDewpoint>
1040 + <waterDewpoint uom="K">51.07</waterDewpoint>
1041 + <wobbeIndex uom="J/m3">514.25</wobbeIndex>
1042 + <grossCalorificValueStd uom="J/m3">378.36</grossCalorificValueStd>
1043 + <rvpStabilizedCrude uom="Pa">379.58</rvpStabilizedCrude>
1044 + <bswStabilizedCrude uom="Euc">832.23</bswStabilizedCrude>
1045 + <densityStabilizedCrude uom="kg/m3">895.99</densityStabilizedCrude>
1046 + </componentContent>
1047 + <period>
1048 + <kind>day</kind>
1049 + <dateStart>2012-03-01</dateStart>
1050 + <dateEnd>2012-03-01</dateEnd>
1051 + <gor uom="Euc">40.37</gor>
1052 + <gorMTD uom="m3/m3">63.45</gorMTD>
1053 + <waterConcMass uom="%">24.23</waterConcMass>
1054 + <waterConcVol uom="ppm">54.56</waterConcVol>
1055 + <atmosphere uom="Pa">23.37</atmosphere>
1056 +
1057 + <volumeValue>
1058 + <volume uom="L">249.11</volume>
1059 + <temp uom="degC">15</temp>
1060 + <pres uom="atm">1</pres>
1061 + </volumeValue><volume status="bad calibration" uom="m3">58.75</volume>
1062 + <volumeStd status="bad calibration" uom="m3">93.65</volumeStd>
1063 + <flowRate status="bad calibration" uom="m3/s">87.15</flowRate>
1064 + <temp uom="K">65.52</temp>
1065 + <pres uom="Pa">53.15</pres>
1066 + <absoluteMinPres uom="Pa">84.14</absoluteMinPres>
1067 +
1068 +
1069 + <work uom="MJ">234.84</work>
1070 + <efficiency uom="%">12.61</efficiency>
1071 + <rvp uom="atm">792.71</rvp>
1072 + <tvp uom="bar">845.1</tvp>
1073 + <bsw uom="%">70.53</bsw>
1074 + <bswPrevious uom="m3/m3">55.6</bswPrevious>
1075 +
1076 + <density uom="kg/m3">49.43</density>
1077 + <densityFlowRate uom="Mg/a">11.75</densityFlowRate>
1078 + <densityStd uom="kg/m3">442.26</densityStd>
1079 + <concentration uom="ppm">77.98</concentration>
1080 + <molecularWeight>51.9</molecularWeight>
1081 + <weightPercent uom="%">12.04</weightPercent>
1082 + <molePercent uom="%">89.37</molePercent>
1083 + <moleAmt uom="kmol">71.28</moleAmt>
1084 + <sg uom="Euc">76.78</sg>
1085 + <hcDewpoint uom="K">938.49</hcDewpoint>
1086 + <waterDewpoint uom="K">424.25</waterDewpoint>
1087 + <wobbeIndex uom="J/m3">409.88</wobbeIndex>
1088 + <grossCalorificValueStd uom="J/m3">543.05</grossCalorificValueStd>
1089 + <rvpStabilizedCrude uom="Pa">375.31</rvpStabilizedCrude>
1090 + <bswStabilizedCrude uom="Euc">619.48</bswStabilizedCrude>
1091 + <densityStabilizedCrude uom="kg/m3">857.5</densityStabilizedCrude>
1092 + </period>
1093 +
1094 + </product>
1095 + </flow>
1096 +
1097 +
1098 +
1099 +
1100 + </facility><facility>
1101 + <name kind="compressor" namingSystem="STATOIL" uidRef="NaN">TYRIHANS compressor</name>
1102 + <facilityParent1 kind="block valve" namingSystem="String" uidRef="x">String</facilityParent1>
1103 + <facilityParent2 kind="block valve" namingSystem="String" uidRef="x">String</facilityParent2>
1104 + <facilityAlias namingSystem="String">String</facilityAlias>
1105 + <facilityAlias namingSystem="String">String</facilityAlias>
1106 + <contextFacility kind="block valve" namingSystem="String" uidRef="x">String</contextFacility>
1107 + <contextFacility kind="block valve" namingSystem="String" uidRef="x">String</contextFacility>
1108 +
1109 +
1110 +
1111 + <flow>
1112 + <kind>production</kind>
1113 + <qualifier>metered - fiscal</qualifier>
1114 + <version>2012-03-01T11:00:00.0Z</version>
1115 + <versionSource>version src 707</versionSource>
1116 + <gor uom="Euc">40.29</gor>
1117 + <gorMTD uom="m3/m3">58.4</gorMTD>
1118 + <waterConcMass uom="%">46.58</waterConcMass>
1119 + <waterConcVol uom="ppm">81.28</waterConcVol>
1120 + <atmosphere uom="Pa">60.96</atmosphere>
1121 + <volumeValue>
1122 + <volume status="device failure" uom="m3">846.9</volume>
1123 + <grossCalorificValue uom="J/m3">828.79</grossCalorificValue>
1124 + <temp uom="K">86.07</temp>
1125 + <pres uom="Pa">52.18</pres>
1126 + </volumeValue>
1127 + <volume status="bad calibration" uom="m3">42.06</volume>
1128 + <volumeStd status="bad calibration" uom="m3">54.54</volumeStd>
1129 + <flowRate status="bad calibration" uom="m3/s">10.81</flowRate>
1130 + <temp uom="K">24.9</temp>
1131 + <pres uom="Pa">56.33</pres>
1132 + <absoluteMinPres uom="Pa">75.4</absoluteMinPres>
1133 + <portDiff uid="b15c4a40-f359-11e1-b743-d067e534860e">
1134 + <port uidRef="b15c4a41-f359-11e1-9645-d067e534860e">Port 1</port>
1135 + <presDiff uom="Pa">11.59</presDiff>
1136 + <tempDiff uom="K">87.23</tempDiff>
1137 + <chokeSize uom="in/32">22.03</chokeSize>
1138 + <chokeRelative uom="%">54.32</chokeRelative>
1139 + </portDiff>
1140 + <portDiff uid="b15c4a42-f359-11e1-b241-d067e534860e">
1141 + <port uidRef="b15c714f-f359-11e1-b6b7-d067e534860e">Port 2</port>
1142 + <presDiff uom="Pa">88.87</presDiff>
1143 + <tempDiff uom="K">12.18</tempDiff>
1144 + <chokeSize uom="in/32">43.28</chokeSize>
1145 + <chokeRelative uom="%">33.13</chokeRelative>
1146 + </portDiff>
1147 + <mass uom="kg">809.05</mass>
1148 + <work uom="MJ">900.5</work>
1149 + <efficiency uom="%">65.19</efficiency>
1150 + <rvp uom="Pa">684.25</rvp>
1151 + <tvp uom="bar">160.2</tvp>
1152 + <bsw uom="%">14.44</bsw>
1153 + <bswPrevious uom="m3/m3">72.93</bswPrevious>
1154 + <densityValue>
1155 + <density uom="kg/m3">366.4</density>
1156 + <temp uom="K">42.15</temp>
1157 + <pres uom="Pa">48.97</pres>
1158 + </densityValue>
1159 + <density uom="kg/m3">110.37</density>
1160 + <densityFlowRate uom="Mg/a">245.46</densityFlowRate>
1161 + <densityStd uom="kg/m3">383.66</densityStd>
1162 + <concentration uom="ppm">59.27</concentration>
1163 + <molecularWeight>43.35</molecularWeight>
1164 + <weightPercent uom="%">74.89</weightPercent>
1165 + <molePercent uom="%">46.25</molePercent>
1166 + <moleAmt uom="kmol">74.51</moleAmt>
1167 + <sg uom="Euc">37.67</sg>
1168 + <hcDewpoint uom="K">553.35</hcDewpoint>
1169 + <waterDewpoint uom="K">747.77</waterDewpoint>
1170 + <wobbeIndex uom="J/m3">705.92</wobbeIndex>
1171 + <grossCalorificValueStd uom="J/m3">560.47</grossCalorificValueStd>
1172 + <rvpStabilizedCrude uom="Pa">143.03</rvpStabilizedCrude>
1173 + <bswStabilizedCrude uom="Euc">747.63</bswStabilizedCrude>
1174 + <densityStabilizedCrude uom="kg/m3">286.01</densityStabilizedCrude>
1175 + <product>
1176 + <kind>oil - net</kind>
1177 + <name namingSystem="TEST604">Test product name 986</name>
1178 + <splitFactor>0.68</splitFactor>
1179 + <gor uom="Euc">54.19</gor>
1180 + <gorMTD uom="m3/m3">82.24</gorMTD>
1181 + <waterConcMass uom="%">68.88</waterConcMass>
1182 + <waterConcVol uom="ppm">51.45</waterConcVol>
1183 + <atmosphere uom="Pa">13.95</atmosphere>
1184 + <volumeValue>
1185 + <volume status="sensor failure" uom="m3">593.81</volume>
1186 + <grossCalorificValue uom="J/m3">175.09</grossCalorificValue>
1187 + <temp uom="K">35.96</temp>
1188 + <pres uom="Pa">64.45</pres>
1189 + </volumeValue>
1190 + <volume status="bad calibration" uom="m3">37.51</volume>
1191 + <volumeStd status="bad calibration" uom="m3">15.96</volumeStd>
1192 + <flowRate status="bad calibration" uom="m3/s">13.5</flowRate>
1193 + <temp uom="K">87.42</temp>
1194 + <pres uom="Pa">68.02</pres>
1195 + <absoluteMinPres uom="Pa">84.66</absoluteMinPres>
1196 + <portDiff uid="b15c7150-f359-11e1-82e3-d067e534860e">
1197 + <port uidRef="b15c7151-f359-11e1-bcb2-d067e534860e">Port 1</port>
1198 + <presDiff uom="Pa">29.49</presDiff>
1199 + <tempDiff uom="K">77.67</tempDiff>
1200 + <chokeSize uom="in/32">30.56</chokeSize>
1201 + <chokeRelative uom="%">37.53</chokeRelative>
1202 + </portDiff>
1203 + <portDiff uid="b15c7152-f359-11e1-a8b9-d067e534860e">
1204 + <port uidRef="b15c7153-f359-11e1-81ac-d067e534860e">Port 2</port>
1205 + <presDiff uom="Pa">42.83</presDiff>
1206 + <tempDiff uom="K">54.87</tempDiff>
1207 + <chokeSize uom="in/32">85.52</chokeSize>
1208 + <chokeRelative uom="%">34.61</chokeRelative>
1209 + </portDiff>
1210 + <mass uom="kg">610.56</mass>
1211 + <work uom="MJ">128.67</work>
1212 + <efficiency uom="%">39.84</efficiency>
1213 + <rvp uom="Pa">424.75</rvp>
1214 + <tvp uom="bar">57.28</tvp>
1215 + <bsw uom="%">75.21</bsw>
1216 + <bswPrevious uom="m3/m3">45.62</bswPrevious>
1217 + <densityValue>
1218 + <density uom="kg/m3">614.43</density>
1219 + <temp uom="K">44.32</temp>
1220 + <pres uom="Pa">11.68</pres>
1221 + </densityValue>
1222 + <density uom="kg/m3">503.27</density>
1223 + <densityFlowRate uom="Mg/a">392.39</densityFlowRate>
1224 + <densityStd uom="kg/m3">17.35</densityStd>
1225 + <concentration uom="ppm">38.15</concentration>
1226 + <molecularWeight>16.86</molecularWeight>
1227 + <weightPercent uom="%">81.26</weightPercent>
1228 + <molePercent uom="%">97.92</molePercent>
1229 + <moleAmt uom="kmol">58.33</moleAmt>
1230 + <sg uom="Euc">52.22</sg>
1231 + <hcDewpoint uom="K">430.19</hcDewpoint>
1232 + <waterDewpoint uom="K">612.34</waterDewpoint>
1233 + <wobbeIndex uom="J/m3">930.22</wobbeIndex>
1234 + <grossCalorificValueStd uom="J/m3">976.12</grossCalorificValueStd>
1235 + <rvpStabilizedCrude uom="Pa">157.5</rvpStabilizedCrude>
1236 + <bswStabilizedCrude uom="Euc">657.84</bswStabilizedCrude>
1237 + <densityStabilizedCrude uom="kg/m3">875.08</densityStabilizedCrude>
1238 + <componentContent uid="b15c985e-f359-11e1-aede-d067e534860e">
1239 + <kind>C8-</kind>
1240 + <referenceKind>C2+</referenceKind>
1241 + <gor uom="Euc">64.08</gor>
1242 + <gorMTD uom="m3/m3">86.34</gorMTD>
1243 + <waterConcMass uom="%">16.26</waterConcMass>
1244 + <waterConcVol uom="ppm">68.4</waterConcVol>
1245 + <atmosphere uom="Pa">88.02</atmosphere>
1246 + <volumeValue>
1247 + <volume status="range limit" uom="m3">728.09</volume>
1248 + <grossCalorificValue uom="J/m3">143.82</grossCalorificValue>
1249 + <temp uom="K">27.37</temp>
1250 + <pres uom="Pa">61.47</pres>
1251 + </volumeValue>
1252 + <volume status="bad calibration" uom="m3">12.13</volume>
1253 + <volumeStd status="bad calibration" uom="m3">20.75</volumeStd>
1254 + <flowRate status="bad calibration" uom="m3/s">40.23</flowRate>
1255 + <temp uom="K">57.29</temp>
1256 + <pres uom="Pa">20.3</pres>
1257 + <absoluteMinPres uom="Pa">20.37</absoluteMinPres>
1258 + <portDiff uid="b15c985f-f359-11e1-8121-d067e534860e">
1259 + <port uidRef="b15c9860-f359-11e1-b1fe-d067e534860e">Port 1</port>
1260 + <presDiff uom="Pa">34.64</presDiff>
1261 + <tempDiff uom="K">69.4</tempDiff>
1262 + <chokeSize uom="in/32">61.98</chokeSize>
1263 + <chokeRelative uom="%">84.39</chokeRelative>
1264 + </portDiff>
1265 + <portDiff uid="b15c9861-f359-11e1-8ce2-d067e534860e">
1266 + <port uidRef="b15c9862-f359-11e1-a329-d067e534860e">Port 2</port>
1267 + <presDiff uom="Pa">28.03</presDiff>
1268 + <tempDiff uom="K">35.98</tempDiff>
1269 + <chokeSize uom="in/32">48.71</chokeSize>
