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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
] ;
rhspin:tableHeaders ("Facility"^^xsd:string "Incident Type"^^xsd:string "Count"^^xsd:string) .
dpr-tables:OtherVolumes
rdf:type rhspin:TableTemplate ;
rdfs:label "Consume, Import, Export, Other Volume List"^^xsd:string ;
rdfs:subClassOf rhspin:DPRTableTemplates ;
spin:body
[ rdf:type sp:Select ;
sp:orderBy ([ sp:varName "flowPurposeName"^^xsd:string
] [ sp:varName "flowInOutFacilityName"^^xsd:string
] [ sp:varName "flowDefinitionName"^^xsd:string
]) ;
sp:resultVariables ([ sp:varName "containingWholeFacilityName"^^xsd:string
] [ sp:varName "flowInOutFacilityName"^^xsd:string
] [ sp:varName "flowPurposeName"^^xsd:string
] [ sp:varName "flowDefinitionName"^^xsd:string
] [ sp:varName "densityValue"^^xsd:string
] [ sp:varName "pressureValue"^^xsd:string
] [ sp:varName "temperatureValue"^^xsd:string
]) ;
sp:where ([ sp:object <http://www.reportinghub.no/ep/schema/report#ProductionReport> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "report"^^xsd:string
]
] [ sp:object
[ sp:varName "report"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/core#partOf> ;
sp:subject
[ sp:varName "productvolumereport"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/report#ProductVolumeReport> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "productvolumereport"^^xsd:string
]
] [ sp:object
[ sp:varName "productionflownetwork"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/report#reportOn> ;
sp:subject
[ sp:varName "productvolumereport"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/flow#ProductionFlowNetwork> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "productionflownetwork"^^xsd:string
]
] [ sp:object
[ sp:varName "flow"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/flow#hasNetworkPart> ;
sp:subject
[ sp:varName "productionflownetwork"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/flow#ProductionFlow> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "flow"^^xsd:string
]
] [ sp:object
[ sp:varName "productionflownetwork"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/flow#facilityContainsFlow> ;
sp:subject
[ sp:varName "productionflownetworkFacility"^^xsd:string
]
] [ sp:object
[ sp:varName "containingWholeFacility"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/core#temporalPartOf> ;
sp:subject
[ sp:varName "productionflownetworkFacility"^^xsd:string
]
] [ sp:object
[ sp:varName "containingWholeFacilityName"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/np/schema/npd#name> ;
sp:subject
[ sp:varName "containingWholeFacility"^^xsd:string
]
] [ sp:object
[ sp:varName "flowWhole"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/core#temporalPartOf> ;
sp:subject
[ sp:varName "flow"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/flow#WholeLifeProductionFlow> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "flowWhole"^^xsd:string
]
] [ sp:object
[ sp:varName "flowInOutFacility"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/flow#flowIntoOrOutOf> ;
sp:subject
[ sp:varName "flowWhole"^^xsd:string
]
] [ rdf:type sp:TriplePath ;
sp:object
[ sp:varName "flowInOutFacilityName"^^xsd:string
] ;
sp:path [ rdf:type sp:AltPath ;
sp:path1 <http://www.reportinghub.no/ep/schema/core#name> ;
sp:path2 <http://www.reportinghub.no/np/schema/npd#name>
] ;
sp:subject
[ sp:varName "flowInOutFacility"^^xsd:string
]
] [ sp:object
[ sp:varName "flowPurpose"^^xsd:string
] ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "flowWhole"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/flow#ProductionFlowPurposeType> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "flowPurpose"^^xsd:string
]
] [ rdf:type sp:Filter ;
sp:expression
[ rdf:type sp:ne ;
sp:arg1 [ sp:varName "flowPurpose"^^xsd:string
] ;
sp:arg2 <http://www.reportinghub.no/ep/schema/flow#Injection>
]
] [ rdf:type sp:Filter ;
sp:expression
[ rdf:type sp:ne ;
sp:arg1 [ sp:varName "flowPurpose"^^xsd:string
] ;
sp:arg2 <http://www.reportinghub.no/ep/schema/flow#Production>
]
] [ sp:object
[ sp:varName "flowPurposeName"^^xsd:string
] ;
sp:predicate rdfs:label ;
sp:subject
[ sp:varName "flowPurpose"^^xsd:string
]
] [ sp:object
[ sp:varName "flowDefinition"^^xsd:string
] ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "flowWhole"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/flow#ProductionFlowDefinitionType> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "flowDefinition"^^xsd:string
]
] [ sp:object
[ sp:varName "flowDefinitionName"^^xsd:string
] ;
sp:predicate rdfs:label ;
sp:subject
[ sp:varName "flowDefinition"^^xsd:string
]
] [ rdf:type sp:Optional ;
sp:elements ([ sp:object
[ sp:varName "temperature"^^xsd:string
] ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "flow"^^xsd:string
]
] [ sp:object
[ sp:varName "density"^^xsd:string
] ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "flow"^^xsd:string
]
] [ sp:object
[ sp:varName "pressure"^^xsd:string
] ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "flow"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/core#Pressure> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "pressure"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/core#Density> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "density"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/core#Temperature> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "temperature"^^xsd:string
]
] [ rdf:type sp:Bind ;
sp:expression
[ rdf:type ep-spin-lib:normalizePropertyUnitAndValue ;
sp:arg1 [ sp:varName "temperature"^^xsd:string
]
] ;
sp:variable
[ sp:varName "temperatureValue"^^xsd:string
]
] [ rdf:type sp:Bind ;
sp:expression
[ rdf:type ep-spin-lib:normalizePropertyUnitAndValue ;
sp:arg1 [ sp:varName "pressure"^^xsd:string
]
] ;
sp:variable
[ sp:varName "pressureValue"^^xsd:string
]
] [ rdf:type sp:Bind ;
sp:expression
[ rdf:type ep-spin-lib:normalizePropertyUnitAndValue ;
sp:arg1 [ sp:varName "density"^^xsd:string
]
] ;
sp:variable
[ sp:varName "densityValue"^^xsd:string
]
])
])
] ;
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) .
dpr-tables:PersonnelInformation
rdf:type rhspin:TableTemplate ;
rdfs:label "Personnel Information"^^xsd:string ;
......@@ -801,98 +1032,648 @@ dpr-tables:PersonnelInformation
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/core#partOf> ;
sp:subject
[ sp:varName "productionOperationReport"^^xsd:string
[ sp:varName "productionOperationReport"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/report#ProductionOperationReport> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "productionOperationReport"^^xsd:string
]
] [ sp:object
[ sp:varName "temporalPartOfFacility"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/report#reportOn> ;
sp:subject
[ sp:varName "productionOperationReport"^^xsd:string
]
] [ sp:object
[ sp:varName "productionFacility"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/core#temporalPartOf> ;
sp:subject
[ sp:varName "temporalPartOfFacility"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/facility#Field> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "productionFacility"^^xsd:string
]
] [ sp:object
[ sp:varName "facilityName"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/np/schema/npd#name> ;
sp:subject
[ sp:varName "productionFacility"^^xsd:string
]
] [ sp:object
[ sp:varName "productionOperationReport"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/core#partOf> ;
sp:subject
[ sp:varName "productionOperationInstallationReport"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/report#ProductionOperationInstallationReport> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "productionOperationInstallationReport"^^xsd:string
]
] [ sp:object
[ sp:varName "installationPart"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/report#reportOn> ;
sp:subject
[ sp:varName "productionOperationInstallationReport"^^xsd:string
]
] [ sp:object
[ sp:varName "crew"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/organization#hasCrew> ;
sp:subject
[ sp:varName "installationPart"^^xsd:string
]
] [ sp:object
[ sp:varName "crewNumber"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/organization#numberInCrew> ;
sp:subject
[ sp:varName "crew"^^xsd:string
]
] [ sp:object
[ sp:varName "crewType"^^xsd:string
] ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "crew"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/organization#CrewType> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "crewType"^^xsd:string
]
] [ sp:object
[ sp:varName "crewTypename"^^xsd:string
] ;
sp:predicate rdfs:label ;
sp:subject
[ sp:varName "crewType"^^xsd:string
]
])
] ;
rhspin:tableHeaders ("Facility"^^xsd:string "Crew"^^xsd:string "Crew Type"^^xsd:string) .
dpr-tables:ProductFlows
rdf:type rhspin:TableTemplate ;
rdfs:label "Product Flow Details"^^xsd:string ;
rdfs:subClassOf rhspin:DPRTableTemplates ;
spin:body
[ rdf:type sp:Select ;
sp:orderBy ([ sp:varName "flowInOutFacilityName"^^xsd:string
] [ sp:varName "flowPurposeName"^^xsd:string
] [ sp:varName "flowDefinitionName"^^xsd:string
] [ sp:varName "productMaterialName"^^xsd:string
]) ;
sp:resultVariables ([ sp:varName "containingWholeFacilityName"^^xsd:string
] [ sp:varName "flowInOutFacilityName"^^xsd:string
] [ sp:varName "flowPurposeName"^^xsd:string
] [ sp:varName "flowDefinitionName"^^xsd:string
] [ sp:varName "productMaterialName"^^xsd:string
] [ sp:varName "densityValue"^^xsd:string
] [ sp:varName "temperatureValue"^^xsd:string
] [ sp:varName "pressureValue"^^xsd:string
]) ;
sp:where ([ sp:object <http://www.reportinghub.no/ep/schema/report#ProductionReport> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "report"^^xsd:string
]
] [ sp:object
[ sp:varName "report"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/core#partOf> ;
sp:subject
[ sp:varName "productvolumereport"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/report#ProductVolumeReport> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "productvolumereport"^^xsd:string
]
] [ sp:object
[ sp:varName "productionflownetwork"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/report#reportOn> ;
sp:subject
[ sp:varName "productvolumereport"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/flow#ProductionFlowNetwork> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "productionflownetwork"^^xsd:string
]
] [ sp:object
[ sp:varName "flow"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/flow#hasNetworkPart> ;
sp:subject
[ sp:varName "productionflownetwork"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/flow#ProductionFlow> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "flow"^^xsd:string
]
] [ sp:object
[ sp:varName "productionflownetwork"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/flow#facilityContainsFlow> ;
sp:subject
[ sp:varName "productionflownetworkFacility"^^xsd:string
]
] [ sp:object
[ sp:varName "containingWholeFacility"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/core#temporalPartOf> ;
sp:subject
[ sp:varName "productionflownetworkFacility"^^xsd:string
]
] [ sp:object
[ sp:varName "containingWholeFacilityName"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/np/schema/npd#name> ;
sp:subject
[ sp:varName "containingWholeFacility"^^xsd:string
]
] [ sp:object
[ sp:varName "flowWhole"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/core#temporalPartOf> ;
sp:subject
[ sp:varName "flow"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/flow#WholeLifeProductionFlow> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "flowWhole"^^xsd:string
]
] [ sp:object
[ sp:varName "flowInOutFacility"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/flow#flowIntoOrOutOf> ;
sp:subject
[ sp:varName "flowWhole"^^xsd:string
]
] [ rdf:type sp:TriplePath ;
sp:object
[ sp:varName "flowInOutFacilityName"^^xsd:string
] ;
sp:path [ rdf:type sp:AltPath ;
sp:path1 <http://www.reportinghub.no/ep/schema/core#name> ;
sp:path2 <http://www.reportinghub.no/np/schema/npd#name>
] ;
sp:subject
[ sp:varName "flowInOutFacility"^^xsd:string
]
] [ sp:object
[ sp:varName "flowPurpose"^^xsd:string
] ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "flowWhole"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/flow#ProductionFlowPurposeType> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "flowPurpose"^^xsd:string
]
] [ rdf:type sp:Filter ;
sp:expression
[ rdf:type sp:eq ;
sp:arg1 [ sp:varName "flowPurpose"^^xsd:string
] ;
sp:arg2 <http://www.reportinghub.no/ep/schema/flow#Production>
]
] [ sp:object
[ sp:varName "flowPurposeName"^^xsd:string
] ;
sp:predicate rdfs:label ;
sp:subject
[ sp:varName "flowPurpose"^^xsd:string
]
] [ sp:object
[ sp:varName "flowDefinition"^^xsd:string
] ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "flowWhole"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/flow#ProductionFlowDefinitionType> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "flowDefinition"^^xsd:string
]
] [ sp:object
[ sp:varName "flowDefinitionName"^^xsd:string
] ;
sp:predicate rdfs:label ;
sp:subject
[ sp:varName "flowDefinition"^^xsd:string
]
] [ rdf:type sp:Optional ;
sp:elements ([ sp:object
[ sp:varName "productFlow"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/flow#hasMixedPart> ;
sp:subject
[ sp:varName "flow"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/flow#ProductFlow> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "productFlow"^^xsd:string
]
] [ sp:object
[ sp:varName "productFlowWholeLife"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/core#temporalPartOf> ;
sp:subject
[ sp:varName "productFlow"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/flow#WholeLifeProductFlow> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "productFlowWholeLife"^^xsd:string
]
] [ sp:object
[ sp:varName "productMaterialType"^^xsd:string
] ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "productFlowWholeLife"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/flow#ProductMaterialType> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "productMaterialType"^^xsd:string
]
] [ sp:object
[ sp:varName "productMaterialName"^^xsd:string
] ;
sp:predicate rdfs:label ;
sp:subject
[ sp:varName "productMaterialType"^^xsd:string
]
] [ rdf:type sp:Optional ;
sp:elements ([ sp:object
[ sp:varName "pressure"^^xsd:string
] ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "productFlow"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/core#Pressure> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "pressure"^^xsd:string
]
] [ rdf:type sp:Bind ;
sp:expression
[ rdf:type ep-spin-lib:normalizePropertyUnitAndValue ;
sp:arg1 [ sp:varName "pressure"^^xsd:string
]
] ;
sp:variable
[ sp:varName "pressureValue"^^xsd:string
]
])
] [ rdf:type sp:Optional ;
sp:elements ([ sp:object
[ sp:varName "temperature"^^xsd:string
] ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "productFlow"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/core#Temperature> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "temperature"^^xsd:string
]
] [ rdf:type sp:Bind ;
sp:expression
[ rdf:type ep-spin-lib:normalizePropertyUnitAndValue ;
sp:arg1 [ sp:varName "temperature"^^xsd:string
]
] ;
sp:variable
[ sp:varName "temperatureValue"^^xsd:string
]
])
] [ rdf:type sp:Optional ;
sp:elements ([ sp:object
[ sp:varName "density"^^xsd:string
] ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "productFlow"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/core#Density> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "density"^^xsd:string
]
] [ rdf:type sp:Bind ;
sp:expression
[ rdf:type ep-spin-lib:normalizePropertyUnitAndValue ;
sp:arg1 [ sp:varName "density"^^xsd:string
]
] ;
sp:variable
[ sp:varName "densityValue"^^xsd:string
]
])
])
])
] ;
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) .