1270 + <chokeRelative uom="%">42.2</chokeRelative>
1271 + </portDiff>
1272 + <mass uom="kg">34.7</mass>
1273 + <work uom="MJ">311.65</work>
1274 + <efficiency uom="%">36.41</efficiency>
1275 + <rvp uom="Pa">283.92</rvp>
1276 + <tvp uom="bar">81.56</tvp>
1277 + <bsw uom="%">29.64</bsw>
1278 + <bswPrevious uom="m3/m3">47.54</bswPrevious>
1279 + <densityValue>
1280 + <density uom="kg/m3">403.34</density>
1281 + <temp uom="K">96.81</temp>
1282 + <pres uom="Pa">58.59</pres>
1283 + </densityValue>
1284 + <density uom="kg/m3">415.33</density>
1285 + <densityFlowRate uom="Mg/a">95.9</densityFlowRate>
1286 + <densityStd uom="kg/m3">555.16</densityStd>
1287 + <concentration uom="ppm">74.38</concentration>
1288 + <molecularWeight>81.82</molecularWeight>
1289 + <weightPercent uom="%">62.0</weightPercent>
1290 + <molePercent uom="%">25.84</molePercent>
1291 + <moleAmt uom="kmol">17.98</moleAmt>
1292 + <sg uom="Euc">60.75</sg>
1293 + <hcDewpoint uom="K">538.39</hcDewpoint>
1294 + <waterDewpoint uom="K">713.48</waterDewpoint>
1295 + <wobbeIndex uom="J/m3">414.86</wobbeIndex>
1296 + <grossCalorificValueStd uom="J/m3">696.02</grossCalorificValueStd>
1297 + <rvpStabilizedCrude uom="Pa">40.25</rvpStabilizedCrude>
1298 + <bswStabilizedCrude uom="Euc">144.32</bswStabilizedCrude>
1299 + <densityStabilizedCrude uom="kg/m3">449.68</densityStabilizedCrude>
1300 + </componentContent>
1301 + <period>
1302 + <kind>day</kind>
1303 + <dateStart>2012-03-01</dateStart>
1304 + <dateEnd>2012-03-01</dateEnd>
1305 + <gor uom="Euc">82.02</gor>
1306 + <gorMTD uom="m3/m3">48.04</gorMTD>
1307 + <waterConcMass uom="%">36.29</waterConcMass>
1308 + <waterConcVol uom="ppm">31.71</waterConcVol>
1309 + <atmosphere uom="Pa">70.55</atmosphere>
1310 + <volumeValue>
1311 +
1312 + <volume uom="m3">135.02</volume><temp uom="degC">15</temp>
1313 + <pres uom="atm">1</pres>
1314 + </volumeValue>
1315 + <volume status="bad calibration" uom="m3">18.4</volume>
1316 + <volumeStd status="bad calibration" uom="m3">18.47</volumeStd>
1317 + <flowRate status="bad calibration" uom="m3/s">74.13</flowRate>
1318 + <temp uom="K">64.83</temp>
1319 + <pres uom="Pa">67.8</pres>
1320 + <absoluteMinPres uom="Pa">19.88</absoluteMinPres>
1321 +
1322 + <mass uom="kg">248.48</mass>
1323 + <work uom="MJ">713.54</work>
1324 + <efficiency uom="%">35.75</efficiency>
1325 + <rvp uom="kPa">95.73</rvp>
1326 + <tvp uom="bar">222.27</tvp>
1327 + <bsw uom="%">39.13</bsw>
1328 + <bswPrevious uom="m3/m3">60.56</bswPrevious>
1329 + <densityValue>
1330 +
1331 + <density uom="kg/m3">764.0</density>
1332 + <temp uom="degC">15</temp>
1333 + <pres uom="atm">1</pres>
1334 + </densityValue>
1335 + <density uom="kg/m3">44.25</density>
1336 + <densityFlowRate uom="Mg/a">337.54</densityFlowRate>
1337 + <densityStd uom="kg/m3">129.72</densityStd>
1338 + <concentration uom="ppm">50.71</concentration>
1339 + <molecularWeight>90.62</molecularWeight>
1340 + <weightPercent uom="%">17.46</weightPercent>
1341 + <molePercent uom="%">21.28</molePercent>
1342 + <moleAmt uom="kmol">79.29</moleAmt>
1343 + <sg uom="Euc">36.83</sg>
1344 + <hcDewpoint uom="K">581.7</hcDewpoint>
1345 + <waterDewpoint uom="K">52.64</waterDewpoint>
1346 + <wobbeIndex uom="J/m3">35.57</wobbeIndex>
1347 + <grossCalorificValueStd uom="J/m3">875.14</grossCalorificValueStd>
1348 + <rvpStabilizedCrude uom="Pa">128.34</rvpStabilizedCrude>
1349 + <bswStabilizedCrude uom="Euc">300.49</bswStabilizedCrude>
1350 + <densityStabilizedCrude uom="kg/m3">809.42</densityStabilizedCrude>
1351 + </period>
1352 +
1353 + </product>
1354 + </flow>
1355 +
1356 +
1357 +
1358 + <flow>
1359 + <kind>injection</kind>
1360 + <qualifier>metered - fiscal</qualifier>
1361 + <version>2012-03-01T04:00:00.0Z</version>
1362 + <versionSource>version src 635</versionSource>
1363 + <gor uom="Euc">62.59</gor>
1364 + <gorMTD uom="m3/m3">99.11</gorMTD>
1365 + <waterConcMass uom="%">71.6</waterConcMass>
1366 + <waterConcVol uom="ppm">34.53</waterConcVol>
1367 + <atmosphere uom="Pa">59.4</atmosphere>
1368 + <volumeValue>
1369 + <volume status="comm failure" uom="m3">180.82</volume>
1370 + <grossCalorificValue uom="J/m3">511.05</grossCalorificValue>
1371 + <temp uom="K">86.78</temp>
1372 + <pres uom="Pa">73.71</pres>
1373 + </volumeValue>
1374 + <volume status="bad calibration" uom="m3">72.43</volume>
1375 + <volumeStd status="bad calibration" uom="m3">11.29</volumeStd>
1376 + <flowRate status="bad calibration" uom="m3/s">74.12</flowRate>
1377 + <temp uom="K">90.24</temp>
1378 + <pres uom="Pa">39.52</pres>
1379 + <absoluteMinPres uom="Pa">80.54</absoluteMinPres>
1380 + <portDiff uid="b15cbf70-f359-11e1-ad49-d067e534860e">
1381 + <port uidRef="b15cbf71-f359-11e1-8997-d067e534860e">Port 1</port>
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1383 + <tempDiff uom="K">57.28</tempDiff>
1384 + <chokeSize uom="in/32">45.47</chokeSize>
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1388 + <port uidRef="b15cbf73-f359-11e1-b8b2-d067e534860e">Port 2</port>
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1395 + <work uom="MJ">876.38</work>
1396 + <efficiency uom="%">74.86</efficiency>
1397 + <rvp uom="Pa">80.38</rvp>
1398 + <tvp uom="bar">539.07</tvp>
1399 + <bsw uom="%">39.49</bsw>
1400 + <bswPrevious uom="m3/m3">52.6</bswPrevious>
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1403 + <temp uom="K">41.94</temp>
1404 + <pres uom="Pa">95.81</pres>
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1407 + <densityFlowRate uom="Mg/a">195.69</densityFlowRate>
1408 + <densityStd uom="kg/m3">447.12</densityStd>
1409 + <concentration uom="ppm">15.57</concentration>
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1412 + <molePercent uom="%">48.26</molePercent>
1413 + <moleAmt uom="kmol">25.89</moleAmt>
1414 + <sg uom="Euc">42.71</sg>
1415 + <hcDewpoint uom="K">289.18</hcDewpoint>
1416 + <waterDewpoint uom="K">37.94</waterDewpoint>
1417 + <wobbeIndex uom="J/m3">477.46</wobbeIndex>
1418 + <grossCalorificValueStd uom="J/m3">661.2</grossCalorificValueStd>
1419 + <rvpStabilizedCrude uom="Pa">854.6</rvpStabilizedCrude>
1420 + <bswStabilizedCrude uom="Euc">756.71</bswStabilizedCrude>
1421 + <densityStabilizedCrude uom="kg/m3">774.01</densityStabilizedCrude>
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1426 + <gor uom="Euc">94.36</gor>
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1428 + <waterConcMass uom="%">41.65</waterConcMass>
1429 + <waterConcVol uom="ppm">95.09</waterConcVol>
1430 + <atmosphere uom="Pa">67.78</atmosphere>
1431 + <volumeValue>
1432 + <volume status="bad calibration" uom="m3">757.3</volume>
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1434 + <temp uom="K">72.66</temp>
1435 + <pres uom="Pa">39.02</pres>
1436 + </volumeValue>
1437 + <volume status="bad calibration" uom="m3">62.8</volume>
1438 + <volumeStd status="bad calibration" uom="m3">20.85</volumeStd>
1439 + <flowRate status="bad calibration" uom="m3/s">72.97</flowRate>
1440 + <temp uom="K">89.41</temp>
1441 + <pres uom="Pa">21.68</pres>
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1444 + <port uidRef="b15ce681-f359-11e1-8bc7-d067e534860e">Port 1</port>
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1451 + <port uidRef="b15ce683-f359-11e1-8acf-d067e534860e">Port 2</port>
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1457 + <mass uom="kg">508.55</mass>
1458 + <work uom="MJ">457.39</work>
1459 + <efficiency uom="%">92.64</efficiency>
1460 + <rvp uom="Pa">511.71</rvp>
1461 + <tvp uom="bar">832.56</tvp>
1462 + <bsw uom="%">28.79</bsw>
1463 + <bswPrevious uom="m3/m3">55.61</bswPrevious>
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1465 + <density uom="kg/m3">482.8</density>
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1471 + <densityStd uom="kg/m3">31.37</densityStd>
1472 + <concentration uom="ppm">45.21</concentration>
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1475 + <molePercent uom="%">18.61</molePercent>
1476 + <moleAmt uom="kmol">14.59</moleAmt>
1477 + <sg uom="Euc">20.78</sg>
1478 + <hcDewpoint uom="K">182.36</hcDewpoint>
1479 + <waterDewpoint uom="K">58.41</waterDewpoint>
1480 + <wobbeIndex uom="J/m3">189.42</wobbeIndex>
1481 + <grossCalorificValueStd uom="J/m3">542.81</grossCalorificValueStd>
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1483 + <bswStabilizedCrude uom="Euc">229.69</bswStabilizedCrude>
1484 + <densityStabilizedCrude uom="kg/m3">718.59</densityStabilizedCrude>
1485 + <componentContent uid="b15ce684-f359-11e1-a8e5-d067e534860e">
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1490 + <waterConcMass uom="%">67.31</waterConcMass>
1491 + <waterConcVol uom="ppm">13.53</waterConcVol>
1492 + <atmosphere uom="Pa">78.48</atmosphere>
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1494 + <volume status="comm failure" uom="m3">262.35</volume>
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1496 + <temp uom="K">52.64</temp>
1497 + <pres uom="Pa">58.56</pres>
1498 + </volumeValue>
1499 + <volume status="bad calibration" uom="m3">21.98</volume>
1500 + <volumeStd status="bad calibration" uom="m3">23.07</volumeStd>
1501 + <flowRate status="bad calibration" uom="m3/s">31.8</flowRate>
1502 + <temp uom="K">12.52</temp>
1503 + <pres uom="Pa">66.24</pres>
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1506 + <port uidRef="b15d0d8f-f359-11e1-a065-d067e534860e">Port 1</port>
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1509 + <chokeSize uom="in/32">20.44</chokeSize>
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1513 + <port uidRef="b15d0d91-f359-11e1-9dbc-d067e534860e">Port 2</port>
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1516 + <chokeSize uom="in/32">76.78</chokeSize>
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1520 + <work uom="MJ">218.22</work>
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1522 + <rvp uom="Pa">709.92</rvp>
1523 + <tvp uom="bar">728.89</tvp>
1524 + <bsw uom="%">46.3</bsw>
1525 + <bswPrevious uom="m3/m3">50.8</bswPrevious>
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1527 + <density uom="kg/m3">223.38</density>
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1534 + <concentration uom="ppm">55.73</concentration>
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1537 + <molePercent uom="%">64.1</molePercent>
1538 + <moleAmt uom="kmol">49.82</moleAmt>
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1559 + <volume uom="m3">1942.69</volume><temp uom="degC">15</temp>
1560 + <pres uom="atm">1</pres>