dpr-tables:ProductFlowsInjection
rdf:type rhspin:TableTemplate ;
rdfs:label "Injection Product Flow Details"^^xsd:string ;
rdfs:subClassOf rhspin:DPRTableTemplates ;
spin:body
[ rdf:type sp:Select ;
sp:orderBy ([ sp:varName "flowInOutFacilityName"^^xsd:string
] [ sp:varName "flowPurposeName"^^xsd:string
] [ sp:varName "flowDefinitionName"^^xsd:string
] [ sp:varName "productMaterialName"^^xsd:string
]) ;
sp:resultVariables ([ sp:varName "containingWholeFacilityName"^^xsd:string
] [ sp:varName "flowInOutFacilityName"^^xsd:string
] [ sp:varName "flowPurposeName"^^xsd:string
] [ sp:varName "flowDefinitionName"^^xsd:string
] [ sp:varName "productMaterialName"^^xsd:string
] [ sp:varName "densityValue"^^xsd:string
] [ sp:varName "temperatureValue"^^xsd:string
] [ sp:varName "pressureValue"^^xsd:string
]) ;
sp:where ([ sp:object <http://www.reportinghub.no/ep/schema/report#ProductionReport> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "report"^^xsd:string
]
] [ sp:object
[ sp:varName "report"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/core#partOf> ;
sp:subject
[ sp:varName "productvolumereport"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/report#ProductionOperationReport> ;
] [ sp:object <http://www.reportinghub.no/ep/schema/report#ProductVolumeReport> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "productionOperationReport"^^xsd:string
[ sp:varName "productvolumereport"^^xsd:string
]
] [ sp:object
[ sp:varName "temporalPartOfFacility"^^xsd:string
[ sp:varName "productionflownetwork"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/report#reportOn> ;
sp:subject
[ sp:varName "productionOperationReport"^^xsd:string
[ sp:varName "productvolumereport"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/flow#ProductionFlowNetwork> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "productionflownetwork"^^xsd:string
]
] [ sp:object
[ sp:varName "productionFacility"^^xsd:string
[ sp:varName "flow"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/core#temporalPartOf> ;
sp:predicate <http://www.reportinghub.no/ep/schema/flow#hasNetworkPart> ;
sp:subject
[ sp:varName "temporalPartOfFacility"^^xsd:string
[ sp:varName "productionflownetwork"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/facility#Field> ;
] [ sp:object <http://www.reportinghub.no/ep/schema/flow#ProductionFlow> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "productionFacility"^^xsd:string
[ sp:varName "flow"^^xsd:string
]
] [ sp:object
[ sp:varName "facilityName"^^xsd:string
[ sp:varName "productionflownetwork"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/flow#facilityContainsFlow> ;
sp:subject
[ sp:varName "productionflownetworkFacility"^^xsd:string
]
] [ sp:object
[ sp:varName "containingWholeFacility"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/core#temporalPartOf> ;
sp:subject
[ sp:varName "productionflownetworkFacility"^^xsd:string
]
] [ sp:object
[ sp:varName "containingWholeFacilityName"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/np/schema/npd#name> ;
sp:subject
[ sp:varName "productionFacility"^^xsd:string
[ sp:varName "containingWholeFacility"^^xsd:string
]
] [ sp:object
[ sp:varName "productionOperationReport"^^xsd:string
[ sp:varName "flowWhole"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/core#partOf> ;
sp:predicate <http://www.reportinghub.no/ep/schema/core#temporalPartOf> ;
sp:subject
[ sp:varName "productionOperationInstallationReport"^^xsd:string
[ sp:varName "flow"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/report#ProductionOperationInstallationReport> ;
] [ sp:object <http://www.reportinghub.no/ep/schema/flow#WholeLifeProductionFlow> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "productionOperationInstallationReport"^^xsd:string
[ sp:varName "flowWhole"^^xsd:string
]
] [ sp:object
[ sp:varName "installationPart"^^xsd:string
[ sp:varName "flowInOutFacility"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/report#reportOn> ;
sp:predicate <http://www.reportinghub.no/ep/schema/flow#flowIntoOrOutOf> ;
sp:subject
[ sp:varName "productionOperationInstallationReport"^^xsd:string
[ sp:varName "flowWhole"^^xsd:string
]
] [ rdf:type sp:TriplePath ;
sp:object
[ sp:varName "flowInOutFacilityName"^^xsd:string
] ;
sp:path [ rdf:type sp:AltPath ;
sp:path1 <http://www.reportinghub.no/ep/schema/core#name> ;
sp:path2 <http://www.reportinghub.no/np/schema/npd#name>
] ;
sp:subject
[ sp:varName "flowInOutFacility"^^xsd:string
]
] [ sp:object
[ sp:varName "crew"^^xsd:string
[ sp:varName "flowPurpose"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/organization#hasCrew> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "installationPart"^^xsd:string
[ sp:varName "flowWhole"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/flow#ProductionFlowPurposeType> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "flowPurpose"^^xsd:string
]
] [ rdf:type sp:Filter ;
sp:expression
[ rdf:type sp:eq ;
sp:arg1 [ sp:varName "flowPurpose"^^xsd:string
] ;
sp:arg2 <http://www.reportinghub.no/ep/schema/flow#Injection>
]
] [ sp:object
[ sp:varName "crewNumber"^^xsd:string
[ sp:varName "flowPurposeName"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/organization#numberInCrew> ;
sp:predicate rdfs:label ;
sp:subject
[ sp:varName "crew"^^xsd:string
[ sp:varName "flowPurpose"^^xsd:string
]
] [ sp:object
[ sp:varName "crewType"^^xsd:string
[ sp:varName "flowDefinition"^^xsd:string
] ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "crew"^^xsd:string
[ sp:varName "flowWhole"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/organization#CrewType> ;
] [ sp:object <http://www.reportinghub.no/ep/schema/flow#ProductionFlowDefinitionType> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "crewType"^^xsd:string
[ sp:varName "flowDefinition"^^xsd:string
]
] [ sp:object
[ sp:varName "crewTypename"^^xsd:string
[ sp:varName "flowDefinitionName"^^xsd:string
] ;
sp:predicate rdfs:label ;
sp:subject
[ sp:varName "crewType"^^xsd:string
[ sp:varName "flowDefinition"^^xsd:string
]
] [ rdf:type sp:Optional ;
sp:elements ([ sp:object
[ sp:varName "productFlow"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/flow#hasMixedPart> ;
sp:subject
[ sp:varName "flow"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/flow#ProductFlow> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "productFlow"^^xsd:string
]
] [ sp:object
[ sp:varName "productFlowWholeLife"^^xsd:string
] ;
sp:predicate <http://www.reportinghub.no/ep/schema/core#temporalPartOf> ;
sp:subject
[ sp:varName "productFlow"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/flow#WholeLifeProductFlow> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "productFlowWholeLife"^^xsd:string
]
] [ sp:object
[ sp:varName "productMaterialType"^^xsd:string
] ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "productFlowWholeLife"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/flow#ProductMaterialType> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "productMaterialType"^^xsd:string
]
] [ sp:object
[ sp:varName "productMaterialName"^^xsd:string
] ;
sp:predicate rdfs:label ;
sp:subject
[ sp:varName "productMaterialType"^^xsd:string
]
] [ rdf:type sp:Optional ;
sp:elements ([ sp:object
[ sp:varName "pressure"^^xsd:string
] ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "productFlow"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/core#Pressure> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "pressure"^^xsd:string
]
] [ rdf:type sp:Bind ;
sp:expression
[ rdf:type ep-spin-lib:normalizePropertyUnitAndValue ;
sp:arg1 [ sp:varName "pressure"^^xsd:string
]
] ;
sp:variable
[ sp:varName "pressureValue"^^xsd:string
]
])
] [ rdf:type sp:Optional ;
sp:elements ([ sp:object
[ sp:varName "temperature"^^xsd:string
] ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "productFlow"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/core#Temperature> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "temperature"^^xsd:string
]
] [ rdf:type sp:Bind ;
sp:expression
[ rdf:type ep-spin-lib:normalizePropertyUnitAndValue ;
sp:arg1 [ sp:varName "temperature"^^xsd:string
]
] ;
sp:variable
[ sp:varName "temperatureValue"^^xsd:string
]
])
] [ rdf:type sp:Optional ;
sp:elements ([ sp:object
[ sp:varName "density"^^xsd:string
] ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "productFlow"^^xsd:string
]
] [ sp:object <http://www.reportinghub.no/ep/schema/core#Density> ;
sp:predicate rdf:type ;
sp:subject
[ sp:varName "density"^^xsd:string
]
] [ rdf:type sp:Bind ;
sp:expression
[ rdf:type ep-spin-lib:normalizePropertyUnitAndValue ;
sp:arg1 [ sp:varName "density"^^xsd:string
]
] ;
sp:variable
[ sp:varName "densityValue"^^xsd:string
]
])
])
])
] ;
rhspin:tableHeaders ("Facility"^^xsd:string "Crew"^^xsd:string "Crew Type"^^xsd:string) .
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) .
dpr-tables:ProductFlows
dpr-tables:ProductFlowsOther
rdf:type rhspin:TableTemplate ;
rdfs:label "Product Flow Details"^^xsd:string ;
rdfs:label "Import, Export, Consumet and Other Product Flow Details"^^xsd:string ;
rdfs:subClassOf rhspin:DPRTableTemplates ;
spin:body
[ rdf:type sp:Select ;
......@@ -1014,6 +1795,20 @@ dpr-tables:ProductFlows
sp:subject
[ sp:varName "flowPurpose"^^xsd:string
]
] [ rdf:type sp:Filter ;
sp:expression
[ rdf:type sp:eq ;
sp:arg1 [ sp:varName "flowPurpose"^^xsd:string
] ;
sp:arg2 <http://www.reportinghub.no/ep/schema/flow#Injection>
]
] [ rdf:type sp:Filter ;
sp:expression
[ rdf:type sp:eq ;
sp:arg1 [ sp:varName "flowPurpose"^^xsd:string
] ;
sp:arg2 <http://www.reportinghub.no/ep/schema/flow#Production>
]
] [ sp:object
[ sp:varName "flowPurposeName"^^xsd:string
] ;
......@@ -1316,8 +2111,8 @@ dpr-tables:ProductionVolumes
rdfs:subClassOf rhspin:DPRTableTemplates ;
spin:body
[ rdf:type sp:Select ;
sp:orderBy ([ sp:varName "flowInOutFacilityName"^^xsd:string
] [ sp:varName "flowPurposeName"^^xsd:string
sp:orderBy ([ sp:varName "flowPurposeName"^^xsd:string
] [ sp:varName "flowInOutFacilityName"^^xsd:string
] [ sp:varName "flowDefinitionName"^^xsd:string
]) ;
sp:resultVariables ([ sp:varName "containingWholeFacilityName"^^xsd:string
......@@ -1432,6 +2227,13 @@ dpr-tables:ProductionVolumes
sp:subject
[ sp:varName "flowPurpose"^^xsd:string
]
] [ rdf:type sp:Filter ;
sp:expression
[ rdf:type sp:eq ;
sp:arg1 [ sp:varName "flowPurpose"^^xsd:string
] ;
sp:arg2 <http://www.reportinghub.no/ep/schema/flow#Production>
]
] [ sp:object
[ sp:varName "flowPurposeName"^^xsd:string
] ;
......
......@@ -55,9 +55,17 @@ WHERE {
<dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:ProductionOperationActivity" />
<dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:ProductionVolumes" />
<dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:ProductFlows" />
<dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:InjectionVolumes" />
<dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:ProductFlowsInjection" />
<dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:OtherVolumes" />
<dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:ProductFlowsOther" />
<dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:ProductFlows" />
......
<?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>
<DocumentName namingSystem="EC">ÅSGARD March 2012</DocumentName>
<DocumentAlias namingSystem="EC">ÅSGARD Copex Report</DocumentAlias>
<DocumentDate>2012-03-06T00:00:00.0Z</DocumentDate>
<documentClass namingSystem="EC">Statoil Petroleum AS</documentClass>
<documentClass namingSystem="EC">DPR 2.0</documentClass>
<documentClass namingSystem="ERH">dpr2</documentClass><FileCreationInformation>
<FileCreationDate>2012-03-16T00:00:00.0Z</FileCreationDate>
<SoftwareName>Energy Components</SoftwareName>
<FileCreator>Statoil Petroleum AS</FileCreator>
<Comment>NA</Comment>
</FileCreationInformation>
<Owner>Statoil Petroleum AS</Owner>
</documentInfo><context xsi:type="obj_report">
<kind>DPR 2.0</kind>
<title>ÅSGARD</title>
<date>2012-03-01</date>
<dateEnd>2012-03-01</dateEnd>
<month>2012-03</month>
<year>2012</year>
<reportVersion>1.2</reportVersion>
<reportStatus>final</reportStatus>
<installation kind="field" namingSystem="NPD" uidRef="43765">ÅSGARD</installation>
<operator>
<name>Statoil Petroleum AS</name>
<role>Operating company</role>
</operator>
</context><object xsi:type="obj_productionOperation">
<name>ÅSGARD operation report</name>
<installation kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</installation>
<periodKind>day</periodKind>
<dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
<operator>
<name>Statoil Petroleum AS</name>
<role>Operator</role>
<personName>
<prefix>Mr</prefix>
<first>Test</first>
<last>Dong</last>
</personName>
<address>
<name>Statoil Petroleum AS</name>
<street>Rosenberggate 99</street>
<city>Stavanger</city>
<country>Norway</country>
<postalCode>4002</postalCode>
</address>
</operator>
<title>ÅSGARD operation report</title>
<geographicContext>
<country>Norway</country>
<field namingSystem="DONG">ÅSGARD</field>
</geographicContext>
<issueDate>2012-03-02</issueDate>
<issuedBy>
<name>Statoil Petroleum AS</name>
<role>Operator</role>
<personName>
<prefix>Mr</prefix>
<first>Test</first>
<last>Dong</last>
</personName>
</issuedBy>
<approvalDate>2012-03-02</approvalDate>
<approver>
<name>Statoil Petroleum AS</name>
<role>Platformssjef</role>
<personName>
<prefix>Mr</prefix>
<first>Test</first>
<last>Dong</last>
</personName>
</approver>
<installationReport uid="b13e8911-f359-11e1-a8ee-d067e534860e">
<installation kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</installation>
<bedsAvailable>10</bedsAvailable>
<crewCount type="catering crew">1</crewCount>
<crewCount type="contractor crew">4</crewCount>
<crewCount type="own crew">5</crewCount>
<work uom="h">23</work>
<workMonthToDate uom="d">15</workMonthToDate>
<workYearToDate uom="d">67</workYearToDate>
<operationalHSE>
<IncidentCount>1</IncidentCount>
<sinceLostTime uom="d">10</sinceLostTime>
<sincePreventionExercise uom="d">21</sincePreventionExercise>
<sinceDefinedSituation uom="d">4</sinceDefinedSituation>
<alarmCount>0</alarmCount>
<safetyIntroCount>0</safetyIntroCount>
<safetyDescription>It must be emphasized, once ag</safetyDescription>
<safety>
<meantimeIncident uom="d">0</meantimeIncident>
<safetyCount period="day" type="lost time incident">1</safetyCount>
<safetyCount period="day" type="sick on board">1</safetyCount>
<comment>
<dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
<remark>Furthermore, an important property of these three types of EC is not to be considered in determining</remark>
</comment>
</safety>
<weather>
<dTim>2012-03-01T00:00:00.0Z</dTim>
<agency>Weather agency</agency>
<barometricPressure uom="Pa">58.32</barometricPressure>
<beaufortScaleNumber>10</beaufortScaleNumber>
<tempSurfaceMn uom="degC">15</tempSurfaceMn>
<tempSurfaceMx uom="degC">19</tempSurfaceMx>
<tempWindChill uom="degC">19</tempWindChill>
<tempsea uom="degC">13</tempsea>
<visibility uom="m">638</visibility>
<aziWave uom="rad">1</aziWave>
<htWave uom="m">5</htWave>
<significantWave uom="m">3</significantWave>
<maxWave uom="m">7</maxWave>
<periodWave uom="s">6</periodWave>
<aziWind uom="rad">4</aziWind>
<velWind uom="m/s">6</velWind>
<typePrecip>rain</typePrecip>
<amtPrecip uom="m">5</amtPrecip>
<coverCloud>459</coverCloud>
<ceilingCloud uom="m">178</ceilingCloud>
<currentSea uom="m/s">1</currentSea>
<aziCurrentSea uom="rad">1</aziCurrentSea>
<comments>For one thing, the appearance of parasitic gaps in domains relatively inaccessible to ordinary extra</comments>
</weather>
</operationalHSE>
<productionActivity>
<lostProduction>
<volumeAndReason reasonLost="extended maint turnaround export" uom="m3">1515.91</volumeAndReason>
<volumeAndReason reasonLost="extended maint turnaround" uom="m3">1407.18</volumeAndReason>
<thirdPartyProcessing>
<installation kind="platform">Ekofisk</installation>
<oilStdTempPres uom="m3">1246.33</oilStdTempPres>
<gasStdTempPres uom="m3">1897.53</gasStdTempPres>
</thirdPartyProcessing>
</lostProduction>
<waterCleaningQuality>
<samplePoint>Sample 1</samplePoint>
<oilInWaterProduced uom="Euc">195.36</oilInWaterProduced>
<amountOfOil uom="kg">109.73</amountOfOil>
<ammonium uom="kg/m3">4.31</ammonium>
<totalOrganicCarbon uom="Euc">91.2</totalOrganicCarbon>
<phenol uom="kg/m3">95.62</phenol>
<glycol uom="kg/m3">49.54</glycol>
<phValue>6.17</phValue>
<waterTemperature uom="degC">10.87</waterTemperature>
<residualChloride uom="Euc">168.63</residualChloride>
<oxygen uom="Euc">37.37</oxygen>
<turbidity>118.69</turbidity>
<coulterCounter uom="Euc">51.55</coulterCounter>
<comment>
<dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
<remark>If the position of the trace in (99c) were only relatively inaccessible to movement, this selectiona</remark>
</comment>
</waterCleaningQuality>
<shutdown>
<installation kind="well">String</installation>
<description>Preventive maintenance</description>
<dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
<volumetricDownTime uom="h">22</volumetricDownTime>
<lossOilStdTempPres uom="m3">973.87</lossOilStdTempPres>
<lossGasStdTempPres uom="m3">7360.4</lossGasStdTempPres>
<activity>
<dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
<remark>It appears that the speaker-hearer's linguistic intuition cannot be arbitrary in the ultimate standa</remark>
</activity>
</shutdown>
<alarm>
<dTim>2012-03-01T00:00:00.0Z</dTim>
<area>Area A</area>
<type>Gas Alarm</type>
<reason>Faulty alarm</reason>
<comment>Nevertheless, the descriptive power of the base component raises serious doubts about a corpus of ut</comment>
</alarm>
<marineOperation>
<dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T02:00:00.0Z</dTimEnd>
<generalComment>Clearly, a descriptively adequate grammar is not quite equivalent to a general convention regarding </generalComment>
<supplyShip>Supply 1</supplyShip>
<standbyVessel>Standby 1</standbyVessel>
<supplyShipComment>
<dTimStart>2012-03-01T01:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T06:00:00.0Z</dTimEnd>
<remark>From C1, it follows that the speaker-hearer's linguistic intuition delimits the requirement that bra</remark>
</supplyShipComment>
<supplyShipComment>
<dTimStart>2012-03-01T06:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T08:00:00.0Z</dTimEnd>
<remark>If the position of the trace in (99c) were only relatively inaccessible to movement, most of the met</remark>
</supplyShipComment>
<standbyVesselComment>
<dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
<remark>I suggested that these results would follow from the assumption that the theory of syntactic feature</remark>
</standbyVesselComment>
<basketMovement>
<dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
<remark>With this clarification, this selectionally introduced contextual feature raises serious doubts abou</remark>
</basketMovement>
<basketMovement>
<dTimStart>2012-03-01T02:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T04:00:00.0Z</dTimEnd>
<remark>Notice, incidentally, that relational information delimits the extended c-command discussed in conne</remark>
</basketMovement>
<activity>
<dTimStart>2012-03-01T06:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T08:00:00.0Z</dTimEnd>
<remark>I suggested that these results would follow from the assumption that the notion of level of grammati</remark>
</activity>
<activity>
<dTimStart>2012-03-01T09:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T11:00:00.0Z</dTimEnd>
<remark>However, this assumption is not correct, since the descriptive power of the base component is necess</remark>
</activity>
</marineOperation>
<cargoShipOperation>
<vesselName>Cargo 1</vesselName>
<dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
<captain>Captain 1</captain>
<cargo>Oil</cargo>
<oilGrossStdTempPres uom="m3">6349.63</oilGrossStdTempPres>
<oilGrossTotalStdTempPres uom="m3">6383.1</oilGrossTotalStdTempPres>
<oilNetStdTempPres uom="m3">9682.53</oilNetStdTempPres>
<oilNetMonthToDateStdTempPres uom="m3">6330.86</oilNetMonthToDateStdTempPres>
<densityStdTempPres uom="kg/m3">720.98</densityStdTempPres>
<rvp uom="Pa">167.33</rvp>
<bsw uom="Euc">119.96</bsw>
<salt uom="kg/m3">181.07</salt>
<comment>
<dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
<remark>We will bring evidence in favor of the following thesis: relational information suffices to account </remark>
</comment>
<comment>
<dTimStart>2012-03-01T01:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T02:00:00.0Z</dTimEnd>
<remark>I suggested that these results would follow from the assumption that the speaker-hearer's linguistic</remark>
</comment>
</cargoShipOperation>
<operationalComment>
<type>production</type>
<dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
<comment>To provide a constituent structure for T(Z,K), the speaker-hearer's linguistic intuition is rather d</comment>
</operationalComment>
<operationalComment>
<type>production</type>
<dTimStart>2012-03-01T06:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T12:00:00.0Z</dTimEnd>
<comment>From C1, it follows that the fundamental error of regarding functional notions as categorial appears</comment>
</operationalComment>
</productionActivity>
</installationReport>
</object><object xsi:type="obj_fluidSample">
<name>TYRIHANS-LIQUID-CHARACTERISTICS-1</name>
<sampleType>separator oil</sampleType>
<facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
<acquisitionDate>2012-02-12</acquisitionDate>
<customData>
<extensionNameValue>
<name>ValidFrom</name>
<value>2012-02-12T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
<extensionNameValue>
<name>ValidTo</name>
<value>2012-02-21T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
</customData>
</object><object xsi:type="obj_fluidSample">
<name>TYRIHANS-GAS-CHARACTERISTICS-1</name>
<sampleType>separator gas</sampleType>
<facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
<acquisitionDate>2012-02-11</acquisitionDate>
<customData>
<extensionNameValue>
<name>ValidFrom</name>
<value>2012-02-11T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
<extensionNameValue>
<name>ValidTo</name>
<value>2012-02-21T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
</customData>
</object><object xsi:type="obj_fluidSample">
<name>TYRIHANS-LIQUID-CHARACTERISTICS-2</name>
<sampleType>separator oil</sampleType>
<facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
<acquisitionDate>2012-02-11</acquisitionDate>
<customData>
<extensionNameValue>
<name>ValidFrom</name>
<value>2012-02-11T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
<extensionNameValue>
<name>ValidTo</name>
<value>2012-02-24T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
</customData>
</object><object xsi:type="obj_fluidSample">
<name>TYRIHANS-GAS-CHARACTERISTICS-2</name>
<sampleType>separator gas</sampleType>
<facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
<acquisitionDate>2012-02-15</acquisitionDate>
<customData>
<extensionNameValue>
<name>ValidFrom</name>
<value>2012-02-15T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
<extensionNameValue>
<name>ValidTo</name>
<value>2012-02-28T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
</customData>
</object><object xsi:type="obj_fluidSample">
<name>TYRIHANS-LIQUID-CHARACTERISTICS-3</name>
<sampleType>separator oil</sampleType>
<facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
<acquisitionDate>2012-02-12</acquisitionDate>
<customData>
<extensionNameValue>
<name>ValidFrom</name>
<value>2012-02-12T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
<extensionNameValue>
<name>ValidTo</name>
<value>2012-02-23T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
</customData>
</object><object xsi:type="obj_fluidSample">
<name>TYRIHANS-GAS-CHARACTERISTICS-3</name>
<sampleType>separator gas</sampleType>
<facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
<acquisitionDate>2012-02-12</acquisitionDate>
<customData>
<extensionNameValue>
<name>ValidFrom</name>
<value>2012-02-12T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
<extensionNameValue>
<name>ValidTo</name>
<value>2012-02-22T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
</customData>
</object><object xsi:type="obj_fluidSample">
<name>TYRIHANS-LIQUID-CHARACTERISTICS-1</name>
<sampleType>separator oil</sampleType>
<facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
<acquisitionDate>2012-02-13</acquisitionDate>
<customData>
<extensionNameValue>
<name>ValidFrom</name>
<value>2012-02-13T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
<extensionNameValue>
<name>ValidTo</name>
<value>2012-02-24T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
</customData>
</object><object xsi:type="obj_fluidSample">
<name>TYRIHANS-GAS-CHARACTERISTICS-1</name>
<sampleType>separator gas</sampleType>
<facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
<acquisitionDate>2012-02-14</acquisitionDate>
<customData>
<extensionNameValue>
<name>ValidFrom</name>
<value>2012-02-14T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
<extensionNameValue>
<name>ValidTo</name>
<value>2012-02-26T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
</customData>
</object><object xsi:type="obj_fluidSample">
<name>TYRIHANS-LIQUID-CHARACTERISTICS-2</name>
<sampleType>separator oil</sampleType>
<facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
<acquisitionDate>2012-02-15</acquisitionDate>
<customData>
<extensionNameValue>
<name>ValidFrom</name>
<value>2012-02-15T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
<extensionNameValue>
<name>ValidTo</name>
<value>2012-02-23T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
</customData>
</object><object xsi:type="obj_fluidSample">
<name>TYRIHANS-GAS-CHARACTERISTICS-2</name>
<sampleType>separator gas</sampleType>
<facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
<acquisitionDate>2012-02-13</acquisitionDate>
<customData>
<extensionNameValue>
<name>ValidFrom</name>
<value>2012-02-13T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
<extensionNameValue>
<name>ValidTo</name>
<value>2012-02-27T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
</customData>
</object><object xsi:type="obj_fluidSample">
<name>TYRIHANS-LIQUID-CHARACTERISTICS-3</name>
<sampleType>separator oil</sampleType>
<facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
<acquisitionDate>2012-02-11</acquisitionDate>
<customData>
<extensionNameValue>
<name>ValidFrom</name>
<value>2012-02-11T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
<extensionNameValue>
<name>ValidTo</name>
<value>2012-02-23T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
</customData>
</object><object xsi:type="obj_fluidSample">
<name>TYRIHANS-GAS-CHARACTERISTICS-3</name>
<sampleType>separator gas</sampleType>
<facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
<acquisitionDate>2012-02-13</acquisitionDate>
<customData>
<extensionNameValue>
<name>ValidFrom</name>
<value>2012-02-13T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
<extensionNameValue>
<name>ValidTo</name>
<value>2012-02-21T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
</customData>
</object><object xsi:type="obj_fluidSample">
<name>TYRIHANS-LIQUID-CHARACTERISTICS-1</name>
<sampleType>separator oil</sampleType>
<facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
<acquisitionDate>2012-02-13</acquisitionDate>
<customData>
<extensionNameValue>
<name>ValidFrom</name>
<value>2012-02-13T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
<extensionNameValue>
<name>ValidTo</name>
<value>2012-02-24T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
</customData>
</object><object xsi:type="obj_fluidSample">
<name>TYRIHANS-GAS-CHARACTERISTICS-1</name>
<sampleType>separator gas</sampleType>
<facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
<acquisitionDate>2012-02-13</acquisitionDate>
<customData>
<extensionNameValue>
<name>ValidFrom</name>
<value>2012-02-13T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
<extensionNameValue>
<name>ValidTo</name>
<value>2012-02-27T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
</customData>
</object><object xsi:type="obj_fluidSample">
<name>TYRIHANS-LIQUID-CHARACTERISTICS-2</name>
<sampleType>separator oil</sampleType>
<facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
<acquisitionDate>2012-02-11</acquisitionDate>
<customData>
<extensionNameValue>
<name>ValidFrom</name>
<value>2012-02-11T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
<extensionNameValue>
<name>ValidTo</name>
<value>2012-02-25T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
</customData>
</object><object xsi:type="obj_fluidSample">
<name>TYRIHANS-GAS-CHARACTERISTICS-2</name>
<sampleType>separator gas</sampleType>
<facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
<acquisitionDate>2012-02-15</acquisitionDate>
<customData>
<extensionNameValue>
<name>ValidFrom</name>
<value>2012-02-15T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
<extensionNameValue>
<name>ValidTo</name>
<value>2012-02-26T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
</customData>
</object><object xsi:type="obj_fluidSample">
<name>TYRIHANS-LIQUID-CHARACTERISTICS-3</name>
<sampleType>separator oil</sampleType>
<facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
<acquisitionDate>2012-02-14</acquisitionDate>
<customData>
<extensionNameValue>
<name>ValidFrom</name>
<value>2012-02-14T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
<extensionNameValue>
<name>ValidTo</name>
<value>2012-02-22T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
</customData>
</object><object xsi:type="obj_fluidSample">
<name>TYRIHANS-GAS-CHARACTERISTICS-3</name>
<sampleType>separator gas</sampleType>
<facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
<acquisitionDate>2012-02-12</acquisitionDate>
<customData>
<extensionNameValue>
<name>ValidFrom</name>
<value>2012-02-12T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
<extensionNameValue>
<name>ValidTo</name>
<value>2012-02-24T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
</customData>
</object><object xsi:type="obj_productVolume">
<name>TYRIHANS</name>
<installation kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</installation>
<facility>
<name kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</name>
<facilityParent1 kind="block valve" namingSystem="String" uidRef="x">String</facilityParent1>
<facilityParent2 kind="block valve" namingSystem="String" uidRef="x">String</facilityParent2>
<facilityAlias namingSystem="String">String</facilityAlias>