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1563 + <volumeStd status="bad calibration" uom="m3">66.4</volumeStd>
1564 + <flowRate status="bad calibration" uom="m3/s">52.11</flowRate>
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1566 + <pres uom="Pa">50.23</pres>
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1571 + <efficiency uom="%">80.38</efficiency>
1572 + <rvp uom="kPa">871.12</rvp>
1573 + <tvp uom="bar">138.67</tvp>
1574 + <bsw uom="%">60.01</bsw>
1575 + <bswPrevious uom="m3/m3">28.12</bswPrevious>
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1578 + <density uom="kg/m3">792.8</density>
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1584 + <densityStd uom="kg/m3">232.29</densityStd>
1585 + <concentration uom="ppm">44.72</concentration>
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1588 + <molePercent uom="%">95.88</molePercent>
1589 + <moleAmt uom="kmol">67.42</moleAmt>
1590 + <sg uom="Euc">98.09</sg>
1591 + <hcDewpoint uom="K">829.2</hcDewpoint>
1592 + <waterDewpoint uom="K">803.34</waterDewpoint>
1593 + <wobbeIndex uom="J/m3">223.36</wobbeIndex>
1594 + <grossCalorificValueStd uom="J/m3">318.81</grossCalorificValueStd>
1595 + <rvpStabilizedCrude uom="Pa">793.94</rvpStabilizedCrude>
1596 + <bswStabilizedCrude uom="Euc">171.79</bswStabilizedCrude>
1597 + <densityStabilizedCrude uom="kg/m3">750.3</densityStabilizedCrude>
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1600 + </product>
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1813 + <sampleType>separator oil</sampleType>
1814 + <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
1815 + <acquisitionDate>2012-02-12</acquisitionDate>
1816 + <customData>
1817 + <extensionNameValue>
1818 + <name>ValidFrom</name>
1819 + <value>2012-02-12T00:00:00.0Z</value>
1820 + <dataType>dateTime</dataType>
1821 + </extensionNameValue>
1822 + <extensionNameValue>
1823 + <name>ValidTo</name>
1824 + <value>2012-02-28T00:00:00.0Z</value>
1825 + <dataType>dateTime</dataType>
1826 + </extensionNameValue>
1827 + </customData>
1828 + </object><object xsi:type="obj_fluidSample">
1829 + <name>TYRIHANS-GAS-CHARACTERISTICS-1</name>
1830 + <sampleType>separator gas</sampleType>
1831 + <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
1832 + <acquisitionDate>2012-02-13</acquisitionDate>
1833 + <customData>
1834 + <extensionNameValue>
1835 + <name>ValidFrom</name>
1836 + <value>2012-02-13T00:00:00.0Z</value>
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1838 + </extensionNameValue>
1839 + <extensionNameValue>
1840 + <name>ValidTo</name>
1841 + <value>2012-02-26T00:00:00.0Z</value>
1842 + <dataType>dateTime</dataType>
1843 + </extensionNameValue>
1844 + </customData>
1845 + </object><object xsi:type="obj_fluidSample">
1846 + <name>TYRIHANS-LIQUID-CHARACTERISTICS-2</name>
1847 + <sampleType>separator oil</sampleType>
1848 + <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
1849 + <acquisitionDate>2012-02-11</acquisitionDate>
1850 + <customData>
1851 + <extensionNameValue>
1852 + <name>ValidFrom</name>
1853 + <value>2012-02-11T00:00:00.0Z</value>
1854 + <dataType>dateTime</dataType>
1855 + </extensionNameValue>
1856 + <extensionNameValue>
1857 + <name>ValidTo</name>
1858 + <value>2012-02-23T00:00:00.0Z</value>
1859 + <dataType>dateTime</dataType>
1860 + </extensionNameValue>
1861 + </customData>
1862 + </object><object xsi:type="obj_fluidSample">
1863 + <name>TYRIHANS-GAS-CHARACTERISTICS-2</name>
1864 + <sampleType>separator gas</sampleType>
1865 + <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
1866 + <acquisitionDate>2012-02-15</acquisitionDate>
1867 + <customData>
1868 + <extensionNameValue>
1869 + <name>ValidFrom</name>
1870 + <value>2012-02-15T00:00:00.0Z</value>
1871 + <dataType>dateTime</dataType>
1872 + </extensionNameValue>
1873 + <extensionNameValue>
1874 + <name>ValidTo</name>
1875 + <value>2012-02-23T00:00:00.0Z</value>
1876 + <dataType>dateTime</dataType>
1877 + </extensionNameValue>
1878 + </customData>
1879 + </object><object xsi:type="obj_fluidSample">
1880 + <name>TYRIHANS-LIQUID-CHARACTERISTICS-3</name>
1881 + <sampleType>separator oil</sampleType>
1882 + <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
1883 + <acquisitionDate>2012-02-12</acquisitionDate>
1884 + <customData>
1885 + <extensionNameValue>
1886 + <name>ValidFrom</name>
1887 + <value>2012-02-12T00:00:00.0Z</value>
1888 + <dataType>dateTime</dataType>
1889 + </extensionNameValue>
1890 + <extensionNameValue>
1891 + <name>ValidTo</name>
1892 + <value>2012-02-26T00:00:00.0Z</value>
1893 + <dataType>dateTime</dataType>
1894 + </extensionNameValue>
1895 + </customData>
1896 + </object><object xsi:type="obj_fluidSample">
1897 + <name>TYRIHANS-GAS-CHARACTERISTICS-3</name>
1898 + <sampleType>separator gas</sampleType>
1899 + <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
1900 + <acquisitionDate>2012-02-12</acquisitionDate>
1901 + <customData>
1902 + <extensionNameValue>
1903 + <name>ValidFrom</name>
1904 + <value>2012-02-12T00:00:00.0Z</value>
1905 + <dataType>dateTime</dataType>
1906 + </extensionNameValue>
1907 + <extensionNameValue>
1908 + <name>ValidTo</name>
1909 + <value>2012-02-26T00:00:00.0Z</value>
1910 + <dataType>dateTime</dataType>
1911 + </extensionNameValue>
1912 + </customData>
1913 + </object></objects>
...\ No newline at end of file ...\ No newline at end of file
1 -<?xml version="1.0" encoding="UTF-8" standalone="no"?><objects xmlns="http://www.epim.no/schemas/mprml/1" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" version="1.0(MPRML)"><documentInfo>
2 - <DocumentName namingSystem="EC">ÅSGARD March 2012</DocumentName>
3 - <DocumentAlias namingSystem="EC">ÅSGARD Copex Report</DocumentAlias>
4 - <DocumentDate>2012-03-06T00:00:00.0Z</DocumentDate>
5 - <documentClass namingSystem="EC">Statoil Petroleum AS</documentClass>
6 - <documentClass namingSystem="EC">DPR 2.0</documentClass>
7 - <documentClass namingSystem="ERH">dpr2</documentClass><FileCreationInformation>
8 -
9 - <FileCreationDate>2012-03-16T00:00:00.0Z</FileCreationDate>
10 -
11 - <SoftwareName>Energy Components</SoftwareName>
12 - <FileCreator>Statoil Petroleum AS</FileCreator>
13 - <Comment>NA</Comment>
14 - </FileCreationInformation>
15 - <Owner>Statoil Petroleum AS</Owner>
16 - </documentInfo><context xsi:type="obj_report">
17 - <kind>DPR 2.0</kind>
18 -
19 - <title>ÅSGARD</title>
20 - <date>2012-03-01</date>
21 - <dateEnd>2012-03-01</dateEnd>
22 - <month>2012-03</month>
23 - <year>2012</year>
24 - <reportVersion>2.0</reportVersion>
25 - <reportStatus>final</reportStatus>
26 - <installation kind="field" namingSystem="NPD" uidRef="43765">ÅSGARD</installation>
27 - <operator>
28 - <name>Statoil Petroleum AS</name>
29 - <role>Operating company</role>
30 - </operator>
31 - </context><object xsi:type="obj_productionOperation">
32 - <name>ÅSGARD operation report</name>
33 - <installation kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</installation>
34 - <periodKind>day</periodKind>
35 - <dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
36 - <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
37 - <operator>
38 - <name>Statoil Petroleum AS</name>
39 - <role>Operator</role>
40 - <personName>
41 - <prefix>Mr</prefix>
42 - <first>Test</first>
43 - <last>Dong</last>
44 - </personName>
45 - <address>
46 - <name>Statoil Petroleum AS</name>
47 - <street>Rosenberggate 99</street>
48 - <city>Stavanger</city>
49 - <country>Norway</country>
50 - <postalCode>4002</postalCode>
51 - </address>
52 - </operator>
53 - <title>ÅSGARD operation report</title>
54 - <geographicContext>
55 - <country>Norway</country>
56 - <field namingSystem="DONG">ÅSGARD</field>
57 -
58 - </geographicContext>
59 - <issueDate>2012-03-02</issueDate>
60 - <issuedBy>
61 - <name>Statoil Petroleum AS</name>
62 - <role>Operator</role>
63 - <personName>
64 - <prefix>Mr</prefix>
65 - <first>Test</first>
66 - <last>Dong</last>
67 - </personName>
68 - </issuedBy>
69 - <approvalDate>2012-03-02</approvalDate>
70 - <approver>
71 - <name>Statoil Petroleum AS</name>
72 - <role>Platformssjef</role>
73 - <personName>
74 - <prefix>Mr</prefix>
75 - <first>Test</first>
76 - <last>Dong</last>
77 - </personName>
78 - </approver>
79 - <installationReport uid="a57d492e-bad4-11e1-963a-c0f8dae91040">
80 - <installation kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</installation>
81 - <bedsAvailable>10</bedsAvailable>
82 - <crewCount type="catering crew">1</crewCount>
83 - <crewCount type="contractor crew">4</crewCount>
84 - <crewCount type="own crew">5</crewCount>
85 - <work uom="h">22</work>
86 - <workMonthToDate uom="d">23</workMonthToDate>
87 - <workYearToDate uom="d">62</workYearToDate>
88 - <operationalHSE>
89 - <IncidentCount>1</IncidentCount>
90 - <sinceLostTime uom="d">10</sinceLostTime>
91 - <sincePreventionExercise uom="d">13</sincePreventionExercise>
92 - <sinceDefinedSituation uom="d">2</sinceDefinedSituation>
93 - <alarmCount>0</alarmCount>
94 - <safetyIntroCount>0</safetyIntroCount>
95 - <safetyDescription>I suggested that these results</safetyDescription>
96 - <safety>
97 - <meantimeIncident uom="d">2</meantimeIncident>
98 - <safetyCount period="day" type="lost time incident">1</safetyCount>
99 - <safetyCount period="day" type="sick on board">1</safetyCount>
100 - <comment>
101 - <dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
102 - <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
103 - <remark>It may be, then, that the notion of level of grammaticalness is unspecified with respect to a parasi</remark>
104 - </comment>
105 - </safety>
106 - <weather>
107 - <dTim>2012-03-01T00:00:00.0Z</dTim>
108 - <agency>Weather agency</agency>
109 - <barometricPressure uom="Pa">57.56</barometricPressure>
110 - <beaufortScaleNumber>5</beaufortScaleNumber>
111 - <tempSurfaceMn uom="degC">15</tempSurfaceMn>
112 - <tempSurfaceMx uom="degC">12</tempSurfaceMx>
113 - <tempWindChill uom="degC">13</tempWindChill>
114 - <tempsea uom="degC">13</tempsea>
115 - <visibility uom="m">391</visibility>
116 - <aziWave uom="rad">9</aziWave>
117 - <htWave uom="m">7</htWave>
118 - <significantWave uom="m">6</significantWave>
119 - <maxWave uom="m">2</maxWave>
120 - <periodWave uom="s">3</periodWave>
121 - <aziWind uom="rad">2</aziWind>
122 - <velWind uom="m/s">9</velWind>
123 - <typePrecip>rain</typePrecip>
124 - <amtPrecip uom="m">3</amtPrecip>
125 - <coverCloud>180</coverCloud>
126 - <ceilingCloud uom="m">230</ceilingCloud>
127 - <currentSea uom="m/s">1</currentSea>
128 - <aziCurrentSea uom="rad">3</aziCurrentSea>
129 - <comments>I suggested that these results would follow from the assumption that the descriptive power of the ba</comments>
130 - </weather>
131 -
132 - </operationalHSE>
133 -
134 - <productionActivity>
135 - <lostProduction>
136 - <volumeAndReason reasonLost="topside equipment failure-maint" uom="m3">1053.4</volumeAndReason>
137 - <volumeAndReason reasonLost="preventive maint topside" uom="m3">1140.2</volumeAndReason>
138 - <thirdPartyProcessing>
139 - <installation kind="platform">Ekofisk</installation>
140 - <oilStdTempPres uom="m3">1747.83</oilStdTempPres>
141 - <gasStdTempPres uom="m3">1196.25</gasStdTempPres>
142 - </thirdPartyProcessing>
143 -
144 - </lostProduction>
145 - <waterCleaningQuality>
146 - <samplePoint>Sample 1</samplePoint>
147 - <oilInWaterProduced uom="Euc">61.94</oilInWaterProduced>
148 - <amountOfOil uom="kg">96.85</amountOfOil>
149 - <ammonium uom="kg/m3">4.84</ammonium>
150 - <totalOrganicCarbon uom="Euc">14.33</totalOrganicCarbon>
151 - <phenol uom="kg/m3">27.87</phenol>
152 - <glycol uom="kg/m3">117.24</glycol>
153 - <phValue>8.03</phValue>
154 - <waterTemperature uom="degC">12.37</waterTemperature>
155 - <residualChloride uom="Euc">125.49</residualChloride>
156 - <oxygen uom="Euc">52.8</oxygen>
157 - <turbidity>32.4</turbidity>
158 - <coulterCounter uom="Euc">185.06</coulterCounter>
159 -
160 - <comment>
161 - <dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
162 - <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
163 - <remark>So far, the descriptive power of the base component is not to be considered in determining problems </remark>
164 - </comment>
165 - </waterCleaningQuality>
166 - <shutdown>
167 - <installation kind="well">String</installation>
168 - <description>Preventive maintenance</description>
169 - <dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
170 - <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
171 - <volumetricDownTime uom="h">0</volumetricDownTime>
172 - <lossOilStdTempPres uom="m3">780.08</lossOilStdTempPres>
173 - <lossGasStdTempPres uom="m3">7223.75</lossGasStdTempPres>
174 - <activity>
175 - <dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
176 - <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
177 - <remark>For any transformation which is sufficiently diversified in application to be of any interest, the t</remark>
178 - </activity>
179 -
180 - </shutdown>
181 -
182 - <alarm>
183 - <dTim>2012-03-01T00:00:00.0Z</dTim>
184 - <area>Area A</area>
185 - <type>Gas Alarm</type>
186 - <reason>Faulty alarm</reason>
187 - <comment>Nevertheless, a subset of English sentences interesting on quite independent grounds suffices to acc</comment>
188 - </alarm>
189 -
190 - <marineOperation>
191 - <dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
192 - <dTimEnd>2012-03-01T02:00:00.0Z</dTimEnd>
193 - <generalComment>Clearly, the appearance of parasitic gaps in domains relatively inaccessible to ordinary extraction </generalComment>
194 - <supplyShip>Supply 1</supplyShip>
195 - <standbyVessel>Standby 1</standbyVessel>
196 - <supplyShipComment>
197 -
198 - <dTimStart>2012-03-01T01:00:00.0Z</dTimStart>
199 - <dTimEnd>2012-03-01T06:00:00.0Z</dTimEnd>
200 - <remark>So far, a case of semigrammaticalness of a different sort may remedy and, at the same time, eliminat</remark>
201 - </supplyShipComment>
202 - <supplyShipComment>
203 -
204 - <dTimStart>2012-03-01T06:00:00.0Z</dTimStart>
205 - <dTimEnd>2012-03-01T08:00:00.0Z</dTimEnd>
206 - <remark>Thus a subset of English sentences interesting on quite independent grounds is to be regarded as a d</remark>
207 - </supplyShipComment>
208 -
209 - <standbyVesselComment>
210 - <dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
211 - <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
212 - <remark>It appears that the systematic use of complex symbols is to be regarded as problems of phonemic and </remark>
213 - </standbyVesselComment>
214 -
215 - <basketMovement>
216 - <dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
217 - <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
218 - <remark>However, this assumption is not correct, since the descriptive power of the base component is rather</remark>
219 - </basketMovement>
220 - <basketMovement>
221 - <dTimStart>2012-03-01T02:00:00.0Z</dTimStart>
222 - <dTimEnd>2012-03-01T04:00:00.0Z</dTimEnd>
223 - <remark>A consequence of the approach just outlined is that the systematic use of complex symbols delimits t</remark>
224 - </basketMovement>
225 - <activity>
226 - <dTimStart>2012-03-01T06:00:00.0Z</dTimStart>
227 - <dTimEnd>2012-03-01T08:00:00.0Z</dTimEnd>
228 - <remark>In the discussion of resumptive pronouns following (81), the theory of syntactic features developed </remark>
229 - </activity>
230 - <activity>
231 - <dTimStart>2012-03-01T09:00:00.0Z</dTimStart>
232 - <dTimEnd>2012-03-01T11:00:00.0Z</dTimEnd>
233 - <remark>Thus this selectionally introduced contextual feature is to be regarded as an important distinction </remark>
234 - </activity>
235 - </marineOperation>
236 -
237 - <cargoShipOperation>
238 - <vesselName>Cargo 1</vesselName>
239 - <dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
240 - <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
241 - <captain>Captain 1</captain>
242 - <cargo>Oil</cargo>
243 - <oilGrossStdTempPres uom="m3">5381.62</oilGrossStdTempPres>
244 - <oilGrossTotalStdTempPres uom="m3">6615.82</oilGrossTotalStdTempPres>
245 - <oilNetStdTempPres uom="m3">5342.1</oilNetStdTempPres>
246 - <oilNetMonthToDateStdTempPres uom="m3">5241.47</oilNetMonthToDateStdTempPres>
247 - <densityStdTempPres uom="kg/m3">719.05</densityStdTempPres>
248 -
249 - <rvp uom="Pa">132.25</rvp>
250 - <bsw uom="Euc">197.35</bsw>
251 - <salt uom="kg/m3">116.05</salt>
252 - <comment>
253 - <dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
254 - <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
255 - <remark>This suggests that a case of semigrammaticalness of a different sort does not affect the structure o</remark>
256 - </comment>
257 - <comment>
258 - <dTimStart>2012-03-01T01:00:00.0Z</dTimStart>
259 - <dTimEnd>2012-03-01T02:00:00.0Z</dTimEnd>
260 - <remark>In the discussion of resumptive pronouns following (81), a case of semigrammaticalness of a differen</remark>
261 - </comment>
262 - </cargoShipOperation>
263 - <operationalComment>
264 - <type>production</type>
265 - <dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
266 - <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
267 - <comment>Nevertheless, most of the methodological work in modern linguistics is not quite equivalent to a des</comment>
268 - </operationalComment>
269 - <operationalComment>
270 - <type>production</type>
271 - <dTimStart>2012-03-01T06:00:00.0Z</dTimStart>
272 - <dTimEnd>2012-03-01T12:00:00.0Z</dTimEnd>
273 - <comment>For any transformation which is sufficiently diversified in application to be of any interest, the t</comment>
274 - </operationalComment>
275 - </productionActivity>
276 - </installationReport>
277 -</object><object xsi:type="obj_productVolume">
278 - <name>TYRIHANS</name>
279 - <installation kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</installation>
280 - <facility>
281 - <name kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</name>
282 - <facilityParent1 kind="block valve" namingSystem="String" uidRef="x">String</facilityParent1>
283 - <facilityParent2 kind="block valve" namingSystem="String" uidRef="x">String</facilityParent2>
284 - <facilityAlias namingSystem="String">String</facilityAlias>
285 - <facilityAlias namingSystem="String">String</facilityAlias>
286 - <contextFacility kind="block valve" namingSystem="String" uidRef="x">String</contextFacility>
287 - <contextFacility kind="block valve" namingSystem="String" uidRef="x">String</contextFacility>
288 -
289 -
290 - <downtimeReason uid="a5939051-bad4-11e1-acc2-c0f8dae91040">
291 - <who>MR Who</who>
292 - <role>Platform manager</role>
293 - <dTimStart>2012-03-01T02:00:00.0Z</dTimStart>
294 - <dTimEnd>2012-03-01T04:00:00.0Z</dTimEnd>
295 - <remark>A consequence of the approach just outlined is that the speaker-hearer's linguistic intuition delimi</remark>
296 - </downtimeReason>
297 - <downtimeReason uid="a5939052-bad4-11e1-9b76-c0f8dae91040">
298 - <who>Mr Who2</who>
299 - <role>Platform manager 2</role>
300 - <dTimStart>2012-03-01T06:00:00.0Z</dTimStart>
301 - <dTimEnd>2012-03-01T14:00:00.0Z</dTimEnd>
302 - <remark>To characterize a linguistic level L, a descriptively adequate grammar does not readily tolerate the</remark>
303 - </downtimeReason>
304 - <flow>
305 - <kind>production</kind>
306 - <qualifier>saleable</qualifier>
307 - <version>2012-03-01T22:00:00.0Z</version>
308 - <versionSource>version src 914</versionSource>
309 - <gor uom="Euc">53.07</gor>
310 - <gorMTD uom="m3/m3">51.46</gorMTD>
311 - <waterConcMass uom="%">91.44</waterConcMass>
312 - <waterConcVol uom="ppm">49.19</waterConcVol>
313 - <atmosphere uom="Pa">75.38</atmosphere>
314 - <volumeValue>
315 - <volume status="questionable" uom="m3">785.16</volume>
316 - <grossCalorificValue uom="J/m3">641.22</grossCalorificValue>
317 - <temp uom="K">35.18</temp>
318 - <pres uom="Pa">94.73</pres>
319 - </volumeValue>
320 - <volume status="bad calibration" uom="m3">18.01</volume>
321 - <volumeStd status="bad calibration" uom="m3">16.78</volumeStd>
322 - <flowRate status="bad calibration" uom="m3/s">25.65</flowRate>
323 - <temp uom="K">61.2</temp>
324 - <pres uom="Pa">41.65</pres>
325 - <absoluteMinPres uom="Pa">65.2</absoluteMinPres>
326 - <portDiff uid="a593b75e-bad4-11e1-8a2f-c0f8dae91040">
327 - <port uidRef="a593b75f-bad4-11e1-9811-c0f8dae91040">Port 1</port>
328 - <presDiff uom="Pa">77.05</presDiff>
329 - <tempDiff uom="K">20.15</tempDiff>
330 - <chokeSize uom="in/32">71.74</chokeSize>
331 - <chokeRelative uom="%">23.04</chokeRelative>
332 - </portDiff>
333 - <portDiff uid="a593b760-bad4-11e1-852b-c0f8dae91040">
334 - <port uidRef="a593b761-bad4-11e1-913c-c0f8dae91040">Port 2</port>
335 - <presDiff uom="Pa">29.37</presDiff>
336 - <tempDiff uom="K">33.5</tempDiff>
337 - <chokeSize uom="in/32">55.86</chokeSize>
338 - <chokeRelative uom="%">62.26</chokeRelative>
339 - </portDiff>
340 - <mass uom="kg">596.23</mass>
341 - <work uom="MJ">116.13</work>
342 - <efficiency uom="%">58.88</efficiency>
343 - <rvp uom="Pa">761.31</rvp>
344 - <tvp uom="bar">609.35</tvp>
345 - <bsw uom="%">38.95</bsw>
346 - <bswPrevious uom="m3/m3">37.52</bswPrevious>
347 - <densityValue>