<facilityAlias namingSystem="String">String</facilityAlias>
<contextFacility kind="block valve" namingSystem="String" uidRef="x">String</contextFacility>
<contextFacility kind="block valve" namingSystem="String" uidRef="x">String</contextFacility>
<downtimeReason uid="b15b5fde-f359-11e1-a318-d067e534860e">
<who>MR Who</who>
<role>Platform manager</role>
<dTimStart>2012-03-01T02:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T04:00:00.0Z</dTimEnd>
<remark>Let us continue to suppose that any associated supporting element is unspecified with respect to an </remark>
</downtimeReason>
<downtimeReason uid="b15b86ee-f359-11e1-a386-d067e534860e">
<who>Mr Who2</who>
<role>Platform manager 2</role>
<dTimStart>2012-03-01T06:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T14:00:00.0Z</dTimEnd>
<remark>It appears that the descriptive power of the base component does not readily tolerate an abstract un</remark>
</downtimeReason>
<flow>
<kind>production</kind>
<qualifier>saleable</qualifier>
<version>2012-03-01T16:00:00.0Z</version>
<versionSource>version src 71</versionSource>
<gor uom="Euc">75.46</gor>
<gorMTD uom="m3/m3">57.69</gorMTD>
<waterConcMass uom="%">35.9</waterConcMass>
<waterConcVol uom="ppm">86.59</waterConcVol>
<atmosphere uom="Pa">28.71</atmosphere>
<volumeValue>
<volume status="bad calibration" uom="m3">834.26</volume>
<grossCalorificValue uom="J/m3">613.16</grossCalorificValue>
<temp uom="K">47.11</temp>
<pres uom="Pa">12.89</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">19.72</volume>
<volumeStd status="bad calibration" uom="m3">89.01</volumeStd>
<flowRate status="bad calibration" uom="m3/s">71.85</flowRate>
<temp uom="K">98.42</temp>
<pres uom="Pa">68.45</pres>
<absoluteMinPres uom="Pa">29.8</absoluteMinPres>
<portDiff uid="b15b86ef-f359-11e1-a5d7-d067e534860e">
<port uidRef="b15b86f0-f359-11e1-9bf6-d067e534860e">Port 1</port>
<presDiff uom="Pa">91.4</presDiff>
<tempDiff uom="K">70.32</tempDiff>
<chokeSize uom="in/32">68.22</chokeSize>
<chokeRelative uom="%">95.71</chokeRelative>
</portDiff>
<portDiff uid="b15b86f1-f359-11e1-8fc8-d067e534860e">
<port uidRef="b15b86f2-f359-11e1-8f01-d067e534860e">Port 2</port>
<presDiff uom="Pa">97.94</presDiff>
<tempDiff uom="K">98.68</tempDiff>
<chokeSize uom="in/32">45.3</chokeSize>
<chokeRelative uom="%">24.82</chokeRelative>
</portDiff>
<mass uom="kg">485.46</mass>
<work uom="MJ">464.84</work>
<efficiency uom="%">70.77</efficiency>
<rvp uom="Pa">262.77</rvp>
<tvp uom="bar">527.14</tvp>
<bsw uom="%">80.9</bsw>
<bswPrevious uom="m3/m3">18.13</bswPrevious>
<densityValue>
<density uom="kg/m3">34.68</density>
<temp uom="K">48.15</temp>
<pres uom="Pa">36.68</pres>
</densityValue>
<density uom="kg/m3">642.61</density>
<densityFlowRate uom="Mg/a">495.01</densityFlowRate>
<densityStd uom="kg/m3">303.76</densityStd>
<concentration uom="ppm">49.74</concentration>
<molecularWeight>42.55</molecularWeight>
<weightPercent uom="%">67.96</weightPercent>
<molePercent uom="%">41.57</molePercent>
<moleAmt uom="kmol">98.22</moleAmt>
<sg uom="Euc">87.09</sg>
<hcDewpoint uom="K">229.53</hcDewpoint>
<waterDewpoint uom="K">880.59</waterDewpoint>
<wobbeIndex uom="J/m3">897.79</wobbeIndex>
<grossCalorificValueStd uom="J/m3">27.92</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">574.9</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">541.59</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">716.88</densityStabilizedCrude>
<product>
<kind>oil - net</kind>
<name namingSystem="TEST954">Test product name 622</name>
<splitFactor>0.65</splitFactor>
<gor uom="Euc">98.73</gor>
<gorMTD uom="m3/m3">84.85</gorMTD>
<waterConcMass uom="%">73.24</waterConcMass>
<waterConcVol uom="ppm">98.74</waterConcVol>
<atmosphere uom="Pa">58.79</atmosphere>
<volumeValue>
<volume status="range limit" uom="m3">880.44</volume>
<grossCalorificValue uom="J/m3">494.48</grossCalorificValue>
<temp uom="K">75.73</temp>
<pres uom="Pa">75.0</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">44.97</volume>
<volumeStd status="bad calibration" uom="m3">92.29</volumeStd>
<flowRate status="bad calibration" uom="m3/s">62.29</flowRate>
<temp uom="K">90.95</temp>
<pres uom="Pa">27.05</pres>
<absoluteMinPres uom="Pa">99.82</absoluteMinPres>
<portDiff uid="b15bae00-f359-11e1-8073-d067e534860e">
<port uidRef="b15bae01-f359-11e1-8368-d067e534860e">Port 1</port>
<presDiff uom="Pa">26.55</presDiff>
<tempDiff uom="K">70.35</tempDiff>
<chokeSize uom="in/32">47.5</chokeSize>
<chokeRelative uom="%">68.21</chokeRelative>
</portDiff>
<portDiff uid="b15bae02-f359-11e1-96c3-d067e534860e">
<port uidRef="b15bae03-f359-11e1-a6c2-d067e534860e">Port 2</port>
<presDiff uom="Pa">61.59</presDiff>
<tempDiff uom="K">94.72</tempDiff>
<chokeSize uom="in/32">75.58</chokeSize>
<chokeRelative uom="%">44.09</chokeRelative>
</portDiff>
<mass uom="kg">388.85</mass>
<work uom="MJ">154.17</work>
<efficiency uom="%">70.62</efficiency>
<rvp uom="Pa">684.1</rvp>
<tvp uom="bar">419.71</tvp>
<bsw uom="%">12.38</bsw>
<bswPrevious uom="m3/m3">40.59</bswPrevious>
<densityValue>
<density uom="kg/m3">373.41</density>
<temp uom="K">36.61</temp>
<pres uom="Pa">80.1</pres>
</densityValue>
<density uom="kg/m3">419.96</density>
<densityFlowRate uom="Mg/a">472.06</densityFlowRate>
<densityStd uom="kg/m3">25.67</densityStd>
<concentration uom="ppm">41.01</concentration>
<molecularWeight>61.05</molecularWeight>
<weightPercent uom="%">80.88</weightPercent>
<molePercent uom="%">55.97</molePercent>
<moleAmt uom="kmol">34.75</moleAmt>
<sg uom="Euc">89.59</sg>
<hcDewpoint uom="K">42.61</hcDewpoint>
<waterDewpoint uom="K">861.58</waterDewpoint>
<wobbeIndex uom="J/m3">994.75</wobbeIndex>
<grossCalorificValueStd uom="J/m3">661.77</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">903.29</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">802.46</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">732.34</densityStabilizedCrude>
<componentContent uid="b15bae04-f359-11e1-928c-d067e534860e">
<kind>diesel</kind>
<referenceKind>aqueous</referenceKind>
<gor uom="Euc">57.74</gor>
<gorMTD uom="m3/m3">76.27</gorMTD>
<waterConcMass uom="%">30.42</waterConcMass>
<waterConcVol uom="ppm">43.48</waterConcVol>
<atmosphere uom="Pa">17.04</atmosphere>
<volumeValue>
<volume status="device failure" uom="m3">825.44</volume>
<grossCalorificValue uom="J/m3">928.39</grossCalorificValue>
<temp uom="K">72.1</temp>
<pres uom="Pa">65.0</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">13.92</volume>
<volumeStd status="bad calibration" uom="m3">30.25</volumeStd>
<flowRate status="bad calibration" uom="m3/s">40.77</flowRate>
<temp uom="K">21.06</temp>
<pres uom="Pa">27.33</pres>
<absoluteMinPres uom="Pa">17.25</absoluteMinPres>
<portDiff uid="b15bd50f-f359-11e1-9159-d067e534860e">
<port uidRef="b15bd510-f359-11e1-9333-d067e534860e">Port 1</port>
<presDiff uom="Pa">19.8</presDiff>
<tempDiff uom="K">24.95</tempDiff>
<chokeSize uom="in/32">34.22</chokeSize>
<chokeRelative uom="%">50.23</chokeRelative>
</portDiff>
<portDiff uid="b15bd511-f359-11e1-a2ee-d067e534860e">
<port uidRef="b15bd512-f359-11e1-b5a7-d067e534860e">Port 2</port>
<presDiff uom="Pa">25.76</presDiff>
<tempDiff uom="K">29.53</tempDiff>
<chokeSize uom="in/32">76.31</chokeSize>
<chokeRelative uom="%">36.08</chokeRelative>
</portDiff>
<mass uom="kg">749.09</mass>
<work uom="MJ">343.14</work>
<efficiency uom="%">36.97</efficiency>
<rvp uom="Pa">677.75</rvp>
<tvp uom="bar">316.01</tvp>
<bsw uom="%">82.71</bsw>
<bswPrevious uom="m3/m3">54.68</bswPrevious>
<densityValue>
<density uom="kg/m3">425.32</density>
<temp uom="K">13.6</temp>
<pres uom="Pa">45.04</pres>
</densityValue>
<density uom="kg/m3">233.23</density>
<densityFlowRate uom="Mg/a">329.23</densityFlowRate>
<densityStd uom="kg/m3">487.14</densityStd>
<concentration uom="ppm">37.94</concentration>
<molecularWeight>47.64</molecularWeight>
<weightPercent uom="%">84.25</weightPercent>
<molePercent uom="%">83.28</molePercent>
<moleAmt uom="kmol">42.97</moleAmt>
<sg uom="Euc">41.5</sg>
<hcDewpoint uom="K">790.71</hcDewpoint>
<waterDewpoint uom="K">877.18</waterDewpoint>
<wobbeIndex uom="J/m3">691.74</wobbeIndex>
<grossCalorificValueStd uom="J/m3">667.72</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">114.98</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">61.25</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">367.63</densityStabilizedCrude>
</componentContent>
<period>
<kind>day</kind>
<dateStart>2012-03-01</dateStart>
<dateEnd>2012-03-01</dateEnd>
<gor uom="Euc">52.02</gor>
<gorMTD uom="m3/m3">59.95</gorMTD>
<waterConcMass uom="%">37.44</waterConcMass>
<waterConcVol uom="ppm">78.68</waterConcVol>
<atmosphere uom="Pa">82.5</atmosphere>
<volumeValue>
<volume uom="m3">2696.85</volume><temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">43.45</volume>
<volumeStd status="bad calibration" uom="m3">41.94</volumeStd>
<flowRate status="bad calibration" uom="m3/s">30.44</flowRate>
<temp uom="K">17.45</temp>
<pres uom="Pa">60.12</pres>
<absoluteMinPres uom="Pa">29.16</absoluteMinPres>
<mass uom="kg">259.85</mass>
<work uom="J">80.56</work>
<efficiency uom="%">73.47</efficiency>
<rvp uom="bar">964.46</rvp>
<tvp uom="bar">759.53</tvp>
<bsw uom="%">35.01</bsw>
<bswPrevious uom="m3/m3">19.09</bswPrevious>
<densityValue>
<density uom="kg/m3">778.74</density>
<temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</densityValue>
<density uom="kg/m3">637.68</density>
<densityFlowRate uom="Mg/a">113.92</densityFlowRate>
<densityStd uom="kg/m3">455.32</densityStd>
<concentration uom="ppm">78.91</concentration>
<molecularWeight>19.7</molecularWeight>
<weightPercent uom="%">79.84</weightPercent>
<molePercent uom="%">72.58</molePercent>
<moleAmt uom="kmol">83.36</moleAmt>
<sg uom="Euc">51.11</sg>
<hcDewpoint uom="K">664.37</hcDewpoint>
<waterDewpoint uom="K">105.18</waterDewpoint>
<wobbeIndex uom="J/m3">847.7</wobbeIndex>
<grossCalorificValueStd uom="J/m3">427.91</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">273.24</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">744.11</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">859.26</densityStabilizedCrude>
</period>
</product>
</flow>
<flow>
<kind>consume - fuel</kind>
<qualifier>allocated</qualifier>
<version>2012-03-01T01:00:00.0Z</version>
<versionSource>version src 623</versionSource>
<gor uom="Euc">68.83</gor>
<gorMTD uom="m3/m3">97.3</gorMTD>
<waterConcMass uom="%">98.72</waterConcMass>
<waterConcVol uom="ppm">91.68</waterConcVol>
<atmosphere uom="Pa">27.77</atmosphere>
<volumeValue>
<volume status="device failure" uom="m3">80.69</volume>
<grossCalorificValue uom="J/m3">582.24</grossCalorificValue>
<temp uom="K">74.63</temp>
<pres uom="Pa">29.01</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">20.84</volume>
<volumeStd status="bad calibration" uom="m3">45.1</volumeStd>
<flowRate status="bad calibration" uom="m3/s">48.81</flowRate>
<temp uom="K">20.51</temp>
<pres uom="Pa">48.91</pres>
<absoluteMinPres uom="Pa">94.27</absoluteMinPres>
<portDiff uid="b15bfc1e-f359-11e1-b6e9-d067e534860e">
<port uidRef="b15bfc1f-f359-11e1-b41f-d067e534860e">Port 1</port>
<presDiff uom="Pa">53.35</presDiff>
<tempDiff uom="K">35.64</tempDiff>
<chokeSize uom="in/32">95.67</chokeSize>
<chokeRelative uom="%">88.74</chokeRelative>
</portDiff>
<portDiff uid="b15bfc20-f359-11e1-8833-d067e534860e">
<port uidRef="b15bfc21-f359-11e1-86ec-d067e534860e">Port 2</port>
<presDiff uom="Pa">81.34</presDiff>
<tempDiff uom="K">79.54</tempDiff>
<chokeSize uom="in/32">85.86</chokeSize>
<chokeRelative uom="%">32.62</chokeRelative>
</portDiff>
<mass uom="kg">524.18</mass>
<work uom="MJ">122.33</work>
<efficiency uom="%">91.84</efficiency>
<rvp uom="Pa">789.55</rvp>
<tvp uom="bar">602.6</tvp>
<bsw uom="%">22.89</bsw>
<bswPrevious uom="m3/m3">49.54</bswPrevious>
<densityValue>
<density uom="kg/m3">506.75</density>
<temp uom="K">26.87</temp>
<pres uom="Pa">32.79</pres>
</densityValue>
<density uom="kg/m3">344.63</density>
<densityFlowRate uom="Mg/a">229.21</densityFlowRate>
<densityStd uom="kg/m3">522.81</densityStd>
<concentration uom="ppm">72.37</concentration>
<molecularWeight>52.41</molecularWeight>
<weightPercent uom="%">67.02</weightPercent>
<molePercent uom="%">62.95</molePercent>
<moleAmt uom="kmol">77.62</moleAmt>
<sg uom="Euc">25.65</sg>
<hcDewpoint uom="K">339.47</hcDewpoint>
<waterDewpoint uom="K">383.0</waterDewpoint>
<wobbeIndex uom="J/m3">324.3</wobbeIndex>
<grossCalorificValueStd uom="J/m3">913.96</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">237.3</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">289.09</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">209.51</densityStabilizedCrude>
<product>
<kind>diesel</kind>
<name namingSystem="TEST949">Test product name 536</name>
<splitFactor>0.11</splitFactor>
<gor uom="Euc">95.69</gor>
<gorMTD uom="m3/m3">32.66</gorMTD>
<waterConcMass uom="%">58.1</waterConcMass>
<waterConcVol uom="ppm">19.2</waterConcVol>
<atmosphere uom="Pa">92.1</atmosphere>
<volumeValue>
<volume status="range limit" uom="m3">366.3</volume>
<grossCalorificValue uom="J/m3">570.6</grossCalorificValue>
<temp uom="K">41.33</temp>
<pres uom="Pa">50.99</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">12.59</volume>
<volumeStd status="bad calibration" uom="m3">63.05</volumeStd>
<flowRate status="bad calibration" uom="m3/s">98.13</flowRate>
<temp uom="K">68.37</temp>
<pres uom="Pa">23.28</pres>
<absoluteMinPres uom="Pa">92.22</absoluteMinPres>
<portDiff uid="b15bfc22-f359-11e1-af66-d067e534860e">
<port uidRef="b15bfc23-f359-11e1-b17d-d067e534860e">Port 1</port>
<presDiff uom="Pa">33.31</presDiff>
<tempDiff uom="K">84.21</tempDiff>
<chokeSize uom="in/32">13.44</chokeSize>
<chokeRelative uom="%">97.63</chokeRelative>
</portDiff>
<portDiff uid="b15c2330-f359-11e1-add9-d067e534860e">
<port uidRef="b15c2331-f359-11e1-ad46-d067e534860e">Port 2</port>
<presDiff uom="Pa">75.85</presDiff>
<tempDiff uom="K">89.75</tempDiff>
<chokeSize uom="in/32">40.06</chokeSize>
<chokeRelative uom="%">70.16</chokeRelative>
</portDiff>
<mass uom="kg">733.99</mass>
<work uom="MJ">835.71</work>
<efficiency uom="%">70.64</efficiency>
<rvp uom="Pa">675.65</rvp>
<tvp uom="bar">532.88</tvp>
<bsw uom="%">38.79</bsw>
<bswPrevious uom="m3/m3">32.91</bswPrevious>
<densityValue>
<density uom="kg/m3">35.09</density>
<temp uom="K">56.34</temp>
<pres uom="Pa">76.01</pres>
</densityValue>
<density uom="kg/m3">160.37</density>
<densityFlowRate uom="Mg/a">420.95</densityFlowRate>
<densityStd uom="kg/m3">548.86</densityStd>
<concentration uom="ppm">25.46</concentration>
<molecularWeight>76.55</molecularWeight>
<weightPercent uom="%">32.03</weightPercent>
<molePercent uom="%">90.69</molePercent>
<moleAmt uom="kmol">82.36</moleAmt>
<sg uom="Euc">22.8</sg>
<hcDewpoint uom="K">986.14</hcDewpoint>
<waterDewpoint uom="K">490.97</waterDewpoint>
<wobbeIndex uom="J/m3">215.6</wobbeIndex>
<grossCalorificValueStd uom="J/m3">939.64</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">62.37</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">580.57</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">445.39</densityStabilizedCrude>
<componentContent uid="b15c2332-f359-11e1-be17-d067e534860e">
<kind>C6-</kind>
<referenceKind>propane</referenceKind>
<gor uom="Euc">94.3</gor>
<gorMTD uom="m3/m3">49.21</gorMTD>
<waterConcMass uom="%">42.65</waterConcMass>
<waterConcVol uom="ppm">95.55</waterConcVol>
<atmosphere uom="Pa">98.22</atmosphere>
<volumeValue>
<volume status="range limit" uom="m3">872.16</volume>
<grossCalorificValue uom="J/m3">292.66</grossCalorificValue>
<temp uom="K">30.17</temp>
<pres uom="Pa">87.79</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">36.67</volume>
<volumeStd status="bad calibration" uom="m3">83.65</volumeStd>
<flowRate status="bad calibration" uom="m3/s">47.6</flowRate>
<temp uom="K">59.59</temp>
<pres uom="Pa">74.77</pres>
<absoluteMinPres uom="Pa">50.9</absoluteMinPres>
<portDiff uid="b15c2333-f359-11e1-bf87-d067e534860e">
<port uidRef="b15c2334-f359-11e1-b1b1-d067e534860e">Port 1</port>
<presDiff uom="Pa">10.46</presDiff>
<tempDiff uom="K">82.76</tempDiff>
<chokeSize uom="in/32">15.31</chokeSize>
<chokeRelative uom="%">45.42</chokeRelative>
</portDiff>
<portDiff uid="b15c2335-f359-11e1-8296-d067e534860e">
<port uidRef="b15c2336-f359-11e1-af3c-d067e534860e">Port 2</port>
<presDiff uom="Pa">20.64</presDiff>
<tempDiff uom="K">24.55</tempDiff>
<chokeSize uom="in/32">90.41</chokeSize>
<chokeRelative uom="%">13.97</chokeRelative>
</portDiff>
<mass uom="kg">486.03</mass>
<work uom="MJ">667.54</work>
<efficiency uom="%">55.01</efficiency>
<rvp uom="Pa">539.8</rvp>
<tvp uom="bar">983.91</tvp>
<bsw uom="%">85.95</bsw>
<bswPrevious uom="m3/m3">69.42</bswPrevious>
<densityValue>
<density uom="kg/m3">83.37</density>
<temp uom="K">27.62</temp>
<pres uom="Pa">74.95</pres>
</densityValue>
<density uom="kg/m3">431.44</density>
<densityFlowRate uom="Mg/a">462.15</densityFlowRate>
<densityStd uom="kg/m3">75.11</densityStd>
<concentration uom="ppm">15.2</concentration>
<molecularWeight>83.02</molecularWeight>
<weightPercent uom="%">28.9</weightPercent>
<molePercent uom="%">40.99</molePercent>
<moleAmt uom="kmol">18.78</moleAmt>
<sg uom="Euc">69.2</sg>
<hcDewpoint uom="K">535.24</hcDewpoint>
<waterDewpoint uom="K">51.07</waterDewpoint>
<wobbeIndex uom="J/m3">514.25</wobbeIndex>
<grossCalorificValueStd uom="J/m3">378.36</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">379.58</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">832.23</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">895.99</densityStabilizedCrude>
</componentContent>
<period>
<kind>day</kind>
<dateStart>2012-03-01</dateStart>
<dateEnd>2012-03-01</dateEnd>
<gor uom="Euc">40.37</gor>
<gorMTD uom="m3/m3">63.45</gorMTD>
<waterConcMass uom="%">24.23</waterConcMass>
<waterConcVol uom="ppm">54.56</waterConcVol>
<atmosphere uom="Pa">23.37</atmosphere>
<volumeValue>
<volume uom="L">249.11</volume>
<temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</volumeValue><volume status="bad calibration" uom="m3">58.75</volume>
<volumeStd status="bad calibration" uom="m3">93.65</volumeStd>
<flowRate status="bad calibration" uom="m3/s">87.15</flowRate>
<temp uom="K">65.52</temp>
<pres uom="Pa">53.15</pres>
<absoluteMinPres uom="Pa">84.14</absoluteMinPres>
<work uom="MJ">234.84</work>
<efficiency uom="%">12.61</efficiency>
<rvp uom="atm">792.71</rvp>
<tvp uom="bar">845.1</tvp>
<bsw uom="%">70.53</bsw>
<bswPrevious uom="m3/m3">55.6</bswPrevious>
<density uom="kg/m3">49.43</density>
<densityFlowRate uom="Mg/a">11.75</densityFlowRate>
<densityStd uom="kg/m3">442.26</densityStd>
<concentration uom="ppm">77.98</concentration>
<molecularWeight>51.9</molecularWeight>
<weightPercent uom="%">12.04</weightPercent>
<molePercent uom="%">89.37</molePercent>
<moleAmt uom="kmol">71.28</moleAmt>
<sg uom="Euc">76.78</sg>
<hcDewpoint uom="K">938.49</hcDewpoint>
<waterDewpoint uom="K">424.25</waterDewpoint>
<wobbeIndex uom="J/m3">409.88</wobbeIndex>
<grossCalorificValueStd uom="J/m3">543.05</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">375.31</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">619.48</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">857.5</densityStabilizedCrude>
</period>
</product>
</flow>
</facility><facility>
<name kind="compressor" namingSystem="STATOIL" uidRef="NaN">TYRIHANS compressor</name>
<facilityParent1 kind="block valve" namingSystem="String" uidRef="x">String</facilityParent1>
<facilityParent2 kind="block valve" namingSystem="String" uidRef="x">String</facilityParent2>
<facilityAlias namingSystem="String">String</facilityAlias>
<facilityAlias namingSystem="String">String</facilityAlias>
<contextFacility kind="block valve" namingSystem="String" uidRef="x">String</contextFacility>
<contextFacility kind="block valve" namingSystem="String" uidRef="x">String</contextFacility>
<flow>
<kind>production</kind>
<qualifier>metered - fiscal</qualifier>
<version>2012-03-01T11:00:00.0Z</version>
<versionSource>version src 707</versionSource>
<gor uom="Euc">40.29</gor>
<gorMTD uom="m3/m3">58.4</gorMTD>
<waterConcMass uom="%">46.58</waterConcMass>
<waterConcVol uom="ppm">81.28</waterConcVol>
<atmosphere uom="Pa">60.96</atmosphere>
<volumeValue>
<volume status="device failure" uom="m3">846.9</volume>
<grossCalorificValue uom="J/m3">828.79</grossCalorificValue>
<temp uom="K">86.07</temp>
<pres uom="Pa">52.18</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">42.06</volume>
<volumeStd status="bad calibration" uom="m3">54.54</volumeStd>
<flowRate status="bad calibration" uom="m3/s">10.81</flowRate>
<temp uom="K">24.9</temp>
<pres uom="Pa">56.33</pres>
<absoluteMinPres uom="Pa">75.4</absoluteMinPres>
<portDiff uid="b15c4a40-f359-11e1-b743-d067e534860e">
<port uidRef="b15c4a41-f359-11e1-9645-d067e534860e">Port 1</port>
<presDiff uom="Pa">11.59</presDiff>
<tempDiff uom="K">87.23</tempDiff>
<chokeSize uom="in/32">22.03</chokeSize>
<chokeRelative uom="%">54.32</chokeRelative>
</portDiff>
<portDiff uid="b15c4a42-f359-11e1-b241-d067e534860e">
<port uidRef="b15c714f-f359-11e1-b6b7-d067e534860e">Port 2</port>
<presDiff uom="Pa">88.87</presDiff>
<tempDiff uom="K">12.18</tempDiff>
<chokeSize uom="in/32">43.28</chokeSize>
<chokeRelative uom="%">33.13</chokeRelative>
</portDiff>
<mass uom="kg">809.05</mass>
<work uom="MJ">900.5</work>
<efficiency uom="%">65.19</efficiency>
<rvp uom="Pa">684.25</rvp>
<tvp uom="bar">160.2</tvp>
<bsw uom="%">14.44</bsw>
<bswPrevious uom="m3/m3">72.93</bswPrevious>
<densityValue>
<density uom="kg/m3">366.4</density>
<temp uom="K">42.15</temp>
<pres uom="Pa">48.97</pres>
</densityValue>
<density uom="kg/m3">110.37</density>
<densityFlowRate uom="Mg/a">245.46</densityFlowRate>
<densityStd uom="kg/m3">383.66</densityStd>
<concentration uom="ppm">59.27</concentration>
<molecularWeight>43.35</molecularWeight>
<weightPercent uom="%">74.89</weightPercent>
<molePercent uom="%">46.25</molePercent>
<moleAmt uom="kmol">74.51</moleAmt>
<sg uom="Euc">37.67</sg>
<hcDewpoint uom="K">553.35</hcDewpoint>
<waterDewpoint uom="K">747.77</waterDewpoint>
<wobbeIndex uom="J/m3">705.92</wobbeIndex>
<grossCalorificValueStd uom="J/m3">560.47</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">143.03</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">747.63</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">286.01</densityStabilizedCrude>
<product>
<kind>oil - net</kind>
<name namingSystem="TEST604">Test product name 986</name>
<splitFactor>0.68</splitFactor>
<gor uom="Euc">54.19</gor>
<gorMTD uom="m3/m3">82.24</gorMTD>
<waterConcMass uom="%">68.88</waterConcMass>
<waterConcVol uom="ppm">51.45</waterConcVol>
<atmosphere uom="Pa">13.95</atmosphere>
<volumeValue>
<volume status="sensor failure" uom="m3">593.81</volume>
<grossCalorificValue uom="J/m3">175.09</grossCalorificValue>
<temp uom="K">35.96</temp>
<pres uom="Pa">64.45</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">37.51</volume>
<volumeStd status="bad calibration" uom="m3">15.96</volumeStd>
<flowRate status="bad calibration" uom="m3/s">13.5</flowRate>
<temp uom="K">87.42</temp>
<pres uom="Pa">68.02</pres>
<absoluteMinPres uom="Pa">84.66</absoluteMinPres>
<portDiff uid="b15c7150-f359-11e1-82e3-d067e534860e">
<port uidRef="b15c7151-f359-11e1-bcb2-d067e534860e">Port 1</port>
<presDiff uom="Pa">29.49</presDiff>
<tempDiff uom="K">77.67</tempDiff>
<chokeSize uom="in/32">30.56</chokeSize>
<chokeRelative uom="%">37.53</chokeRelative>
</portDiff>
<portDiff uid="b15c7152-f359-11e1-a8b9-d067e534860e">
<port uidRef="b15c7153-f359-11e1-81ac-d067e534860e">Port 2</port>
<presDiff uom="Pa">42.83</presDiff>
<tempDiff uom="K">54.87</tempDiff>
<chokeSize uom="in/32">85.52</chokeSize>
<chokeRelative uom="%">34.61</chokeRelative>
</portDiff>
<mass uom="kg">610.56</mass>
<work uom="MJ">128.67</work>
<efficiency uom="%">39.84</efficiency>
<rvp uom="Pa">424.75</rvp>
<tvp uom="bar">57.28</tvp>
<bsw uom="%">75.21</bsw>
<bswPrevious uom="m3/m3">45.62</bswPrevious>
<densityValue>
<density uom="kg/m3">614.43</density>
<temp uom="K">44.32</temp>
<pres uom="Pa">11.68</pres>
</densityValue>
<density uom="kg/m3">503.27</density>
<densityFlowRate uom="Mg/a">392.39</densityFlowRate>
<densityStd uom="kg/m3">17.35</densityStd>
<concentration uom="ppm">38.15</concentration>
<molecularWeight>16.86</molecularWeight>
<weightPercent uom="%">81.26</weightPercent>
<molePercent uom="%">97.92</molePercent>
<moleAmt uom="kmol">58.33</moleAmt>
<sg uom="Euc">52.22</sg>
<hcDewpoint uom="K">430.19</hcDewpoint>
<waterDewpoint uom="K">612.34</waterDewpoint>
<wobbeIndex uom="J/m3">930.22</wobbeIndex>
<grossCalorificValueStd uom="J/m3">976.12</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">157.5</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">657.84</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">875.08</densityStabilizedCrude>
<componentContent uid="b15c985e-f359-11e1-aede-d067e534860e">
<kind>C8-</kind>
<referenceKind>C2+</referenceKind>
<gor uom="Euc">64.08</gor>
<gorMTD uom="m3/m3">86.34</gorMTD>
<waterConcMass uom="%">16.26</waterConcMass>
<waterConcVol uom="ppm">68.4</waterConcVol>
<atmosphere uom="Pa">88.02</atmosphere>
<volumeValue>
<volume status="range limit" uom="m3">728.09</volume>
<grossCalorificValue uom="J/m3">143.82</grossCalorificValue>
<temp uom="K">27.37</temp>
<pres uom="Pa">61.47</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">12.13</volume>
<volumeStd status="bad calibration" uom="m3">20.75</volumeStd>
<flowRate status="bad calibration" uom="m3/s">40.23</flowRate>
<temp uom="K">57.29</temp>
<pres uom="Pa">20.3</pres>
<absoluteMinPres uom="Pa">20.37</absoluteMinPres>
<portDiff uid="b15c985f-f359-11e1-8121-d067e534860e">
<port uidRef="b15c9860-f359-11e1-b1fe-d067e534860e">Port 1</port>
<presDiff uom="Pa">34.64</presDiff>
<tempDiff uom="K">69.4</tempDiff>
<chokeSize uom="in/32">61.98</chokeSize>
<chokeRelative uom="%">84.39</chokeRelative>
</portDiff>
<portDiff uid="b15c9861-f359-11e1-8ce2-d067e534860e">
<port uidRef="b15c9862-f359-11e1-a329-d067e534860e">Port 2</port>
<presDiff uom="Pa">28.03</presDiff>
<tempDiff uom="K">35.98</tempDiff>
<chokeSize uom="in/32">48.71</chokeSize>
<chokeRelative uom="%">42.2</chokeRelative>
</portDiff>
<mass uom="kg">34.7</mass>
<work uom="MJ">311.65</work>
<efficiency uom="%">36.41</efficiency>
<rvp uom="Pa">283.92</rvp>
<tvp uom="bar">81.56</tvp>
<bsw uom="%">29.64</bsw>
<bswPrevious uom="m3/m3">47.54</bswPrevious>
<densityValue>
<density uom="kg/m3">403.34</density>
<temp uom="K">96.81</temp>
<pres uom="Pa">58.59</pres>
</densityValue>
<density uom="kg/m3">415.33</density>
<densityFlowRate uom="Mg/a">95.9</densityFlowRate>
<densityStd uom="kg/m3">555.16</densityStd>
<concentration uom="ppm">74.38</concentration>
<molecularWeight>81.82</molecularWeight>
<weightPercent uom="%">62.0</weightPercent>
<molePercent uom="%">25.84</molePercent>
<moleAmt uom="kmol">17.98</moleAmt>
<sg uom="Euc">60.75</sg>
<hcDewpoint uom="K">538.39</hcDewpoint>
<waterDewpoint uom="K">713.48</waterDewpoint>
<wobbeIndex uom="J/m3">414.86</wobbeIndex>
<grossCalorificValueStd uom="J/m3">696.02</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">40.25</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">144.32</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">449.68</densityStabilizedCrude>
</componentContent>
<period>
<kind>day</kind>
<dateStart>2012-03-01</dateStart>
<dateEnd>2012-03-01</dateEnd>
<gor uom="Euc">82.02</gor>
<gorMTD uom="m3/m3">48.04</gorMTD>
<waterConcMass uom="%">36.29</waterConcMass>
<waterConcVol uom="ppm">31.71</waterConcVol>
<atmosphere uom="Pa">70.55</atmosphere>
<volumeValue>
<volume uom="m3">135.02</volume><temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">18.4</volume>
<volumeStd status="bad calibration" uom="m3">18.47</volumeStd>
<flowRate status="bad calibration" uom="m3/s">74.13</flowRate>
<temp uom="K">64.83</temp>
<pres uom="Pa">67.8</pres>
<absoluteMinPres uom="Pa">19.88</absoluteMinPres>
<mass uom="kg">248.48</mass>
<work uom="MJ">713.54</work>
<efficiency uom="%">35.75</efficiency>
<rvp uom="kPa">95.73</rvp>
<tvp uom="bar">222.27</tvp>
<bsw uom="%">39.13</bsw>
<bswPrevious uom="m3/m3">60.56</bswPrevious>
<densityValue>
<density uom="kg/m3">764.0</density>
<temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</densityValue>
<density uom="kg/m3">44.25</density>
<densityFlowRate uom="Mg/a">337.54</densityFlowRate>
<densityStd uom="kg/m3">129.72</densityStd>
<concentration uom="ppm">50.71</concentration>
<molecularWeight>90.62</molecularWeight>
<weightPercent uom="%">17.46</weightPercent>
<molePercent uom="%">21.28</molePercent>
<moleAmt uom="kmol">79.29</moleAmt>
<sg uom="Euc">36.83</sg>
<hcDewpoint uom="K">581.7</hcDewpoint>
<waterDewpoint uom="K">52.64</waterDewpoint>
<wobbeIndex uom="J/m3">35.57</wobbeIndex>
<grossCalorificValueStd uom="J/m3">875.14</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">128.34</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">300.49</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">809.42</densityStabilizedCrude>
</period>
</product>
</flow>
<flow>
<kind>injection</kind>
<qualifier>metered - fiscal</qualifier>
<version>2012-03-01T04:00:00.0Z</version>
<versionSource>version src 635</versionSource>
<gor uom="Euc">62.59</gor>
<gorMTD uom="m3/m3">99.11</gorMTD>
<waterConcMass uom="%">71.6</waterConcMass>
<waterConcVol uom="ppm">34.53</waterConcVol>
<atmosphere uom="Pa">59.4</atmosphere>
<volumeValue>
<volume status="comm failure" uom="m3">180.82</volume>
<grossCalorificValue uom="J/m3">511.05</grossCalorificValue>
<temp uom="K">86.78</temp>
<pres uom="Pa">73.71</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">72.43</volume>
<volumeStd status="bad calibration" uom="m3">11.29</volumeStd>
<flowRate status="bad calibration" uom="m3/s">74.12</flowRate>
<temp uom="K">90.24</temp>
<pres uom="Pa">39.52</pres>
<absoluteMinPres uom="Pa">80.54</absoluteMinPres>
<portDiff uid="b15cbf70-f359-11e1-ad49-d067e534860e">
<port uidRef="b15cbf71-f359-11e1-8997-d067e534860e">Port 1</port>
<presDiff uom="Pa">69.24</presDiff>
<tempDiff uom="K">57.28</tempDiff>
<chokeSize uom="in/32">45.47</chokeSize>
<chokeRelative uom="%">33.96</chokeRelative>
</portDiff>
<portDiff uid="b15cbf72-f359-11e1-88aa-d067e534860e">
<port uidRef="b15cbf73-f359-11e1-b8b2-d067e534860e">Port 2</port>
<presDiff uom="Pa">48.38</presDiff>
<tempDiff uom="K">82.09</tempDiff>
<chokeSize uom="in/32">68.67</chokeSize>
<chokeRelative uom="%">79.74</chokeRelative>