348 - <density uom="kg/m3">154.93</density>
349 - <temp uom="K">43.99</temp>
350 - <pres uom="Pa">84.69</pres>
351 - </densityValue>
352 - <density uom="kg/m3">134.58</density>
353 - <densityFlowRate uom="Mg/a">291.27</densityFlowRate>
354 - <densityStd uom="kg/m3">422.56</densityStd>
355 - <concentration uom="ppm">27.37</concentration>
356 - <molecularWeight>42.48</molecularWeight>
357 - <weightPercent uom="%">90.64</weightPercent>
358 - <molePercent uom="%">98.52</molePercent>
359 - <moleAmt uom="kmol">22.78</moleAmt>
360 - <sg uom="Euc">59.65</sg>
361 - <hcDewpoint uom="K">918.59</hcDewpoint>
362 - <waterDewpoint uom="K">505.72</waterDewpoint>
363 - <wobbeIndex uom="J/m3">783.46</wobbeIndex>
364 - <grossCalorificValueStd uom="J/m3">35.94</grossCalorificValueStd>
365 - <rvpStabilizedCrude uom="Pa">973.12</rvpStabilizedCrude>
366 - <bswStabilizedCrude uom="Euc">854.65</bswStabilizedCrude>
367 - <densityStabilizedCrude uom="kg/m3">610.47</densityStabilizedCrude>
368 - <product>
369 - <kind>oil - net</kind>
370 - <name namingSystem="TEST17">Test product name 507</name>
371 - <splitFactor>0.67</splitFactor>
372 - <gor uom="Euc">45.98</gor>
373 - <gorMTD uom="m3/m3">54.61</gorMTD>
374 - <waterConcMass uom="%">24.57</waterConcMass>
375 - <waterConcVol uom="ppm">49.63</waterConcVol>
376 - <atmosphere uom="Pa">96.97</atmosphere>
377 - <volumeValue>
378 - <volume status="questionable" uom="m3">882.04</volume>
379 - <grossCalorificValue uom="J/m3">412.16</grossCalorificValue>
380 - <temp uom="K">60.27</temp>
381 - <pres uom="Pa">76.05</pres>
382 - </volumeValue>
383 - <volume status="bad calibration" uom="m3">92.12</volume>
384 - <volumeStd status="bad calibration" uom="m3">18.65</volumeStd>
385 - <flowRate status="bad calibration" uom="m3/s">60.29</flowRate>
386 - <temp uom="K">98.91</temp>
387 - <pres uom="Pa">82.78</pres>
388 - <absoluteMinPres uom="Pa">34.27</absoluteMinPres>
389 - <portDiff uid="a593b762-bad4-11e1-a353-c0f8dae91040">
390 - <port uidRef="a593b763-bad4-11e1-9822-c0f8dae91040">Port 1</port>
391 - <presDiff uom="Pa">67.4</presDiff>
392 - <tempDiff uom="K">54.21</tempDiff>
393 - <chokeSize uom="in/32">79.02</chokeSize>
394 - <chokeRelative uom="%">44.15</chokeRelative>
395 - </portDiff>
396 - <portDiff uid="a593b764-bad4-11e1-ace2-c0f8dae91040">
397 - <port uidRef="a593b765-bad4-11e1-9607-c0f8dae91040">Port 2</port>
398 - <presDiff uom="Pa">41.6</presDiff>
399 - <tempDiff uom="K">90.5</tempDiff>
400 - <chokeSize uom="in/32">65.45</chokeSize>
401 - <chokeRelative uom="%">57.19</chokeRelative>
402 - </portDiff>
403 - <mass uom="kg">79.45</mass>
404 - <work uom="MJ">181.12</work>
405 - <efficiency uom="%">33.95</efficiency>
406 - <rvp uom="Pa">705.54</rvp>
407 - <tvp uom="bar">153.81</tvp>
408 - <bsw uom="%">32.3</bsw>
409 - <bswPrevious uom="m3/m3">95.5</bswPrevious>
410 - <densityValue>
411 - <density uom="kg/m3">175.98</density>
412 - <temp uom="K">56.57</temp>
413 - <pres uom="Pa">45.46</pres>
414 - </densityValue>
415 - <density uom="kg/m3">36.16</density>
416 - <densityFlowRate uom="Mg/a">274.98</densityFlowRate>
417 - <densityStd uom="kg/m3">204.26</densityStd>
418 - <concentration uom="ppm">16.59</concentration>
419 - <molecularWeight>33.95</molecularWeight>
420 - <weightPercent uom="%">50.19</weightPercent>
421 - <molePercent uom="%">93.72</molePercent>
422 - <moleAmt uom="kmol">23.97</moleAmt>
423 - <sg uom="Euc">16.12</sg>
424 - <hcDewpoint uom="K">237.23</hcDewpoint>
425 - <waterDewpoint uom="K">524.96</waterDewpoint>
426 - <wobbeIndex uom="J/m3">840.05</wobbeIndex>
427 - <grossCalorificValueStd uom="J/m3">300.4</grossCalorificValueStd>
428 - <rvpStabilizedCrude uom="Pa">976.7</rvpStabilizedCrude>
429 - <bswStabilizedCrude uom="Euc">265.02</bswStabilizedCrude>
430 - <densityStabilizedCrude uom="kg/m3">296.01</densityStabilizedCrude>
431 - <componentContent uid="a593de6e-bad4-11e1-9499-c0f8dae91040">
432 - <kind>nitrogen oxide gas</kind>
433 - <referenceKind>carbon dioxide gas</referenceKind>
434 - <gor uom="Euc">69.5</gor>
435 - <gorMTD uom="m3/m3">93.25</gorMTD>
436 - <waterConcMass uom="%">60.35</waterConcMass>
437 - <waterConcVol uom="ppm">31.85</waterConcVol>
438 - <atmosphere uom="Pa">91.8</atmosphere>
439 - <volumeValue>
440 - <volume status="bad calibration" uom="m3">712.13</volume>
441 - <grossCalorificValue uom="J/m3">470.75</grossCalorificValue>
442 - <temp uom="K">43.71</temp>
443 - <pres uom="Pa">63.99</pres>
444 - </volumeValue>
445 - <volume status="bad calibration" uom="m3">48.95</volume>
446 - <volumeStd status="bad calibration" uom="m3">61.28</volumeStd>
447 - <flowRate status="bad calibration" uom="m3/s">71.87</flowRate>
448 - <temp uom="K">45.51</temp>
449 - <pres uom="Pa">27.53</pres>
450 - <absoluteMinPres uom="Pa">98.37</absoluteMinPres>
451 - <portDiff uid="a593de6f-bad4-11e1-97d5-c0f8dae91040">
452 - <port uidRef="a5940580-bad4-11e1-b600-c0f8dae91040">Port 1</port>
453 - <presDiff uom="Pa">50.5</presDiff>
454 - <tempDiff uom="K">96.22</tempDiff>
455 - <chokeSize uom="in/32">11.2</chokeSize>
456 - <chokeRelative uom="%">82.82</chokeRelative>
457 - </portDiff>
458 - <portDiff uid="a5940581-bad4-11e1-a2b6-c0f8dae91040">
459 - <port uidRef="a5940582-bad4-11e1-9596-c0f8dae91040">Port 2</port>
460 - <presDiff uom="Pa">21.23</presDiff>
461 - <tempDiff uom="K">19.55</tempDiff>
462 - <chokeSize uom="in/32">91.67</chokeSize>
463 - <chokeRelative uom="%">19.6</chokeRelative>
464 - </portDiff>
465 - <mass uom="kg">456.12</mass>
466 - <work uom="MJ">495.34</work>
467 - <efficiency uom="%">75.15</efficiency>
468 - <rvp uom="Pa">202.1</rvp>
469 - <tvp uom="bar">805.39</tvp>
470 - <bsw uom="%">49.24</bsw>
471 - <bswPrevious uom="m3/m3">98.52</bswPrevious>
472 - <densityValue>
473 - <density uom="kg/m3">538.56</density>
474 - <temp uom="K">61.47</temp>
475 - <pres uom="Pa">48.61</pres>
476 - </densityValue>
477 - <density uom="kg/m3">256.01</density>
478 - <densityFlowRate uom="Mg/a">20.2</densityFlowRate>
479 - <densityStd uom="kg/m3">139.29</densityStd>
480 - <concentration uom="ppm">17.42</concentration>
481 - <molecularWeight>21.62</molecularWeight>
482 - <weightPercent uom="%">80.09</weightPercent>
483 - <molePercent uom="%">35.27</molePercent>
484 - <moleAmt uom="kmol">33.81</moleAmt>
485 - <sg uom="Euc">70.01</sg>
486 - <hcDewpoint uom="K">519.78</hcDewpoint>
487 - <waterDewpoint uom="K">453.96</waterDewpoint>
488 - <wobbeIndex uom="J/m3">431.08</wobbeIndex>
489 - <grossCalorificValueStd uom="J/m3">579.92</grossCalorificValueStd>
490 - <rvpStabilizedCrude uom="Pa">167.9</rvpStabilizedCrude>
491 - <bswStabilizedCrude uom="Euc">97.6</bswStabilizedCrude>
492 - <densityStabilizedCrude uom="kg/m3">229.67</densityStabilizedCrude>
493 - </componentContent>
494 - <period>
495 - <kind>day</kind>
496 - <dateStart>2012-03-01</dateStart>
497 - <dateEnd>2012-03-01</dateEnd>
498 - <gor uom="Euc">80.87</gor>
499 - <gorMTD uom="m3/m3">71.58</gorMTD>
500 - <waterConcMass uom="%">10.64</waterConcMass>
501 - <waterConcVol uom="ppm">83.83</waterConcVol>
502 - <atmosphere uom="Pa">22.32</atmosphere>
503 - <volumeValue>
504 -
505 - <volume uom="m3">2765.7</volume><temp uom="degC">15</temp>
506 - <pres uom="atm">1</pres>
507 - </volumeValue>
508 - <volume status="bad calibration" uom="m3">36.48</volume>
509 - <volumeStd status="bad calibration" uom="m3">38.47</volumeStd>
510 - <flowRate status="bad calibration" uom="m3/s">55.99</flowRate>
511 - <temp uom="K">73.65</temp>
512 - <pres uom="Pa">13.61</pres>
513 - <absoluteMinPres uom="Pa">79.98</absoluteMinPres>
514 -
515 - <mass uom="kg">89.49</mass>
516 - <work uom="kW.h">435.72</work>
517 - <efficiency uom="%">98.18</efficiency>
518 - <rvp uom="bar">461.58</rvp>
519 - <tvp uom="bar">447.55</tvp>
520 - <bsw uom="%">68.5</bsw>
521 - <bswPrevious uom="m3/m3">43.97</bswPrevious>
522 - <densityValue>
523 -
524 - <density uom="kg/m3">780.91</density>
525 - <temp uom="degC">15</temp>
526 - <pres uom="atm">1</pres>
527 - </densityValue>
528 - <density uom="kg/m3">678.0</density>
529 - <densityFlowRate uom="Mg/a">166.24</densityFlowRate>
530 - <densityStd uom="kg/m3">527.52</densityStd>
531 - <concentration uom="ppm">50.64</concentration>
532 - <molecularWeight>87.94</molecularWeight>
533 - <weightPercent uom="%">34.91</weightPercent>
534 - <molePercent uom="%">31.48</molePercent>
535 - <moleAmt uom="kmol">47.46</moleAmt>
536 - <sg uom="Euc">94.18</sg>
537 - <hcDewpoint uom="K">488.91</hcDewpoint>
538 - <waterDewpoint uom="K">840.9</waterDewpoint>
539 - <wobbeIndex uom="J/m3">824.93</wobbeIndex>
540 - <grossCalorificValueStd uom="J/m3">993.66</grossCalorificValueStd>
541 - <rvpStabilizedCrude uom="Pa">398.65</rvpStabilizedCrude>
542 - <bswStabilizedCrude uom="Euc">673.57</bswStabilizedCrude>
543 - <densityStabilizedCrude uom="kg/m3">173.57</densityStabilizedCrude>
544 - </period>
545 -
546 - </product>
547 - </flow>
548 -
549 -
550 -
551 - <flow>
552 - <kind>consume - fuel</kind>
553 - <qualifier>allocated</qualifier>
554 - <version>2012-03-01T17:00:00.0Z</version>
555 - <versionSource>version src 454</versionSource>
556 - <gor uom="Euc">83.64</gor>
557 - <gorMTD uom="m3/m3">45.54</gorMTD>
558 - <waterConcMass uom="%">34.27</waterConcMass>
559 - <waterConcVol uom="ppm">30.89</waterConcVol>
560 - <atmosphere uom="Pa">15.07</atmosphere>
561 - <volumeValue>
562 - <volume status="sensor failure" uom="m3">850.38</volume>
563 - <grossCalorificValue uom="J/m3">882.59</grossCalorificValue>
564 - <temp uom="K">10.19</temp>
565 - <pres uom="Pa">85.11</pres>
566 - </volumeValue>
567 - <volume status="bad calibration" uom="m3">10.84</volume>
568 - <volumeStd status="bad calibration" uom="m3">89.23</volumeStd>
569 - <flowRate status="bad calibration" uom="m3/s">62.14</flowRate>
570 - <temp uom="K">12.66</temp>
571 - <pres uom="Pa">25.63</pres>
572 - <absoluteMinPres uom="Pa">31.24</absoluteMinPres>
573 - <portDiff uid="a5942c8f-bad4-11e1-b412-c0f8dae91040">
574 - <port uidRef="a5942c90-bad4-11e1-836f-c0f8dae91040">Port 1</port>
575 - <presDiff uom="Pa">75.65</presDiff>
576 - <tempDiff uom="K">31.06</tempDiff>
577 - <chokeSize uom="in/32">35.58</chokeSize>
578 - <chokeRelative uom="%">40.81</chokeRelative>
579 - </portDiff>
580 - <portDiff uid="a5942c91-bad4-11e1-9523-c0f8dae91040">
581 - <port uidRef="a5942c92-bad4-11e1-a7de-c0f8dae91040">Port 2</port>
582 - <presDiff uom="Pa">98.78</presDiff>
583 - <tempDiff uom="K">43.86</tempDiff>
584 - <chokeSize uom="in/32">38.01</chokeSize>
585 - <chokeRelative uom="%">35.99</chokeRelative>
586 - </portDiff>