</portDiff>
<mass uom="kg">29.0</mass>
<work uom="MJ">876.38</work>
<efficiency uom="%">74.86</efficiency>
<rvp uom="Pa">80.38</rvp>
<tvp uom="bar">539.07</tvp>
<bsw uom="%">39.49</bsw>
<bswPrevious uom="m3/m3">52.6</bswPrevious>
<densityValue>
<density uom="kg/m3">157.53</density>
<temp uom="K">41.94</temp>
<pres uom="Pa">95.81</pres>
</densityValue>
<density uom="kg/m3">363.73</density>
<densityFlowRate uom="Mg/a">195.69</densityFlowRate>
<densityStd uom="kg/m3">447.12</densityStd>
<concentration uom="ppm">15.57</concentration>
<molecularWeight>63.44</molecularWeight>
<weightPercent uom="%">37.6</weightPercent>
<molePercent uom="%">48.26</molePercent>
<moleAmt uom="kmol">25.89</moleAmt>
<sg uom="Euc">42.71</sg>
<hcDewpoint uom="K">289.18</hcDewpoint>
<waterDewpoint uom="K">37.94</waterDewpoint>
<wobbeIndex uom="J/m3">477.46</wobbeIndex>
<grossCalorificValueStd uom="J/m3">661.2</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">854.6</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">756.71</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">774.01</densityStabilizedCrude>
<product>
<kind>oil - net</kind>
<name namingSystem="TEST443">Test product name 256</name>
<splitFactor>0.09</splitFactor>
<gor uom="Euc">94.36</gor>
<gorMTD uom="m3/m3">80.11</gorMTD>
<waterConcMass uom="%">41.65</waterConcMass>
<waterConcVol uom="ppm">95.09</waterConcVol>
<atmosphere uom="Pa">67.78</atmosphere>
<volumeValue>
<volume status="bad calibration" uom="m3">757.3</volume>
<grossCalorificValue uom="J/m3">513.29</grossCalorificValue>
<temp uom="K">72.66</temp>
<pres uom="Pa">39.02</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">62.8</volume>
<volumeStd status="bad calibration" uom="m3">20.85</volumeStd>
<flowRate status="bad calibration" uom="m3/s">72.97</flowRate>
<temp uom="K">89.41</temp>
<pres uom="Pa">21.68</pres>
<absoluteMinPres uom="Pa">57.03</absoluteMinPres>
<portDiff uid="b15ce680-f359-11e1-85ee-d067e534860e">
<port uidRef="b15ce681-f359-11e1-8bc7-d067e534860e">Port 1</port>
<presDiff uom="Pa">33.98</presDiff>
<tempDiff uom="K">62.45</tempDiff>
<chokeSize uom="in/32">28.8</chokeSize>
<chokeRelative uom="%">76.87</chokeRelative>
</portDiff>
<portDiff uid="b15ce682-f359-11e1-97c0-d067e534860e">
<port uidRef="b15ce683-f359-11e1-8acf-d067e534860e">Port 2</port>
<presDiff uom="Pa">38.76</presDiff>
<tempDiff uom="K">99.18</tempDiff>
<chokeSize uom="in/32">79.9</chokeSize>
<chokeRelative uom="%">49.16</chokeRelative>
</portDiff>
<mass uom="kg">508.55</mass>
<work uom="MJ">457.39</work>
<efficiency uom="%">92.64</efficiency>
<rvp uom="Pa">511.71</rvp>
<tvp uom="bar">832.56</tvp>
<bsw uom="%">28.79</bsw>
<bswPrevious uom="m3/m3">55.61</bswPrevious>
<densityValue>
<density uom="kg/m3">482.8</density>
<temp uom="K">96.1</temp>
<pres uom="Pa">44.6</pres>
</densityValue>
<density uom="kg/m3">144.01</density>
<densityFlowRate uom="Mg/a">456.76</densityFlowRate>
<densityStd uom="kg/m3">31.37</densityStd>
<concentration uom="ppm">45.21</concentration>
<molecularWeight>76.82</molecularWeight>
<weightPercent uom="%">71.14</weightPercent>
<molePercent uom="%">18.61</molePercent>
<moleAmt uom="kmol">14.59</moleAmt>
<sg uom="Euc">20.78</sg>
<hcDewpoint uom="K">182.36</hcDewpoint>
<waterDewpoint uom="K">58.41</waterDewpoint>
<wobbeIndex uom="J/m3">189.42</wobbeIndex>
<grossCalorificValueStd uom="J/m3">542.81</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">151.96</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">229.69</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">718.59</densityStabilizedCrude>
<componentContent uid="b15ce684-f359-11e1-a8e5-d067e534860e">
<kind>C6-</kind>
<referenceKind>C5+</referenceKind>
<gor uom="Euc">20.4</gor>
<gorMTD uom="m3/m3">12.0</gorMTD>
<waterConcMass uom="%">67.31</waterConcMass>
<waterConcVol uom="ppm">13.53</waterConcVol>
<atmosphere uom="Pa">78.48</atmosphere>
<volumeValue>
<volume status="comm failure" uom="m3">262.35</volume>
<grossCalorificValue uom="J/m3">747.49</grossCalorificValue>
<temp uom="K">52.64</temp>
<pres uom="Pa">58.56</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">21.98</volume>
<volumeStd status="bad calibration" uom="m3">23.07</volumeStd>
<flowRate status="bad calibration" uom="m3/s">31.8</flowRate>
<temp uom="K">12.52</temp>
<pres uom="Pa">66.24</pres>
<absoluteMinPres uom="Pa">24.06</absoluteMinPres>
<portDiff uid="b15ce685-f359-11e1-b3b7-d067e534860e">
<port uidRef="b15d0d8f-f359-11e1-a065-d067e534860e">Port 1</port>
<presDiff uom="Pa">24.07</presDiff>
<tempDiff uom="K">42.02</tempDiff>
<chokeSize uom="in/32">20.44</chokeSize>
<chokeRelative uom="%">89.75</chokeRelative>
</portDiff>
<portDiff uid="b15d0d90-f359-11e1-9858-d067e534860e">
<port uidRef="b15d0d91-f359-11e1-9dbc-d067e534860e">Port 2</port>
<presDiff uom="Pa">86.21</presDiff>
<tempDiff uom="K">50.68</tempDiff>
<chokeSize uom="in/32">76.78</chokeSize>
<chokeRelative uom="%">87.98</chokeRelative>
</portDiff>
<mass uom="kg">383.68</mass>
<work uom="MJ">218.22</work>
<efficiency uom="%">14.2</efficiency>
<rvp uom="Pa">709.92</rvp>
<tvp uom="bar">728.89</tvp>
<bsw uom="%">46.3</bsw>
<bswPrevious uom="m3/m3">50.8</bswPrevious>
<densityValue>
<density uom="kg/m3">223.38</density>
<temp uom="K">26.59</temp>
<pres uom="Pa">65.64</pres>
</densityValue>
<density uom="kg/m3">389.51</density>
<densityFlowRate uom="Mg/a">308.61</densityFlowRate>
<densityStd uom="kg/m3">583.86</densityStd>
<concentration uom="ppm">55.73</concentration>
<molecularWeight>43.32</molecularWeight>
<weightPercent uom="%">35.54</weightPercent>
<molePercent uom="%">64.1</molePercent>
<moleAmt uom="kmol">49.82</moleAmt>
<sg uom="Euc">34.66</sg>
<hcDewpoint uom="K">384.87</hcDewpoint>
<waterDewpoint uom="K">652.28</waterDewpoint>
<wobbeIndex uom="J/m3">126.49</wobbeIndex>
<grossCalorificValueStd uom="J/m3">636.51</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">408.77</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">594.39</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">803.93</densityStabilizedCrude>
</componentContent>
<period>
<kind>day</kind>
<dateStart>2012-03-01</dateStart>
<dateEnd>2012-03-01</dateEnd>
<gor uom="Euc">72.91</gor>
<gorMTD uom="m3/m3">58.35</gorMTD>
<waterConcMass uom="%">32.95</waterConcMass>
<waterConcVol uom="ppm">16.43</waterConcVol>
<atmosphere uom="Pa">72.86</atmosphere>
<volumeValue>
<volume uom="m3">1942.69</volume><temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">29.66</volume>
<volumeStd status="bad calibration" uom="m3">66.4</volumeStd>
<flowRate status="bad calibration" uom="m3/s">52.11</flowRate>
<temp uom="K">74.04</temp>
<pres uom="Pa">50.23</pres>
<absoluteMinPres uom="Pa">59.9</absoluteMinPres>
<mass uom="kg">634.99</mass>
<work uom="MJ">307.21</work>
<efficiency uom="%">80.38</efficiency>
<rvp uom="kPa">871.12</rvp>
<tvp uom="bar">138.67</tvp>
<bsw uom="%">60.01</bsw>
<bswPrevious uom="m3/m3">28.12</bswPrevious>
<densityValue>
<density uom="kg/m3">792.8</density>
<temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</densityValue>
<density uom="kg/m3">108.13</density>
<densityFlowRate uom="Mg/a">355.61</densityFlowRate>
<densityStd uom="kg/m3">232.29</densityStd>
<concentration uom="ppm">44.72</concentration>
<molecularWeight>19.96</molecularWeight>
<weightPercent uom="%">15.14</weightPercent>
<molePercent uom="%">95.88</molePercent>
<moleAmt uom="kmol">67.42</moleAmt>
<sg uom="Euc">98.09</sg>
<hcDewpoint uom="K">829.2</hcDewpoint>
<waterDewpoint uom="K">803.34</waterDewpoint>
<wobbeIndex uom="J/m3">223.36</wobbeIndex>
<grossCalorificValueStd uom="J/m3">318.81</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">793.94</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">171.79</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">750.3</densityStabilizedCrude>
</period>
</product>
</flow>
</facility>
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<name>TYRIHANS-LIQUID-CHARACTERISTICS-1</name>
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<name>TYRIHANS-LIQUID-CHARACTERISTICS-1</name>
<sampleType>separator oil</sampleType>
<facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
<acquisitionDate>2012-02-12</acquisitionDate>
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<name>TYRIHANS-GAS-CHARACTERISTICS-1</name>
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<facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
<acquisitionDate>2012-02-13</acquisitionDate>
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<facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
<acquisitionDate>2012-02-11</acquisitionDate>
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<name>TYRIHANS-GAS-CHARACTERISTICS-2</name>
<sampleType>separator gas</sampleType>
<facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
<acquisitionDate>2012-02-15</acquisitionDate>
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<name>TYRIHANS-LIQUID-CHARACTERISTICS-3</name>
<sampleType>separator oil</sampleType>
<facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
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<name>TYRIHANS-GAS-CHARACTERISTICS-3</name>
<sampleType>separator gas</sampleType>
<facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility>
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<?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>
<DocumentName namingSystem="EC">ÅSGARD March 2012</DocumentName>
<DocumentAlias namingSystem="EC">ÅSGARD Copex Report</DocumentAlias>
<DocumentDate>2012-03-06T00:00:00.0Z</DocumentDate>
<documentClass namingSystem="EC">Statoil Petroleum AS</documentClass>
<documentClass namingSystem="EC">DPR 2.0</documentClass>
<documentClass namingSystem="ERH">dpr2</documentClass><FileCreationInformation>
<FileCreationDate>2012-03-16T00:00:00.0Z</FileCreationDate>
<SoftwareName>Energy Components</SoftwareName>
<FileCreator>Statoil Petroleum AS</FileCreator>
<Comment>NA</Comment>
</FileCreationInformation>
<Owner>Statoil Petroleum AS</Owner>
</documentInfo><context xsi:type="obj_report">
<kind>DPR 2.0</kind>
<title>ÅSGARD</title>
<date>2012-03-01</date>
<dateEnd>2012-03-01</dateEnd>
<month>2012-03</month>
<year>2012</year>
<reportVersion>2.0</reportVersion>
<reportStatus>final</reportStatus>
<installation kind="field" namingSystem="NPD" uidRef="43765">ÅSGARD</installation>
<operator>
<name>Statoil Petroleum AS</name>
<role>Operating company</role>
</operator>
</context><object xsi:type="obj_productionOperation">
<name>ÅSGARD operation report</name>
<installation kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</installation>
<periodKind>day</periodKind>
<dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
<operator>
<name>Statoil Petroleum AS</name>
<role>Operator</role>
<personName>
<prefix>Mr</prefix>
<first>Test</first>
<last>Dong</last>
</personName>
<address>
<name>Statoil Petroleum AS</name>
<street>Rosenberggate 99</street>
<city>Stavanger</city>
<country>Norway</country>
<postalCode>4002</postalCode>
</address>
</operator>
<title>ÅSGARD operation report</title>
<geographicContext>
<country>Norway</country>
<field namingSystem="DONG">ÅSGARD</field>
</geographicContext>
<issueDate>2012-03-02</issueDate>
<issuedBy>
<name>Statoil Petroleum AS</name>
<role>Operator</role>
<personName>
<prefix>Mr</prefix>
<first>Test</first>
<last>Dong</last>
</personName>
</issuedBy>
<approvalDate>2012-03-02</approvalDate>
<approver>
<name>Statoil Petroleum AS</name>
<role>Platformssjef</role>
<personName>
<prefix>Mr</prefix>
<first>Test</first>
<last>Dong</last>
</personName>
</approver>
<installationReport uid="a57d492e-bad4-11e1-963a-c0f8dae91040">
<installation kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</installation>
<bedsAvailable>10</bedsAvailable>
<crewCount type="catering crew">1</crewCount>
<crewCount type="contractor crew">4</crewCount>
<crewCount type="own crew">5</crewCount>
<work uom="h">22</work>
<workMonthToDate uom="d">23</workMonthToDate>
<workYearToDate uom="d">62</workYearToDate>
<operationalHSE>
<IncidentCount>1</IncidentCount>
<sinceLostTime uom="d">10</sinceLostTime>
<sincePreventionExercise uom="d">13</sincePreventionExercise>
<sinceDefinedSituation uom="d">2</sinceDefinedSituation>
<alarmCount>0</alarmCount>
<safetyIntroCount>0</safetyIntroCount>
<safetyDescription>I suggested that these results</safetyDescription>
<safety>
<meantimeIncident uom="d">2</meantimeIncident>
<safetyCount period="day" type="lost time incident">1</safetyCount>
<safetyCount period="day" type="sick on board">1</safetyCount>
<comment>
<dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
<remark>It may be, then, that the notion of level of grammaticalness is unspecified with respect to a parasi</remark>
</comment>
</safety>
<weather>
<dTim>2012-03-01T00:00:00.0Z</dTim>
<agency>Weather agency</agency>
<barometricPressure uom="Pa">57.56</barometricPressure>
<beaufortScaleNumber>5</beaufortScaleNumber>
<tempSurfaceMn uom="degC">15</tempSurfaceMn>
<tempSurfaceMx uom="degC">12</tempSurfaceMx>
<tempWindChill uom="degC">13</tempWindChill>
<tempsea uom="degC">13</tempsea>
<visibility uom="m">391</visibility>
<aziWave uom="rad">9</aziWave>
<htWave uom="m">7</htWave>
<significantWave uom="m">6</significantWave>
<maxWave uom="m">2</maxWave>
<periodWave uom="s">3</periodWave>
<aziWind uom="rad">2</aziWind>
<velWind uom="m/s">9</velWind>
<typePrecip>rain</typePrecip>
<amtPrecip uom="m">3</amtPrecip>
<coverCloud>180</coverCloud>
<ceilingCloud uom="m">230</ceilingCloud>
<currentSea uom="m/s">1</currentSea>
<aziCurrentSea uom="rad">3</aziCurrentSea>
<comments>I suggested that these results would follow from the assumption that the descriptive power of the ba</comments>
</weather>
</operationalHSE>
<productionActivity>
<lostProduction>
<volumeAndReason reasonLost="topside equipment failure-maint" uom="m3">1053.4</volumeAndReason>
<volumeAndReason reasonLost="preventive maint topside" uom="m3">1140.2</volumeAndReason>
<thirdPartyProcessing>
<installation kind="platform">Ekofisk</installation>
<oilStdTempPres uom="m3">1747.83</oilStdTempPres>
<gasStdTempPres uom="m3">1196.25</gasStdTempPres>
</thirdPartyProcessing>
</lostProduction>
<waterCleaningQuality>
<samplePoint>Sample 1</samplePoint>
<oilInWaterProduced uom="Euc">61.94</oilInWaterProduced>
<amountOfOil uom="kg">96.85</amountOfOil>
<ammonium uom="kg/m3">4.84</ammonium>
<totalOrganicCarbon uom="Euc">14.33</totalOrganicCarbon>
<phenol uom="kg/m3">27.87</phenol>
<glycol uom="kg/m3">117.24</glycol>
<phValue>8.03</phValue>
<waterTemperature uom="degC">12.37</waterTemperature>
<residualChloride uom="Euc">125.49</residualChloride>
<oxygen uom="Euc">52.8</oxygen>
<turbidity>32.4</turbidity>
<coulterCounter uom="Euc">185.06</coulterCounter>
<comment>
<dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
<remark>So far, the descriptive power of the base component is not to be considered in determining problems </remark>
</comment>
</waterCleaningQuality>
<shutdown>
<installation kind="well">String</installation>
<description>Preventive maintenance</description>
<dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
<volumetricDownTime uom="h">0</volumetricDownTime>
<lossOilStdTempPres uom="m3">780.08</lossOilStdTempPres>
<lossGasStdTempPres uom="m3">7223.75</lossGasStdTempPres>
<activity>
<dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
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<remark>For any transformation which is sufficiently diversified in application to be of any interest, the t</remark>
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<dTim>2012-03-01T00:00:00.0Z</dTim>
<area>Area A</area>
<type>Gas Alarm</type>
<reason>Faulty alarm</reason>
<comment>Nevertheless, a subset of English sentences interesting on quite independent grounds suffices to acc</comment>
</alarm>
<marineOperation>
<dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T02:00:00.0Z</dTimEnd>
<generalComment>Clearly, the appearance of parasitic gaps in domains relatively inaccessible to ordinary extraction </generalComment>
<supplyShip>Supply 1</supplyShip>
<standbyVessel>Standby 1</standbyVessel>
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<dTimStart>2012-03-01T01:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T06:00:00.0Z</dTimEnd>
<remark>So far, a case of semigrammaticalness of a different sort may remedy and, at the same time, eliminat</remark>
</supplyShipComment>
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<dTimStart>2012-03-01T06:00:00.0Z</dTimStart>
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<remark>Thus a subset of English sentences interesting on quite independent grounds is to be regarded as a d</remark>
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<dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
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<remark>It appears that the systematic use of complex symbols is to be regarded as problems of phonemic and </remark>
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<basketMovement>
<dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
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<remark>However, this assumption is not correct, since the descriptive power of the base component is rather</remark>
</basketMovement>
<basketMovement>
<dTimStart>2012-03-01T02:00:00.0Z</dTimStart>
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<remark>A consequence of the approach just outlined is that the systematic use of complex symbols delimits t</remark>
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<dTimStart>2012-03-01T06:00:00.0Z</dTimStart>
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<remark>In the discussion of resumptive pronouns following (81), the theory of syntactic features developed </remark>
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<activity>
<dTimStart>2012-03-01T09:00:00.0Z</dTimStart>
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<remark>Thus this selectionally introduced contextual feature is to be regarded as an important distinction </remark>
</activity>
</marineOperation>
<cargoShipOperation>
<vesselName>Cargo 1</vesselName>
<dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
<captain>Captain 1</captain>
<cargo>Oil</cargo>
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<oilGrossTotalStdTempPres uom="m3">6615.82</oilGrossTotalStdTempPres>
<oilNetStdTempPres uom="m3">5342.1</oilNetStdTempPres>
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<salt uom="kg/m3">116.05</salt>
<comment>
<dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
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<remark>This suggests that a case of semigrammaticalness of a different sort does not affect the structure o</remark>
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<comment>
<dTimStart>2012-03-01T01:00:00.0Z</dTimStart>
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<remark>In the discussion of resumptive pronouns following (81), a case of semigrammaticalness of a differen</remark>
</comment>
</cargoShipOperation>
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<type>production</type>
<dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
<comment>Nevertheless, most of the methodological work in modern linguistics is not quite equivalent to a des</comment>
</operationalComment>
<operationalComment>
<type>production</type>
<dTimStart>2012-03-01T06:00:00.0Z</dTimStart>
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<comment>For any transformation which is sufficiently diversified in application to be of any interest, the t</comment>
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<name>TYRIHANS</name>
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<who>MR Who</who>
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<dTimStart>2012-03-01T02:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T04:00:00.0Z</dTimEnd>
<remark>A consequence of the approach just outlined is that the speaker-hearer's linguistic intuition delimi</remark>
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<who>Mr Who2</who>
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<remark>To characterize a linguistic level L, a descriptively adequate grammar does not readily tolerate the</remark>
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<kind>oil - net</kind>
<name namingSystem="TEST17">Test product name 507</name>
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</volumeValue>
<volume status="bad calibration" uom="m3">92.12</volume>
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<port uidRef="a593b765-bad4-11e1-9607-c0f8dae91040">Port 2</port>
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<tempDiff uom="K">90.5</tempDiff>
<chokeSize uom="in/32">65.45</chokeSize>
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<mass uom="kg">79.45</mass>
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<tvp uom="bar">153.81</tvp>
<bsw uom="%">32.3</bsw>
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<densityValue>
<density uom="kg/m3">175.98</density>
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</densityValue>
<density uom="kg/m3">36.16</density>
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<densityStd uom="kg/m3">204.26</densityStd>
<concentration uom="ppm">16.59</concentration>
<molecularWeight>33.95</molecularWeight>
<weightPercent uom="%">50.19</weightPercent>
<molePercent uom="%">93.72</molePercent>
<moleAmt uom="kmol">23.97</moleAmt>
<sg uom="Euc">16.12</sg>
<hcDewpoint uom="K">237.23</hcDewpoint>
<waterDewpoint uom="K">524.96</waterDewpoint>
<wobbeIndex uom="J/m3">840.05</wobbeIndex>
<grossCalorificValueStd uom="J/m3">300.4</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">976.7</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">265.02</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">296.01</densityStabilizedCrude>
<componentContent uid="a593de6e-bad4-11e1-9499-c0f8dae91040">
<kind>nitrogen oxide gas</kind>
<referenceKind>carbon dioxide gas</referenceKind>
<gor uom="Euc">69.5</gor>
<gorMTD uom="m3/m3">93.25</gorMTD>
<waterConcMass uom="%">60.35</waterConcMass>
<waterConcVol uom="ppm">31.85</waterConcVol>
<atmosphere uom="Pa">91.8</atmosphere>
<volumeValue>
<volume status="bad calibration" uom="m3">712.13</volume>
<grossCalorificValue uom="J/m3">470.75</grossCalorificValue>
<temp uom="K">43.71</temp>
<pres uom="Pa">63.99</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">48.95</volume>
<volumeStd status="bad calibration" uom="m3">61.28</volumeStd>
<flowRate status="bad calibration" uom="m3/s">71.87</flowRate>
<temp uom="K">45.51</temp>
<pres uom="Pa">27.53</pres>
<absoluteMinPres uom="Pa">98.37</absoluteMinPres>
<portDiff uid="a593de6f-bad4-11e1-97d5-c0f8dae91040">
<port uidRef="a5940580-bad4-11e1-b600-c0f8dae91040">Port 1</port>
<presDiff uom="Pa">50.5</presDiff>
<tempDiff uom="K">96.22</tempDiff>
<chokeSize uom="in/32">11.2</chokeSize>
<chokeRelative uom="%">82.82</chokeRelative>
</portDiff>
<portDiff uid="a5940581-bad4-11e1-a2b6-c0f8dae91040">
<port uidRef="a5940582-bad4-11e1-9596-c0f8dae91040">Port 2</port>
<presDiff uom="Pa">21.23</presDiff>
<tempDiff uom="K">19.55</tempDiff>
<chokeSize uom="in/32">91.67</chokeSize>
<chokeRelative uom="%">19.6</chokeRelative>
</portDiff>
<mass uom="kg">456.12</mass>
<work uom="MJ">495.34</work>
<efficiency uom="%">75.15</efficiency>
<rvp uom="Pa">202.1</rvp>
<tvp uom="bar">805.39</tvp>
<bsw uom="%">49.24</bsw>
<bswPrevious uom="m3/m3">98.52</bswPrevious>
<densityValue>
<density uom="kg/m3">538.56</density>
<temp uom="K">61.47</temp>
<pres uom="Pa">48.61</pres>
</densityValue>
<density uom="kg/m3">256.01</density>
<densityFlowRate uom="Mg/a">20.2</densityFlowRate>
<densityStd uom="kg/m3">139.29</densityStd>
<concentration uom="ppm">17.42</concentration>
<molecularWeight>21.62</molecularWeight>
<weightPercent uom="%">80.09</weightPercent>
<molePercent uom="%">35.27</molePercent>
<moleAmt uom="kmol">33.81</moleAmt>
<sg uom="Euc">70.01</sg>
<hcDewpoint uom="K">519.78</hcDewpoint>
<waterDewpoint uom="K">453.96</waterDewpoint>
<wobbeIndex uom="J/m3">431.08</wobbeIndex>
<grossCalorificValueStd uom="J/m3">579.92</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">167.9</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">97.6</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">229.67</densityStabilizedCrude>
</componentContent>
<period>
<kind>day</kind>
<dateStart>2012-03-01</dateStart>
<dateEnd>2012-03-01</dateEnd>
<gor uom="Euc">80.87</gor>
<gorMTD uom="m3/m3">71.58</gorMTD>
<waterConcMass uom="%">10.64</waterConcMass>
<waterConcVol uom="ppm">83.83</waterConcVol>
<atmosphere uom="Pa">22.32</atmosphere>
<volumeValue>
<volume uom="m3">2765.7</volume><temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">36.48</volume>
<volumeStd status="bad calibration" uom="m3">38.47</volumeStd>
<flowRate status="bad calibration" uom="m3/s">55.99</flowRate>
<temp uom="K">73.65</temp>
<pres uom="Pa">13.61</pres>
<absoluteMinPres uom="Pa">79.98</absoluteMinPres>
<mass uom="kg">89.49</mass>
<work uom="kW.h">435.72</work>
<efficiency uom="%">98.18</efficiency>
<rvp uom="bar">461.58</rvp>
<tvp uom="bar">447.55</tvp>
<bsw uom="%">68.5</bsw>
<bswPrevious uom="m3/m3">43.97</bswPrevious>
<densityValue>
<density uom="kg/m3">780.91</density>
<temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</densityValue>
<density uom="kg/m3">678.0</density>
<densityFlowRate uom="Mg/a">166.24</densityFlowRate>
<densityStd uom="kg/m3">527.52</densityStd>
<concentration uom="ppm">50.64</concentration>
<molecularWeight>87.94</molecularWeight>
<weightPercent uom="%">34.91</weightPercent>
<molePercent uom="%">31.48</molePercent>
<moleAmt uom="kmol">47.46</moleAmt>
<sg uom="Euc">94.18</sg>
<hcDewpoint uom="K">488.91</hcDewpoint>
<waterDewpoint uom="K">840.9</waterDewpoint>
<wobbeIndex uom="J/m3">824.93</wobbeIndex>
<grossCalorificValueStd uom="J/m3">993.66</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">398.65</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">673.57</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">173.57</densityStabilizedCrude>
</period>
</product>
</flow>
<flow>
<kind>consume - fuel</kind>
<qualifier>allocated</qualifier>
<version>2012-03-01T17:00:00.0Z</version>
<versionSource>version src 454</versionSource>
<gor uom="Euc">83.64</gor>
<gorMTD uom="m3/m3">45.54</gorMTD>
<waterConcMass uom="%">34.27</waterConcMass>
<waterConcVol uom="ppm">30.89</waterConcVol>
<atmosphere uom="Pa">15.07</atmosphere>
<volumeValue>
<volume status="sensor failure" uom="m3">850.38</volume>
<grossCalorificValue uom="J/m3">882.59</grossCalorificValue>
<temp uom="K">10.19</temp>
<pres uom="Pa">85.11</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">10.84</volume>
<volumeStd status="bad calibration" uom="m3">89.23</volumeStd>
<flowRate status="bad calibration" uom="m3/s">62.14</flowRate>
<temp uom="K">12.66</temp>
<pres uom="Pa">25.63</pres>
<absoluteMinPres uom="Pa">31.24</absoluteMinPres>
<portDiff uid="a5942c8f-bad4-11e1-b412-c0f8dae91040">
<port uidRef="a5942c90-bad4-11e1-836f-c0f8dae91040">Port 1</port>
<presDiff uom="Pa">75.65</presDiff>
<tempDiff uom="K">31.06</tempDiff>
<chokeSize uom="in/32">35.58</chokeSize>
<chokeRelative uom="%">40.81</chokeRelative>
</portDiff>
<portDiff uid="a5942c91-bad4-11e1-9523-c0f8dae91040">
<port uidRef="a5942c92-bad4-11e1-a7de-c0f8dae91040">Port 2</port>
<presDiff uom="Pa">98.78</presDiff>
<tempDiff uom="K">43.86</tempDiff>
<chokeSize uom="in/32">38.01</chokeSize>
<chokeRelative uom="%">35.99</chokeRelative>
</portDiff>
<mass uom="kg">288.8</mass>
<work uom="MJ">21.58</work>
<efficiency uom="%">87.73</efficiency>
<rvp uom="Pa">654.07</rvp>
<tvp uom="bar">679.85</tvp>
<bsw uom="%">53.44</bsw>
<bswPrevious uom="m3/m3">84.51</bswPrevious>
<densityValue>
<density uom="kg/m3">244.39</density>
<temp uom="K">93.72</temp>
<pres uom="Pa">50.81</pres>
</densityValue>
<density uom="kg/m3">137.61</density>
<densityFlowRate uom="Mg/a">464.38</densityFlowRate>
<densityStd uom="kg/m3">42.16</densityStd>
<concentration uom="ppm">51.32</concentration>
<molecularWeight>54.77</molecularWeight>
<weightPercent uom="%">72.21</weightPercent>
<molePercent uom="%">13.21</molePercent>
<moleAmt uom="kmol">25.08</moleAmt>
<sg uom="Euc">64.37</sg>
<hcDewpoint uom="K">658.1</hcDewpoint>
<waterDewpoint uom="K">180.48</waterDewpoint>
<wobbeIndex uom="J/m3">902.14</wobbeIndex>
<grossCalorificValueStd uom="J/m3">976.38</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">733.45</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">542.71</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">616.46</densityStabilizedCrude>
<product>
<kind>diesel</kind>
<name namingSystem="TEST2">Test product name 445</name>
<splitFactor>0.56</splitFactor>
<gor uom="Euc">87.93</gor>
<gorMTD uom="m3/m3">96.91</gorMTD>
<waterConcMass uom="%">34.59</waterConcMass>
<waterConcVol uom="ppm">58.99</waterConcVol>
<atmosphere uom="Pa">34.97</atmosphere>
<volumeValue>
<volume status="range limit" uom="m3">874.32</volume>
<grossCalorificValue uom="J/m3">28.2</grossCalorificValue>
<temp uom="K">78.68</temp>
<pres uom="Pa">95.72</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">27.39</volume>
<volumeStd status="bad calibration" uom="m3">98.79</volumeStd>
<flowRate status="bad calibration" uom="m3/s">18.51</flowRate>
<temp uom="K">30.35</temp>
<pres uom="Pa">32.06</pres>
<absoluteMinPres uom="Pa">39.12</absoluteMinPres>
<portDiff uid="a5942c93-bad4-11e1-99d0-c0f8dae91040">
<port uidRef="a5942c94-bad4-11e1-9bc6-c0f8dae91040">Port 1</port>
<presDiff uom="Pa">42.88</presDiff>
<tempDiff uom="K">95.96</tempDiff>
<chokeSize uom="in/32">95.96</chokeSize>
<chokeRelative uom="%">92.33</chokeRelative>
</portDiff>
<portDiff uid="a5942c95-bad4-11e1-952d-c0f8dae91040">
<port uidRef="a5942c96-bad4-11e1-8807-c0f8dae91040">Port 2</port>
<presDiff uom="Pa">37.99</presDiff>
<tempDiff uom="K">32.1</tempDiff>
<chokeSize uom="in/32">84.84</chokeSize>
<chokeRelative uom="%">28.26</chokeRelative>
</portDiff>
<mass uom="kg">84.07</mass>
<work uom="MJ">59.04</work>
<efficiency uom="%">59.05</efficiency>
<rvp uom="Pa">31.33</rvp>
<tvp uom="bar">923.69</tvp>
<bsw uom="%">77.68</bsw>
<bswPrevious uom="m3/m3">11.7</bswPrevious>
<densityValue>
<density uom="kg/m3">138.04</density>
<temp uom="K">67.82</temp>
<pres uom="Pa">71.84</pres>
</densityValue>
<density uom="kg/m3">571.01</density>
<densityFlowRate uom="Mg/a">141.97</densityFlowRate>
<densityStd uom="kg/m3">117.99</densityStd>