587 - <mass uom="kg">288.8</mass>
588 - <work uom="MJ">21.58</work>
589 - <efficiency uom="%">87.73</efficiency>
590 - <rvp uom="Pa">654.07</rvp>
591 - <tvp uom="bar">679.85</tvp>
592 - <bsw uom="%">53.44</bsw>
593 - <bswPrevious uom="m3/m3">84.51</bswPrevious>
594 - <densityValue>
595 - <density uom="kg/m3">244.39</density>
596 - <temp uom="K">93.72</temp>
597 - <pres uom="Pa">50.81</pres>
598 - </densityValue>
599 - <density uom="kg/m3">137.61</density>
600 - <densityFlowRate uom="Mg/a">464.38</densityFlowRate>
601 - <densityStd uom="kg/m3">42.16</densityStd>
602 - <concentration uom="ppm">51.32</concentration>
603 - <molecularWeight>54.77</molecularWeight>
604 - <weightPercent uom="%">72.21</weightPercent>
605 - <molePercent uom="%">13.21</molePercent>
606 - <moleAmt uom="kmol">25.08</moleAmt>
607 - <sg uom="Euc">64.37</sg>
608 - <hcDewpoint uom="K">658.1</hcDewpoint>
609 - <waterDewpoint uom="K">180.48</waterDewpoint>
610 - <wobbeIndex uom="J/m3">902.14</wobbeIndex>
611 - <grossCalorificValueStd uom="J/m3">976.38</grossCalorificValueStd>
612 - <rvpStabilizedCrude uom="Pa">733.45</rvpStabilizedCrude>
613 - <bswStabilizedCrude uom="Euc">542.71</bswStabilizedCrude>
614 - <densityStabilizedCrude uom="kg/m3">616.46</densityStabilizedCrude>
615 - <product>
616 - <kind>diesel</kind>
617 - <name namingSystem="TEST2">Test product name 445</name>
618 - <splitFactor>0.56</splitFactor>
619 - <gor uom="Euc">87.93</gor>
620 - <gorMTD uom="m3/m3">96.91</gorMTD>
621 - <waterConcMass uom="%">34.59</waterConcMass>
622 - <waterConcVol uom="ppm">58.99</waterConcVol>
623 - <atmosphere uom="Pa">34.97</atmosphere>
624 - <volumeValue>
625 - <volume status="range limit" uom="m3">874.32</volume>
626 - <grossCalorificValue uom="J/m3">28.2</grossCalorificValue>
627 - <temp uom="K">78.68</temp>
628 - <pres uom="Pa">95.72</pres>
629 - </volumeValue>
630 - <volume status="bad calibration" uom="m3">27.39</volume>
631 - <volumeStd status="bad calibration" uom="m3">98.79</volumeStd>
632 - <flowRate status="bad calibration" uom="m3/s">18.51</flowRate>
633 - <temp uom="K">30.35</temp>
634 - <pres uom="Pa">32.06</pres>
635 - <absoluteMinPres uom="Pa">39.12</absoluteMinPres>
636 - <portDiff uid="a5942c93-bad4-11e1-99d0-c0f8dae91040">
637 - <port uidRef="a5942c94-bad4-11e1-9bc6-c0f8dae91040">Port 1</port>
638 - <presDiff uom="Pa">42.88</presDiff>
639 - <tempDiff uom="K">95.96</tempDiff>
640 - <chokeSize uom="in/32">95.96</chokeSize>
641 - <chokeRelative uom="%">92.33</chokeRelative>
642 - </portDiff>
643 - <portDiff uid="a5942c95-bad4-11e1-952d-c0f8dae91040">
644 - <port uidRef="a5942c96-bad4-11e1-8807-c0f8dae91040">Port 2</port>
645 - <presDiff uom="Pa">37.99</presDiff>
646 - <tempDiff uom="K">32.1</tempDiff>
647 - <chokeSize uom="in/32">84.84</chokeSize>
648 - <chokeRelative uom="%">28.26</chokeRelative>
649 - </portDiff>
650 - <mass uom="kg">84.07</mass>
651 - <work uom="MJ">59.04</work>
652 - <efficiency uom="%">59.05</efficiency>
653 - <rvp uom="Pa">31.33</rvp>
654 - <tvp uom="bar">923.69</tvp>
655 - <bsw uom="%">77.68</bsw>
656 - <bswPrevious uom="m3/m3">11.7</bswPrevious>
657 - <densityValue>
658 - <density uom="kg/m3">138.04</density>
659 - <temp uom="K">67.82</temp>
660 - <pres uom="Pa">71.84</pres>
661 - </densityValue>
662 - <density uom="kg/m3">571.01</density>
663 - <densityFlowRate uom="Mg/a">141.97</densityFlowRate>
664 - <densityStd uom="kg/m3">117.99</densityStd>
665 - <concentration uom="ppm">86.56</concentration>
666 - <molecularWeight>50.68</molecularWeight>
667 - <weightPercent uom="%">43.99</weightPercent>
668 - <molePercent uom="%">41.45</molePercent>
669 - <moleAmt uom="kmol">98.87</moleAmt>
670 - <sg uom="Euc">23.8</sg>
671 - <hcDewpoint uom="K">854.28</hcDewpoint>
672 - <waterDewpoint uom="K">12.84</waterDewpoint>
673 - <wobbeIndex uom="J/m3">594.48</wobbeIndex>
674 - <grossCalorificValueStd uom="J/m3">349.99</grossCalorificValueStd>
675 - <rvpStabilizedCrude uom="Pa">484.17</rvpStabilizedCrude>
676 - <bswStabilizedCrude uom="Euc">136.17</bswStabilizedCrude>
677 - <densityStabilizedCrude uom="kg/m3">96.22</densityStabilizedCrude>
678 - <componentContent uid="a594539e-bad4-11e1-94f3-c0f8dae91040">
679 - <kind>normal butane</kind>
680 - <referenceKind>gas</referenceKind>
681 - <gor uom="Euc">49.31</gor>
682 - <gorMTD uom="m3/m3">98.68</gorMTD>
683 - <waterConcMass uom="%">37.24</waterConcMass>
684 - <waterConcVol uom="ppm">84.94</waterConcVol>
685 - <atmosphere uom="Pa">84.18</atmosphere>
686 - <volumeValue>
687 - <volume status="sensor failure" uom="m3">73.31</volume>
688 - <grossCalorificValue uom="J/m3">857.4</grossCalorificValue>
689 - <temp uom="K">71.98</temp>
690 - <pres uom="Pa">49.32</pres>
691 - </volumeValue>
692 - <volume status="bad calibration" uom="m3">99.1</volume>
693 - <volumeStd status="bad calibration" uom="m3">13.42</volumeStd>
694 - <flowRate status="bad calibration" uom="m3/s">73.44</flowRate>
695 - <temp uom="K">42.77</temp>
696 - <pres uom="Pa">53.17</pres>
697 - <absoluteMinPres uom="Pa">57.29</absoluteMinPres>
698 - <portDiff uid="a594539f-bad4-11e1-b23d-c0f8dae91040">
699 - <port uidRef="a59453a0-bad4-11e1-a37c-c0f8dae91040">Port 1</port>
700 - <presDiff uom="Pa">26.17</presDiff>
701 - <tempDiff uom="K">84.48</tempDiff>
702 - <chokeSize uom="in/32">27.72</chokeSize>
703 - <chokeRelative uom="%">20.24</chokeRelative>
704 - </portDiff>
705 - <portDiff uid="a59453a1-bad4-11e1-b446-c0f8dae91040">
706 - <port uidRef="a59453a2-bad4-11e1-aa56-c0f8dae91040">Port 2</port>
707 - <presDiff uom="Pa">52.42</presDiff>
708 - <tempDiff uom="K">27.49</tempDiff>
709 - <chokeSize uom="in/32">24.29</chokeSize>
710 - <chokeRelative uom="%">52.0</chokeRelative>
711 - </portDiff>
712 - <mass uom="kg">215.92</mass>
713 - <work uom="MJ">30.67</work>
714 - <efficiency uom="%">78.11</efficiency>
715 - <rvp uom="Pa">324.12</rvp>
716 - <tvp uom="bar">976.29</tvp>
717 - <bsw uom="%">47.4</bsw>
718 - <bswPrevious uom="m3/m3">67.76</bswPrevious>
719 - <densityValue>
720 - <density uom="kg/m3">662.26</density>
721 - <temp uom="K">16.91</temp>
722 - <pres uom="Pa">38.29</pres>
723 - </densityValue>
724 - <density uom="kg/m3">368.3</density>
725 - <densityFlowRate uom="Mg/a">213.54</densityFlowRate>
726 - <densityStd uom="kg/m3">653.79</densityStd>
727 - <concentration uom="ppm">81.69</concentration>
728 - <molecularWeight>29.26</molecularWeight>
729 - <weightPercent uom="%">33.19</weightPercent>
730 - <molePercent uom="%">99.23</molePercent>
731 - <moleAmt uom="kmol">47.94</moleAmt>
732 - <sg uom="Euc">79.73</sg>
733 - <hcDewpoint uom="K">10.03</hcDewpoint>
734 - <waterDewpoint uom="K">997.84</waterDewpoint>
735 - <wobbeIndex uom="J/m3">30.11</wobbeIndex>
736 - <grossCalorificValueStd uom="J/m3">352.47</grossCalorificValueStd>
737 - <rvpStabilizedCrude uom="Pa">847.36</rvpStabilizedCrude>
738 - <bswStabilizedCrude uom="Euc">511.07</bswStabilizedCrude>
739 - <densityStabilizedCrude uom="kg/m3">866.05</densityStabilizedCrude>
740 - </componentContent>
741 - <period>
742 - <kind>day</kind>
743 - <dateStart>2012-03-01</dateStart>
744 - <dateEnd>2012-03-01</dateEnd>
745 - <gor uom="Euc">11.58</gor>
746 - <gorMTD uom="m3/m3">18.4</gorMTD>
747 - <waterConcMass uom="%">36.78</waterConcMass>
748 - <waterConcVol uom="ppm">50.57</waterConcVol>
749 - <atmosphere uom="Pa">47.47</atmosphere>
750 -
751 - <volumeValue>
752 - <volume uom="L">59.52</volume>
753 - <temp uom="degC">15</temp>
754 - <pres uom="atm">1</pres>
755 - </volumeValue><volume status="bad calibration" uom="m3">95.3</volume>
756 - <volumeStd status="bad calibration" uom="m3">86.7</volumeStd>
757 - <flowRate status="bad calibration" uom="m3/s">11.13</flowRate>
758 - <temp uom="K">65.44</temp>
759 - <pres uom="Pa">69.91</pres>
760 - <absoluteMinPres uom="Pa">81.24</absoluteMinPres>
761 -
762 -
763 - <work uom="J">175.15</work>
764 - <efficiency uom="%">44.51</efficiency>
765 - <rvp uom="atm">390.35</rvp>
766 - <tvp uom="bar">364.31</tvp>
767 - <bsw uom="%">12.64</bsw>
768 - <bswPrevious uom="m3/m3">11.22</bswPrevious>
769 -
770 - <density uom="kg/m3">456.65</density>
771 - <densityFlowRate uom="Mg/a">458.25</densityFlowRate>
772 - <densityStd uom="kg/m3">234.65</densityStd>
773 - <concentration uom="ppm">93.17</concentration>
774 - <molecularWeight>61.41</molecularWeight>
775 - <weightPercent uom="%">93.71</weightPercent>
776 - <molePercent uom="%">80.96</molePercent>
777 - <moleAmt uom="kmol">34.98</moleAmt>
778 - <sg uom="Euc">15.91</sg>
779 - <hcDewpoint uom="K">154.45</hcDewpoint>
780 - <waterDewpoint uom="K">573.72</waterDewpoint>
781 - <wobbeIndex uom="J/m3">790.72</wobbeIndex>
782 - <grossCalorificValueStd uom="J/m3">854.35</grossCalorificValueStd>
783 - <rvpStabilizedCrude uom="Pa">999.73</rvpStabilizedCrude>
784 - <bswStabilizedCrude uom="Euc">590.89</bswStabilizedCrude>
785 - <densityStabilizedCrude uom="kg/m3">739.43</densityStabilizedCrude>
786 - </period>
787 -
788 - </product>
789 - </flow>
790 -
791 -
792 -
793 -
794 - </facility><facility>
795 - <name kind="compressor" namingSystem="STATOIL" uidRef="NaN">TYRIHANS compressor</name>
796 - <facilityParent1 kind="block valve" namingSystem="String" uidRef="x">String</facilityParent1>
797 - <facilityParent2 kind="block valve" namingSystem="String" uidRef="x">String</facilityParent2>
798 - <facilityAlias namingSystem="String">String</facilityAlias>
799 - <facilityAlias namingSystem="String">String</facilityAlias>
800 - <contextFacility kind="block valve" namingSystem="String" uidRef="x">String</contextFacility>
801 - <contextFacility kind="block valve" namingSystem="String" uidRef="x">String</contextFacility>
802 -
803 -
804 -
805 - <flow>
806 - <kind>production</kind>
807 - <qualifier>metered - fiscal</qualifier>
808 - <version>2012-03-01T03:00:00.0Z</version>
809 - <versionSource>version src 974</versionSource>
810 - <gor uom="Euc">35.52</gor>
811 - <gorMTD uom="m3/m3">15.11</gorMTD>
812 - <waterConcMass uom="%">86.31</waterConcMass>
813 - <waterConcVol uom="ppm">42.86</waterConcVol>
814 - <atmosphere uom="Pa">49.52</atmosphere>
815 - <volumeValue>
816 - <volume status="device failure" uom="m3">773.87</volume>
817 - <grossCalorificValue uom="J/m3">694.44</grossCalorificValue>
818 - <temp uom="K">83.41</temp>
819 - <pres uom="Pa">36.72</pres>
820 - </volumeValue>
821 - <volume status="bad calibration" uom="m3">64.39</volume>
822 - <volumeStd status="bad calibration" uom="m3">43.65</volumeStd>
823 - <flowRate status="bad calibration" uom="m3/s">46.86</flowRate>
824 - <temp uom="K">80.75</temp>
825 - <pres uom="Pa">10.23</pres>
826 - <absoluteMinPres uom="Pa">67.92</absoluteMinPres>
827 - <portDiff uid="a5947ab0-bad4-11e1-9447-c0f8dae91040">
828 - <port uidRef="a5947ab1-bad4-11e1-9b4b-c0f8dae91040">Port 1</port>
829 - <presDiff uom="Pa">15.61</presDiff>
830 - <tempDiff uom="K">30.46</tempDiff>
831 - <chokeSize uom="in/32">38.4</chokeSize>
832 - <chokeRelative uom="%">93.09</chokeRelative>
833 - </portDiff>
834 - <portDiff uid="a5947ab2-bad4-11e1-be41-c0f8dae91040">
835 - <port uidRef="a5947ab3-bad4-11e1-86d2-c0f8dae91040">Port 2</port>
836 - <presDiff uom="Pa">32.92</presDiff>
837 - <tempDiff uom="K">91.82</tempDiff>
838 - <chokeSize uom="in/32">57.24</chokeSize>
839 - <chokeRelative uom="%">20.26</chokeRelative>
840 - </portDiff>
841 - <mass uom="kg">213.07</mass>
842 - <work uom="MJ">863.46</work>
843 - <efficiency uom="%">95.65</efficiency>
844 - <rvp uom="Pa">388.96</rvp>
845 - <tvp uom="bar">383.49</tvp>
846 - <bsw uom="%">81.25</bsw>
847 - <bswPrevious uom="m3/m3">20.74</bswPrevious>
848 - <densityValue>
849 - <density uom="kg/m3">42.98</density>
850 - <temp uom="K">82.61</temp>
851 - <pres uom="Pa">22.5</pres>
852 - </densityValue>
853 - <density uom="kg/m3">388.11</density>
854 - <densityFlowRate uom="Mg/a">292.45</densityFlowRate>
855 - <densityStd uom="kg/m3">321.98</densityStd>
856 - <concentration uom="ppm">74.09</concentration>
857 - <molecularWeight>34.21</molecularWeight>
858 - <weightPercent uom="%">58.88</weightPercent>
859 - <molePercent uom="%">72.41</molePercent>
860 - <moleAmt uom="kmol">25.41</moleAmt>
861 - <sg uom="Euc">10.96</sg>
862 - <hcDewpoint uom="K">187.27</hcDewpoint>
863 - <waterDewpoint uom="K">559.4</waterDewpoint>
864 - <wobbeIndex uom="J/m3">211.0</wobbeIndex>
865 - <grossCalorificValueStd uom="J/m3">362.87</grossCalorificValueStd>
866 - <rvpStabilizedCrude uom="Pa">85.82</rvpStabilizedCrude>
867 - <bswStabilizedCrude uom="Euc">659.87</bswStabilizedCrude>
868 - <densityStabilizedCrude uom="kg/m3">806.3</densityStabilizedCrude>
869 - <product>
870 - <kind>oil - net</kind>
871 - <name namingSystem="TEST722">Test product name 264</name>
872 - <splitFactor>0.68</splitFactor>
873 - <gor uom="Euc">22.25</gor>
874 - <gorMTD uom="m3/m3">33.7</gorMTD>
875 - <waterConcMass uom="%">74.49</waterConcMass>
876 - <waterConcVol uom="ppm">75.39</waterConcVol>
877 - <atmosphere uom="Pa">44.42</atmosphere>
878 - <volumeValue>
879 - <volume status="range limit" uom="m3">221.51</volume>
880 - <grossCalorificValue uom="J/m3">981.59</grossCalorificValue>
881 - <temp uom="K">96.24</temp>
882 - <pres uom="Pa">57.34</pres>
883 - </volumeValue>
884 - <volume status="bad calibration" uom="m3">11.95</volume>
885 - <volumeStd status="bad calibration" uom="m3">39.14</volumeStd>
886 - <flowRate status="bad calibration" uom="m3/s">89.55</flowRate>
887 - <temp uom="K">21.21</temp>
888 - <pres uom="Pa">91.15</pres>
889 - <absoluteMinPres uom="Pa">35.26</absoluteMinPres>
890 - <portDiff uid="a594a1c0-bad4-11e1-86bc-c0f8dae91040">
891 - <port uidRef="a594a1c1-bad4-11e1-8aa4-c0f8dae91040">Port 1</port>
892 - <presDiff uom="Pa">95.52</presDiff>
893 - <tempDiff uom="K">80.2</tempDiff>
894 - <chokeSize uom="in/32">70.18</chokeSize>
895 - <chokeRelative uom="%">96.53</chokeRelative>
896 - </portDiff>
897 - <portDiff uid="a594a1c2-bad4-11e1-95a9-c0f8dae91040">
898 - <port uidRef="a594a1c3-bad4-11e1-8626-c0f8dae91040">Port 2</port>
899 - <presDiff uom="Pa">26.71</presDiff>
900 - <tempDiff uom="K">60.83</tempDiff>
901 - <chokeSize uom="in/32">99.35</chokeSize>
902 - <chokeRelative uom="%">10.64</chokeRelative>
903 - </portDiff>
904 - <mass uom="kg">110.74</mass>
905 - <work uom="MJ">133.41</work>
906 - <efficiency uom="%">57.52</efficiency>
907 - <rvp uom="Pa">53.23</rvp>
908 - <tvp uom="bar">67.55</tvp>
909 - <bsw uom="%">86.16</bsw>
910 - <bswPrevious uom="m3/m3">94.84</bswPrevious>
911 - <densityValue>
912 - <density uom="kg/m3">522.77</density>
913 - <temp uom="K">76.29</temp>
914 - <pres uom="Pa">44.64</pres>
915 - </densityValue>
916 - <density uom="kg/m3">207.66</density>
917 - <densityFlowRate uom="Mg/a">566.19</densityFlowRate>
918 - <densityStd uom="kg/m3">699.91</densityStd>
919 - <concentration uom="ppm">47.12</concentration>
920 - <molecularWeight>15.04</molecularWeight>
921 - <weightPercent uom="%">41.72</weightPercent>
922 - <molePercent uom="%">17.4</molePercent>
923 - <moleAmt uom="kmol">96.63</moleAmt>
924 - <sg uom="Euc">66.52</sg>
925 - <hcDewpoint uom="K">41.98</hcDewpoint>
926 - <waterDewpoint uom="K">336.3</waterDewpoint>
927 - <wobbeIndex uom="J/m3">454.09</wobbeIndex>
928 - <grossCalorificValueStd uom="J/m3">582.25</grossCalorificValueStd>
929 - <rvpStabilizedCrude uom="Pa">471.59</rvpStabilizedCrude>
930 - <bswStabilizedCrude uom="Euc">201.79</bswStabilizedCrude>
931 - <densityStabilizedCrude uom="kg/m3">539.47</densityStabilizedCrude>
932 - <componentContent uid="a594c8cf-bad4-11e1-8f50-c0f8dae91040">
933 - <kind>C3-</kind>
934 - <referenceKind>carbon monoxide gas</referenceKind>
935 - <gor uom="Euc">30.35</gor>
936 - <gorMTD uom="m3/m3">51.28</gorMTD>
937 - <waterConcMass uom="%">64.57</waterConcMass>
938 - <waterConcVol uom="ppm">81.28</waterConcVol>
939 - <atmosphere uom="Pa">66.69</atmosphere>
940 - <volumeValue>
941 - <volume status="sensor failure" uom="m3">959.72</volume>
942 - <grossCalorificValue uom="J/m3">11.76</grossCalorificValue>
943 - <temp uom="K">62.44</temp>
944 - <pres uom="Pa">79.62</pres>
945 - </volumeValue>
946 - <volume status="bad calibration" uom="m3">34.82</volume>
947 - <volumeStd status="bad calibration" uom="m3">74.11</volumeStd>
948 - <flowRate status="bad calibration" uom="m3/s">30.08</flowRate>
949 - <temp uom="K">52.87</temp>
950 - <pres uom="Pa">12.73</pres>
951 - <absoluteMinPres uom="Pa">70.57</absoluteMinPres>
952 - <portDiff uid="a594c8d0-bad4-11e1-8cab-c0f8dae91040">
953 - <port uidRef="a594c8d1-bad4-11e1-908b-c0f8dae91040">Port 1</port>
954 - <presDiff uom="Pa">25.53</presDiff>
955 - <tempDiff uom="K">24.35</tempDiff>
956 - <chokeSize uom="in/32">11.2</chokeSize>
957 - <chokeRelative uom="%">23.02</chokeRelative>
958 - </portDiff>
959 - <portDiff uid="a594c8d2-bad4-11e1-9d48-c0f8dae91040">
960 - <port uidRef="a594c8d3-bad4-11e1-b4df-c0f8dae91040">Port 2</port>
961 - <presDiff uom="Pa">94.62</presDiff>
962 - <tempDiff uom="K">57.81</tempDiff>
963 - <chokeSize uom="in/32">95.45</chokeSize>
964 - <chokeRelative uom="%">14.48</chokeRelative>
965 - </portDiff>
966 - <mass uom="kg">217.15</mass>
967 - <work uom="MJ">544.83</work>
968 - <efficiency uom="%">80.0</efficiency>
969 - <rvp uom="Pa">822.33</rvp>
970 - <tvp uom="bar">110.72</tvp>
971 - <bsw uom="%">72.94</bsw>
972 - <bswPrevious uom="m3/m3">38.75</bswPrevious>
973 - <densityValue>
974 - <density uom="kg/m3">61.45</density>
975 - <temp uom="K">42.07</temp>
976 - <pres uom="Pa">37.24</pres>
977 - </densityValue>
978 - <density uom="kg/m3">400.29</density>
979 - <densityFlowRate uom="Mg/a">386.72</densityFlowRate>
980 - <densityStd uom="kg/m3">557.07</densityStd>
981 - <concentration uom="ppm">54.38</concentration>
982 - <molecularWeight>93.53</molecularWeight>
983 - <weightPercent uom="%">14.75</weightPercent>
984 - <molePercent uom="%">67.24</molePercent>
985 - <moleAmt uom="kmol">55.84</moleAmt>
986 - <sg uom="Euc">16.33</sg>
987 - <hcDewpoint uom="K">455.97</hcDewpoint>
988 - <waterDewpoint uom="K">503.48</waterDewpoint>
989 - <wobbeIndex uom="J/m3">248.34</wobbeIndex>
990 - <grossCalorificValueStd uom="J/m3">288.75</grossCalorificValueStd>
991 - <rvpStabilizedCrude uom="Pa">210.29</rvpStabilizedCrude>
992 - <bswStabilizedCrude uom="Euc">51.57</bswStabilizedCrude>
993 - <densityStabilizedCrude uom="kg/m3">88.47</densityStabilizedCrude>
994 - </componentContent>
995 - <period>
996 - <kind>day</kind>
997 - <dateStart>2012-03-01</dateStart>
998 - <dateEnd>2012-03-01</dateEnd>
999 - <gor uom="Euc">56.93</gor>
1000 - <gorMTD uom="m3/m3">70.62</gorMTD>
1001 - <waterConcMass uom="%">70.7</waterConcMass>
1002 - <waterConcVol uom="ppm">83.9</waterConcVol>
1003 - <atmosphere uom="Pa">92.59</atmosphere>
1004 - <volumeValue>
1005 -
1006 - <volume uom="m3">1853.88</volume><temp uom="degC">15</temp>
1007 - <pres uom="atm">1</pres>
1008 - </volumeValue>
1009 - <volume status="bad calibration" uom="m3">67.54</volume>
1010 - <volumeStd status="bad calibration" uom="m3">55.21</volumeStd>
1011 - <flowRate status="bad calibration" uom="m3/s">22.02</flowRate>
1012 - <temp uom="K">66.91</temp>
1013 - <pres uom="Pa">27.85</pres>
1014 - <absoluteMinPres uom="Pa">58.11</absoluteMinPres>
1015 -
1016 - <mass uom="kg">285.7</mass>
1017 - <work uom="kW.h">249.53</work>
1018 - <efficiency uom="%">19.28</efficiency>
1019 - <rvp uom="kPa">81.84</rvp>
1020 - <tvp uom="bar">252.87</tvp>
1021 - <bsw uom="%">36.37</bsw>
1022 - <bswPrevious uom="m3/m3">35.58</bswPrevious>
1023 - <densityValue>
1024 -
1025 - <density uom="kg/m3">786.28</density>
1026 - <temp uom="degC">15</temp>
1027 - <pres uom="atm">1</pres>
1028 - </densityValue>
1029 - <density uom="kg/m3">154.18</density>
1030 - <densityFlowRate uom="Mg/a">478.7</densityFlowRate>
1031 - <densityStd uom="kg/m3">677.04</densityStd>
1032 - <concentration uom="ppm">44.83</concentration>
1033 - <molecularWeight>70.05</molecularWeight>
1034 - <weightPercent uom="%">17.38</weightPercent>
1035 - <molePercent uom="%">51.33</molePercent>
1036 - <moleAmt uom="kmol">96.78</moleAmt>
1037 - <sg uom="Euc">78.21</sg>
1038 - <hcDewpoint uom="K">93.29</hcDewpoint>
1039 - <waterDewpoint uom="K">234.47</waterDewpoint>
1040 - <wobbeIndex uom="J/m3">116.04</wobbeIndex>
1041 - <grossCalorificValueStd uom="J/m3">450.28</grossCalorificValueStd>
1042 - <rvpStabilizedCrude uom="Pa">839.37</rvpStabilizedCrude>
1043 - <bswStabilizedCrude uom="Euc">504.28</bswStabilizedCrude>
1044 - <densityStabilizedCrude uom="kg/m3">993.31</densityStabilizedCrude>
1045 - </period>
1046 -
1047 - </product>
1048 - </flow>
1049 -
1050 -
1051 -
1052 - <flow>
1053 - <kind>injection</kind>
1054 - <qualifier>metered - fiscal</qualifier>
1055 - <version>2012-03-01T19:00:00.0Z</version>
1056 - <versionSource>version src 794</versionSource>
1057 - <gor uom="Euc">46.49</gor>
1058 - <gorMTD uom="m3/m3">92.08</gorMTD>
1059 - <waterConcMass uom="%">20.43</waterConcMass>
1060 - <waterConcVol uom="ppm">32.44</waterConcVol>
1061 - <atmosphere uom="Pa">21.72</atmosphere>
1062 - <volumeValue>
1063 - <volume status="range limit" uom="m3">948.52</volume>
1064 - <grossCalorificValue uom="J/m3">627.63</grossCalorificValue>
1065 - <temp uom="K">30.09</temp>
1066 - <pres uom="Pa">20.19</pres>
1067 - </volumeValue>
1068 - <volume status="bad calibration" uom="m3">96.76</volume>
1069 - <volumeStd status="bad calibration" uom="m3">53.67</volumeStd>
1070 - <flowRate status="bad calibration" uom="m3/s">44.96</flowRate>
1071 - <temp uom="K">17.72</temp>
1072 - <pres uom="Pa">46.28</pres>
1073 - <absoluteMinPres uom="Pa">64.07</absoluteMinPres>
1074 - <portDiff uid="a594efde-bad4-11e1-86cc-c0f8dae91040">
1075 - <port uidRef="a594efdf-bad4-11e1-91c2-c0f8dae91040">Port 1</port>
1076 - <presDiff uom="Pa">96.58</presDiff>
1077 - <tempDiff uom="K">79.73</tempDiff>
1078 - <chokeSize uom="in/32">20.6</chokeSize>
1079 - <chokeRelative uom="%">31.66</chokeRelative>
1080 - </portDiff>
1081 - <portDiff uid="a594efe0-bad4-11e1-bc0c-c0f8dae91040">
1082 - <port uidRef="a594efe1-bad4-11e1-8572-c0f8dae91040">Port 2</port>
1083 - <presDiff uom="Pa">40.89</presDiff>
1084 - <tempDiff uom="K">23.78</tempDiff>
1085 - <chokeSize uom="in/32">34.33</chokeSize>
1086 - <chokeRelative uom="%">28.36</chokeRelative>
1087 - </portDiff>
1088 - <mass uom="kg">187.26</mass>
1089 - <work uom="MJ">405.07</work>
1090 - <efficiency uom="%">28.9</efficiency>
1091 - <rvp uom="Pa">177.55</rvp>
1092 - <tvp uom="bar">274.51</tvp>
1093 - <bsw uom="%">92.53</bsw>
1094 - <bswPrevious uom="m3/m3">83.52</bswPrevious>
1095 - <densityValue>
1096 - <density uom="kg/m3">559.56</density>
1097 - <temp uom="K">56.64</temp>
1098 - <pres uom="Pa">83.99</pres>
1099 - </densityValue>
1100 - <density uom="kg/m3">193.63</density>
1101 - <densityFlowRate uom="Mg/a">81.49</densityFlowRate>
1102 - <densityStd uom="kg/m3">248.0</densityStd>
1103 - <concentration uom="ppm">78.23</concentration>
1104 - <molecularWeight>33.74</molecularWeight>
1105 - <weightPercent uom="%">16.32</weightPercent>
1106 - <molePercent uom="%">75.53</molePercent>
1107 - <moleAmt uom="kmol">58.38</moleAmt>
1108 - <sg uom="Euc">52.82</sg>
1109 - <hcDewpoint uom="K">568.81</hcDewpoint>
1110 - <waterDewpoint uom="K">289.99</waterDewpoint>
1111 - <wobbeIndex uom="J/m3">761.31</wobbeIndex>
1112 - <grossCalorificValueStd uom="J/m3">77.95</grossCalorificValueStd>
1113 - <rvpStabilizedCrude uom="Pa">857.14</rvpStabilizedCrude>
1114 - <bswStabilizedCrude uom="Euc">641.83</bswStabilizedCrude>
1115 - <densityStabilizedCrude uom="kg/m3">877.1</densityStabilizedCrude>
1116 - <product>
1117 - <kind>oil - net</kind>
1118 - <name namingSystem="TEST461">Test product name 963</name>
1119 - <splitFactor>0.88</splitFactor>
1120 - <gor uom="Euc">85.02</gor>
1121 - <gorMTD uom="m3/m3">65.93</gorMTD>
1122 - <waterConcMass uom="%">52.36</waterConcMass>
1123 - <waterConcVol uom="ppm">57.95</waterConcVol>
1124 - <atmosphere uom="Pa">64.13</atmosphere>
1125 - <volumeValue>
1126 - <volume status="range limit" uom="m3">146.14</volume>
1127 - <grossCalorificValue uom="J/m3">391.77</grossCalorificValue>
1128 - <temp uom="K">51.18</temp>
1129 - <pres uom="Pa">65.31</pres>
1130 - </volumeValue>
1131 - <volume status="bad calibration" uom="m3">62.37</volume>
1132 - <volumeStd status="bad calibration" uom="m3">34.97</volumeStd>
1133 - <flowRate status="bad calibration" uom="m3/s">61.68</flowRate>
1134 - <temp uom="K">31.15</temp>
1135 - <pres uom="Pa">58.89</pres>
1136 - <absoluteMinPres uom="Pa">68.44</absoluteMinPres>
1137 - <portDiff uid="a59516f0-bad4-11e1-b4d5-c0f8dae91040">
1138 - <port uidRef="a59516f1-bad4-11e1-8ab5-c0f8dae91040">Port 1</port>
1139 - <presDiff uom="Pa">87.12</presDiff>
1140 - <tempDiff uom="K">12.2</tempDiff>
1141 - <chokeSize uom="in/32">46.71</chokeSize>
1142 - <chokeRelative uom="%">78.09</chokeRelative>
1143 - </portDiff>
1144 - <portDiff uid="a59516f2-bad4-11e1-9b39-c0f8dae91040">
1145 - <port uidRef="a59516f3-bad4-11e1-8b42-c0f8dae91040">Port 2</port>
1146 - <presDiff uom="Pa">75.38</presDiff>
1147 - <tempDiff uom="K">48.86</tempDiff>
1148 - <chokeSize uom="in/32">24.95</chokeSize>
1149 - <chokeRelative uom="%">60.77</chokeRelative>
1150 - </portDiff>
1151 - <mass uom="kg">288.91</mass>
1152 - <work uom="MJ">14.37</work>
1153 - <efficiency uom="%">60.8</efficiency>
1154 - <rvp uom="Pa">805.05</rvp>
1155 - <tvp uom="bar">499.5</tvp>
1156 - <bsw uom="%">85.77</bsw>
1157 - <bswPrevious uom="m3/m3">55.49</bswPrevious>
1158 - <densityValue>
1159 - <density uom="kg/m3">494.4</density>
1160 - <temp uom="K">70.43</temp>
1161 - <pres uom="Pa">59.66</pres>
1162 - </densityValue>
1163 - <density uom="kg/m3">663.33</density>
1164 - <densityFlowRate uom="Mg/a">170.49</densityFlowRate>
1165 - <densityStd uom="kg/m3">251.24</densityStd>
1166 - <concentration uom="ppm">48.7</concentration>
1167 - <molecularWeight>71.03</molecularWeight>
1168 - <weightPercent uom="%">47.07</weightPercent>
1169 - <molePercent uom="%">47.44</molePercent>
1170 - <moleAmt uom="kmol">26.12</moleAmt>
1171 - <sg uom="Euc">70.4</sg>
1172 - <hcDewpoint uom="K">177.28</hcDewpoint>
1173 - <waterDewpoint uom="K">775.28</waterDewpoint>
1174 - <wobbeIndex uom="J/m3">556.7</wobbeIndex>
1175 - <grossCalorificValueStd uom="J/m3">585.16</grossCalorificValueStd>
1176 - <rvpStabilizedCrude uom="Pa">549.22</rvpStabilizedCrude>
1177 - <bswStabilizedCrude uom="Euc">124.52</bswStabilizedCrude>
1178 - <densityStabilizedCrude uom="kg/m3">540.43</densityStabilizedCrude>
1179 - <componentContent uid="a59516f4-bad4-11e1-90c0-c0f8dae91040">
1180 - <kind>aqueous</kind>
1181 - <referenceKind>neopentane</referenceKind>
1182 - <gor uom="Euc">53.44</gor>
1183 - <gorMTD uom="m3/m3">47.79</gorMTD>
1184 - <waterConcMass uom="%">96.69</waterConcMass>
1185 - <waterConcVol uom="ppm">79.13</waterConcVol>
1186 - <atmosphere uom="Pa">63.3</atmosphere>
1187 - <volumeValue>
1188 - <volume status="sensor failure" uom="m3">57.17</volume>
1189 - <grossCalorificValue uom="J/m3">264.73</grossCalorificValue>
1190 - <temp uom="K">11.05</temp>
1191 - <pres uom="Pa">84.52</pres>
1192 - </volumeValue>
1193 - <volume status="bad calibration" uom="m3">79.24</volume>
1194 - <volumeStd status="bad calibration" uom="m3">90.56</volumeStd>
1195 - <flowRate status="bad calibration" uom="m3/s">42.01</flowRate>
1196 - <temp uom="K">27.55</temp>
1197 - <pres uom="Pa">47.34</pres>
1198 - <absoluteMinPres uom="Pa">75.07</absoluteMinPres>
1199 - <portDiff uid="a59516f5-bad4-11e1-9971-c0f8dae91040">
1200 - <port uidRef="a5953e00-bad4-11e1-9080-c0f8dae91040">Port 1</port>
1201 - <presDiff uom="Pa">65.18</presDiff>
1202 - <tempDiff uom="K">92.33</tempDiff>
1203 - <chokeSize uom="in/32">49.71</chokeSize>
1204 - <chokeRelative uom="%">16.17</chokeRelative>
1205 - </portDiff>
1206 - <portDiff uid="a5953e01-bad4-11e1-ac32-c0f8dae91040">
1207 - <port uidRef="a5953e02-bad4-11e1-93d8-c0f8dae91040">Port 2</port>
1208 - <presDiff uom="Pa">89.36</presDiff>
1209 - <tempDiff uom="K">46.85</tempDiff>
1210 - <chokeSize uom="in/32">89.93</chokeSize>
1211 - <chokeRelative uom="%">43.86</chokeRelative>
1212 - </portDiff>
1213 - <mass uom="kg">742.25</mass>
1214 - <work uom="MJ">656.82</work>
1215 - <efficiency uom="%">27.55</efficiency>
1216 - <rvp uom="Pa">66.57</rvp>
1217 - <tvp uom="bar">543.79</tvp>
1218 - <bsw uom="%">40.6</bsw>
1219 - <bswPrevious uom="m3/m3">15.09</bswPrevious>
1220 - <densityValue>
1221 - <density uom="kg/m3">665.18</density>
1222 - <temp uom="K">37.11</temp>
1223 - <pres uom="Pa">38.39</pres>
1224 - </densityValue>
1225 - <density uom="kg/m3">358.27</density>
1226 - <densityFlowRate uom="Mg/a">525.76</densityFlowRate>
1227 - <densityStd uom="kg/m3">615.11</densityStd>
1228 - <concentration uom="ppm">29.01</concentration>
1229 - <molecularWeight>35.13</molecularWeight>
1230 - <weightPercent uom="%">70.55</weightPercent>
1231 - <molePercent uom="%">64.15</molePercent>
1232 - <moleAmt uom="kmol">81.69</moleAmt>
1233 - <sg uom="Euc">20.94</sg>
1234 - <hcDewpoint uom="K">162.95</hcDewpoint>
1235 - <waterDewpoint uom="K">585.5</waterDewpoint>
1236 - <wobbeIndex uom="J/m3">371.93</wobbeIndex>
1237 - <grossCalorificValueStd uom="J/m3">582.81</grossCalorificValueStd>
1238 - <rvpStabilizedCrude uom="Pa">641.21</rvpStabilizedCrude>
1239 - <bswStabilizedCrude uom="Euc">932.05</bswStabilizedCrude>
1240 - <densityStabilizedCrude uom="kg/m3">172.79</densityStabilizedCrude>
1241 - </componentContent>
1242 - <period>
1243 - <kind>day</kind>
1244 - <dateStart>2012-03-01</dateStart>
1245 - <dateEnd>2012-03-01</dateEnd>
1246 - <gor uom="Euc">19.78</gor>
1247 - <gorMTD uom="m3/m3">37.1</gorMTD>
1248 - <waterConcMass uom="%">65.31</waterConcMass>
1249 - <waterConcVol uom="ppm">25.1</waterConcVol>
1250 - <atmosphere uom="Pa">87.71</atmosphere>
1251 - <volumeValue>
1252 -
1253 - <volume uom="m3">1840.26</volume><temp uom="degC">15</temp>
1254 - <pres uom="atm">1</pres>
1255 - </volumeValue>
1256 - <volume status="bad calibration" uom="m3">46.21</volume>
1257 - <volumeStd status="bad calibration" uom="m3">91.31</volumeStd>
1258 - <flowRate status="bad calibration" uom="m3/s">83.51</flowRate>
1259 - <temp uom="K">94.43</temp>
1260 - <pres uom="Pa">49.54</pres>
1261 - <absoluteMinPres uom="Pa">95.99</absoluteMinPres>
1262 -
1263 - <mass uom="kg">227.68</mass>
1264 - <work uom="J">673.21</work>
1265 - <efficiency uom="%">95.47</efficiency>
1266 - <rvp uom="atm">913.47</rvp>
1267 - <tvp uom="bar">66.26</tvp>
1268 - <bsw uom="%">11.43</bsw>
1269 - <bswPrevious uom="m3/m3">17.01</bswPrevious>
1270 - <densityValue>
1271 -
1272 - <density uom="kg/m3">729.18</density>
1273 - <temp uom="degC">15</temp>
1274 - <pres uom="atm">1</pres>
1275 - </densityValue>
1276 - <density uom="kg/m3">22.79</density>
1277 - <densityFlowRate uom="Mg/a">552.38</densityFlowRate>
1278 - <densityStd uom="kg/m3">648.4</densityStd>
1279 - <concentration uom="ppm">18.68</concentration>
1280 - <molecularWeight>70.94</molecularWeight>
1281 - <weightPercent uom="%">75.94</weightPercent>
1282 - <molePercent uom="%">95.19</molePercent>
1283 - <moleAmt uom="kmol">39.95</moleAmt>
1284 - <sg uom="Euc">66.04</sg>
1285 - <hcDewpoint uom="K">510.83</hcDewpoint>
1286 - <waterDewpoint uom="K">758.31</waterDewpoint>
1287 - <wobbeIndex uom="J/m3">22.63</wobbeIndex>
1288 - <grossCalorificValueStd uom="J/m3">439.77</grossCalorificValueStd>
1289 - <rvpStabilizedCrude uom="Pa">161.28</rvpStabilizedCrude>
1290 - <bswStabilizedCrude uom="Euc">103.29</bswStabilizedCrude>
1291 - <densityStabilizedCrude uom="kg/m3">600.54</densityStabilizedCrude>
1292 - </period>
1293 -
1294 - </product>
1295 - </flow>
1296 -
1297 -
1298 -
1299 -
1300 - </facility>
1301 - </object></objects>
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