<concentration uom="ppm">86.56</concentration>
<molecularWeight>50.68</molecularWeight>
<weightPercent uom="%">43.99</weightPercent>
<molePercent uom="%">41.45</molePercent>
<moleAmt uom="kmol">98.87</moleAmt>
<sg uom="Euc">23.8</sg>
<hcDewpoint uom="K">854.28</hcDewpoint>
<waterDewpoint uom="K">12.84</waterDewpoint>
<wobbeIndex uom="J/m3">594.48</wobbeIndex>
<grossCalorificValueStd uom="J/m3">349.99</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">484.17</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">136.17</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">96.22</densityStabilizedCrude>
<componentContent uid="a594539e-bad4-11e1-94f3-c0f8dae91040">
<kind>normal butane</kind>
<referenceKind>gas</referenceKind>
<gor uom="Euc">49.31</gor>
<gorMTD uom="m3/m3">98.68</gorMTD>
<waterConcMass uom="%">37.24</waterConcMass>
<waterConcVol uom="ppm">84.94</waterConcVol>
<atmosphere uom="Pa">84.18</atmosphere>
<volumeValue>
<volume status="sensor failure" uom="m3">73.31</volume>
<grossCalorificValue uom="J/m3">857.4</grossCalorificValue>
<temp uom="K">71.98</temp>
<pres uom="Pa">49.32</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">99.1</volume>
<volumeStd status="bad calibration" uom="m3">13.42</volumeStd>
<flowRate status="bad calibration" uom="m3/s">73.44</flowRate>
<temp uom="K">42.77</temp>
<pres uom="Pa">53.17</pres>
<absoluteMinPres uom="Pa">57.29</absoluteMinPres>
<portDiff uid="a594539f-bad4-11e1-b23d-c0f8dae91040">
<port uidRef="a59453a0-bad4-11e1-a37c-c0f8dae91040">Port 1</port>
<presDiff uom="Pa">26.17</presDiff>
<tempDiff uom="K">84.48</tempDiff>
<chokeSize uom="in/32">27.72</chokeSize>
<chokeRelative uom="%">20.24</chokeRelative>
</portDiff>
<portDiff uid="a59453a1-bad4-11e1-b446-c0f8dae91040">
<port uidRef="a59453a2-bad4-11e1-aa56-c0f8dae91040">Port 2</port>
<presDiff uom="Pa">52.42</presDiff>
<tempDiff uom="K">27.49</tempDiff>
<chokeSize uom="in/32">24.29</chokeSize>
<chokeRelative uom="%">52.0</chokeRelative>
</portDiff>
<mass uom="kg">215.92</mass>
<work uom="MJ">30.67</work>
<efficiency uom="%">78.11</efficiency>
<rvp uom="Pa">324.12</rvp>
<tvp uom="bar">976.29</tvp>
<bsw uom="%">47.4</bsw>
<bswPrevious uom="m3/m3">67.76</bswPrevious>
<densityValue>
<density uom="kg/m3">662.26</density>
<temp uom="K">16.91</temp>
<pres uom="Pa">38.29</pres>
</densityValue>
<density uom="kg/m3">368.3</density>
<densityFlowRate uom="Mg/a">213.54</densityFlowRate>
<densityStd uom="kg/m3">653.79</densityStd>
<concentration uom="ppm">81.69</concentration>
<molecularWeight>29.26</molecularWeight>
<weightPercent uom="%">33.19</weightPercent>
<molePercent uom="%">99.23</molePercent>
<moleAmt uom="kmol">47.94</moleAmt>
<sg uom="Euc">79.73</sg>
<hcDewpoint uom="K">10.03</hcDewpoint>
<waterDewpoint uom="K">997.84</waterDewpoint>
<wobbeIndex uom="J/m3">30.11</wobbeIndex>
<grossCalorificValueStd uom="J/m3">352.47</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">847.36</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">511.07</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">866.05</densityStabilizedCrude>
</componentContent>
<period>
<kind>day</kind>
<dateStart>2012-03-01</dateStart>
<dateEnd>2012-03-01</dateEnd>
<gor uom="Euc">11.58</gor>
<gorMTD uom="m3/m3">18.4</gorMTD>
<waterConcMass uom="%">36.78</waterConcMass>
<waterConcVol uom="ppm">50.57</waterConcVol>
<atmosphere uom="Pa">47.47</atmosphere>
<volumeValue>
<volume uom="L">59.52</volume>
<temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</volumeValue><volume status="bad calibration" uom="m3">95.3</volume>
<volumeStd status="bad calibration" uom="m3">86.7</volumeStd>
<flowRate status="bad calibration" uom="m3/s">11.13</flowRate>
<temp uom="K">65.44</temp>
<pres uom="Pa">69.91</pres>
<absoluteMinPres uom="Pa">81.24</absoluteMinPres>
<work uom="J">175.15</work>
<efficiency uom="%">44.51</efficiency>
<rvp uom="atm">390.35</rvp>
<tvp uom="bar">364.31</tvp>
<bsw uom="%">12.64</bsw>
<bswPrevious uom="m3/m3">11.22</bswPrevious>
<density uom="kg/m3">456.65</density>
<densityFlowRate uom="Mg/a">458.25</densityFlowRate>
<densityStd uom="kg/m3">234.65</densityStd>
<concentration uom="ppm">93.17</concentration>
<molecularWeight>61.41</molecularWeight>
<weightPercent uom="%">93.71</weightPercent>
<molePercent uom="%">80.96</molePercent>
<moleAmt uom="kmol">34.98</moleAmt>
<sg uom="Euc">15.91</sg>
<hcDewpoint uom="K">154.45</hcDewpoint>
<waterDewpoint uom="K">573.72</waterDewpoint>
<wobbeIndex uom="J/m3">790.72</wobbeIndex>
<grossCalorificValueStd uom="J/m3">854.35</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">999.73</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">590.89</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">739.43</densityStabilizedCrude>
</period>
</product>
</flow>
</facility><facility>
<name kind="compressor" namingSystem="STATOIL" uidRef="NaN">TYRIHANS compressor</name>
<facilityParent1 kind="block valve" namingSystem="String" uidRef="x">String</facilityParent1>
<facilityParent2 kind="block valve" namingSystem="String" uidRef="x">String</facilityParent2>
<facilityAlias namingSystem="String">String</facilityAlias>
<facilityAlias namingSystem="String">String</facilityAlias>
<contextFacility kind="block valve" namingSystem="String" uidRef="x">String</contextFacility>
<contextFacility kind="block valve" namingSystem="String" uidRef="x">String</contextFacility>
<flow>
<kind>production</kind>
<qualifier>metered - fiscal</qualifier>
<version>2012-03-01T03:00:00.0Z</version>
<versionSource>version src 974</versionSource>
<gor uom="Euc">35.52</gor>
<gorMTD uom="m3/m3">15.11</gorMTD>
<waterConcMass uom="%">86.31</waterConcMass>
<waterConcVol uom="ppm">42.86</waterConcVol>
<atmosphere uom="Pa">49.52</atmosphere>
<volumeValue>
<volume status="device failure" uom="m3">773.87</volume>
<grossCalorificValue uom="J/m3">694.44</grossCalorificValue>
<temp uom="K">83.41</temp>
<pres uom="Pa">36.72</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">64.39</volume>
<volumeStd status="bad calibration" uom="m3">43.65</volumeStd>
<flowRate status="bad calibration" uom="m3/s">46.86</flowRate>
<temp uom="K">80.75</temp>
<pres uom="Pa">10.23</pres>
<absoluteMinPres uom="Pa">67.92</absoluteMinPres>
<portDiff uid="a5947ab0-bad4-11e1-9447-c0f8dae91040">
<port uidRef="a5947ab1-bad4-11e1-9b4b-c0f8dae91040">Port 1</port>
<presDiff uom="Pa">15.61</presDiff>
<tempDiff uom="K">30.46</tempDiff>
<chokeSize uom="in/32">38.4</chokeSize>
<chokeRelative uom="%">93.09</chokeRelative>
</portDiff>
<portDiff uid="a5947ab2-bad4-11e1-be41-c0f8dae91040">
<port uidRef="a5947ab3-bad4-11e1-86d2-c0f8dae91040">Port 2</port>
<presDiff uom="Pa">32.92</presDiff>
<tempDiff uom="K">91.82</tempDiff>
<chokeSize uom="in/32">57.24</chokeSize>
<chokeRelative uom="%">20.26</chokeRelative>
</portDiff>
<mass uom="kg">213.07</mass>
<work uom="MJ">863.46</work>
<efficiency uom="%">95.65</efficiency>
<rvp uom="Pa">388.96</rvp>
<tvp uom="bar">383.49</tvp>
<bsw uom="%">81.25</bsw>
<bswPrevious uom="m3/m3">20.74</bswPrevious>
<densityValue>
<density uom="kg/m3">42.98</density>
<temp uom="K">82.61</temp>
<pres uom="Pa">22.5</pres>
</densityValue>
<density uom="kg/m3">388.11</density>
<densityFlowRate uom="Mg/a">292.45</densityFlowRate>
<densityStd uom="kg/m3">321.98</densityStd>
<concentration uom="ppm">74.09</concentration>
<molecularWeight>34.21</molecularWeight>
<weightPercent uom="%">58.88</weightPercent>
<molePercent uom="%">72.41</molePercent>
<moleAmt uom="kmol">25.41</moleAmt>
<sg uom="Euc">10.96</sg>
<hcDewpoint uom="K">187.27</hcDewpoint>
<waterDewpoint uom="K">559.4</waterDewpoint>
<wobbeIndex uom="J/m3">211.0</wobbeIndex>
<grossCalorificValueStd uom="J/m3">362.87</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">85.82</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">659.87</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">806.3</densityStabilizedCrude>
<product>
<kind>oil - net</kind>
<name namingSystem="TEST722">Test product name 264</name>
<splitFactor>0.68</splitFactor>
<gor uom="Euc">22.25</gor>
<gorMTD uom="m3/m3">33.7</gorMTD>
<waterConcMass uom="%">74.49</waterConcMass>
<waterConcVol uom="ppm">75.39</waterConcVol>
<atmosphere uom="Pa">44.42</atmosphere>
<volumeValue>
<volume status="range limit" uom="m3">221.51</volume>
<grossCalorificValue uom="J/m3">981.59</grossCalorificValue>
<temp uom="K">96.24</temp>
<pres uom="Pa">57.34</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">11.95</volume>
<volumeStd status="bad calibration" uom="m3">39.14</volumeStd>
<flowRate status="bad calibration" uom="m3/s">89.55</flowRate>
<temp uom="K">21.21</temp>
<pres uom="Pa">91.15</pres>
<absoluteMinPres uom="Pa">35.26</absoluteMinPres>
<portDiff uid="a594a1c0-bad4-11e1-86bc-c0f8dae91040">
<port uidRef="a594a1c1-bad4-11e1-8aa4-c0f8dae91040">Port 1</port>
<presDiff uom="Pa">95.52</presDiff>
<tempDiff uom="K">80.2</tempDiff>
<chokeSize uom="in/32">70.18</chokeSize>
<chokeRelative uom="%">96.53</chokeRelative>
</portDiff>
<portDiff uid="a594a1c2-bad4-11e1-95a9-c0f8dae91040">
<port uidRef="a594a1c3-bad4-11e1-8626-c0f8dae91040">Port 2</port>
<presDiff uom="Pa">26.71</presDiff>
<tempDiff uom="K">60.83</tempDiff>
<chokeSize uom="in/32">99.35</chokeSize>
<chokeRelative uom="%">10.64</chokeRelative>
</portDiff>
<mass uom="kg">110.74</mass>
<work uom="MJ">133.41</work>
<efficiency uom="%">57.52</efficiency>
<rvp uom="Pa">53.23</rvp>
<tvp uom="bar">67.55</tvp>
<bsw uom="%">86.16</bsw>
<bswPrevious uom="m3/m3">94.84</bswPrevious>
<densityValue>
<density uom="kg/m3">522.77</density>
<temp uom="K">76.29</temp>
<pres uom="Pa">44.64</pres>
</densityValue>
<density uom="kg/m3">207.66</density>
<densityFlowRate uom="Mg/a">566.19</densityFlowRate>
<densityStd uom="kg/m3">699.91</densityStd>
<concentration uom="ppm">47.12</concentration>
<molecularWeight>15.04</molecularWeight>
<weightPercent uom="%">41.72</weightPercent>
<molePercent uom="%">17.4</molePercent>
<moleAmt uom="kmol">96.63</moleAmt>
<sg uom="Euc">66.52</sg>
<hcDewpoint uom="K">41.98</hcDewpoint>
<waterDewpoint uom="K">336.3</waterDewpoint>
<wobbeIndex uom="J/m3">454.09</wobbeIndex>
<grossCalorificValueStd uom="J/m3">582.25</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">471.59</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">201.79</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">539.47</densityStabilizedCrude>
<componentContent uid="a594c8cf-bad4-11e1-8f50-c0f8dae91040">
<kind>C3-</kind>
<referenceKind>carbon monoxide gas</referenceKind>
<gor uom="Euc">30.35</gor>
<gorMTD uom="m3/m3">51.28</gorMTD>
<waterConcMass uom="%">64.57</waterConcMass>
<waterConcVol uom="ppm">81.28</waterConcVol>
<atmosphere uom="Pa">66.69</atmosphere>
<volumeValue>
<volume status="sensor failure" uom="m3">959.72</volume>
<grossCalorificValue uom="J/m3">11.76</grossCalorificValue>
<temp uom="K">62.44</temp>
<pres uom="Pa">79.62</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">34.82</volume>
<volumeStd status="bad calibration" uom="m3">74.11</volumeStd>
<flowRate status="bad calibration" uom="m3/s">30.08</flowRate>
<temp uom="K">52.87</temp>
<pres uom="Pa">12.73</pres>
<absoluteMinPres uom="Pa">70.57</absoluteMinPres>
<portDiff uid="a594c8d0-bad4-11e1-8cab-c0f8dae91040">
<port uidRef="a594c8d1-bad4-11e1-908b-c0f8dae91040">Port 1</port>
<presDiff uom="Pa">25.53</presDiff>
<tempDiff uom="K">24.35</tempDiff>
<chokeSize uom="in/32">11.2</chokeSize>
<chokeRelative uom="%">23.02</chokeRelative>
</portDiff>
<portDiff uid="a594c8d2-bad4-11e1-9d48-c0f8dae91040">
<port uidRef="a594c8d3-bad4-11e1-b4df-c0f8dae91040">Port 2</port>
<presDiff uom="Pa">94.62</presDiff>
<tempDiff uom="K">57.81</tempDiff>
<chokeSize uom="in/32">95.45</chokeSize>
<chokeRelative uom="%">14.48</chokeRelative>
</portDiff>
<mass uom="kg">217.15</mass>
<work uom="MJ">544.83</work>
<efficiency uom="%">80.0</efficiency>
<rvp uom="Pa">822.33</rvp>
<tvp uom="bar">110.72</tvp>
<bsw uom="%">72.94</bsw>
<bswPrevious uom="m3/m3">38.75</bswPrevious>
<densityValue>
<density uom="kg/m3">61.45</density>
<temp uom="K">42.07</temp>
<pres uom="Pa">37.24</pres>
</densityValue>
<density uom="kg/m3">400.29</density>
<densityFlowRate uom="Mg/a">386.72</densityFlowRate>
<densityStd uom="kg/m3">557.07</densityStd>
<concentration uom="ppm">54.38</concentration>
<molecularWeight>93.53</molecularWeight>
<weightPercent uom="%">14.75</weightPercent>
<molePercent uom="%">67.24</molePercent>
<moleAmt uom="kmol">55.84</moleAmt>
<sg uom="Euc">16.33</sg>
<hcDewpoint uom="K">455.97</hcDewpoint>
<waterDewpoint uom="K">503.48</waterDewpoint>
<wobbeIndex uom="J/m3">248.34</wobbeIndex>
<grossCalorificValueStd uom="J/m3">288.75</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">210.29</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">51.57</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">88.47</densityStabilizedCrude>
</componentContent>
<period>
<kind>day</kind>
<dateStart>2012-03-01</dateStart>
<dateEnd>2012-03-01</dateEnd>
<gor uom="Euc">56.93</gor>
<gorMTD uom="m3/m3">70.62</gorMTD>
<waterConcMass uom="%">70.7</waterConcMass>
<waterConcVol uom="ppm">83.9</waterConcVol>
<atmosphere uom="Pa">92.59</atmosphere>
<volumeValue>
<volume uom="m3">1853.88</volume><temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">67.54</volume>
<volumeStd status="bad calibration" uom="m3">55.21</volumeStd>
<flowRate status="bad calibration" uom="m3/s">22.02</flowRate>
<temp uom="K">66.91</temp>
<pres uom="Pa">27.85</pres>
<absoluteMinPres uom="Pa">58.11</absoluteMinPres>
<mass uom="kg">285.7</mass>
<work uom="kW.h">249.53</work>
<efficiency uom="%">19.28</efficiency>
<rvp uom="kPa">81.84</rvp>
<tvp uom="bar">252.87</tvp>
<bsw uom="%">36.37</bsw>
<bswPrevious uom="m3/m3">35.58</bswPrevious>
<densityValue>
<density uom="kg/m3">786.28</density>
<temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</densityValue>
<density uom="kg/m3">154.18</density>
<densityFlowRate uom="Mg/a">478.7</densityFlowRate>
<densityStd uom="kg/m3">677.04</densityStd>
<concentration uom="ppm">44.83</concentration>
<molecularWeight>70.05</molecularWeight>
<weightPercent uom="%">17.38</weightPercent>
<molePercent uom="%">51.33</molePercent>
<moleAmt uom="kmol">96.78</moleAmt>
<sg uom="Euc">78.21</sg>
<hcDewpoint uom="K">93.29</hcDewpoint>
<waterDewpoint uom="K">234.47</waterDewpoint>
<wobbeIndex uom="J/m3">116.04</wobbeIndex>
<grossCalorificValueStd uom="J/m3">450.28</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">839.37</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">504.28</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">993.31</densityStabilizedCrude>
</period>
</product>
</flow>
<flow>
<kind>injection</kind>
<qualifier>metered - fiscal</qualifier>
<version>2012-03-01T19:00:00.0Z</version>
<versionSource>version src 794</versionSource>
<gor uom="Euc">46.49</gor>
<gorMTD uom="m3/m3">92.08</gorMTD>
<waterConcMass uom="%">20.43</waterConcMass>
<waterConcVol uom="ppm">32.44</waterConcVol>
<atmosphere uom="Pa">21.72</atmosphere>
<volumeValue>
<volume status="range limit" uom="m3">948.52</volume>
<grossCalorificValue uom="J/m3">627.63</grossCalorificValue>
<temp uom="K">30.09</temp>
<pres uom="Pa">20.19</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">96.76</volume>
<volumeStd status="bad calibration" uom="m3">53.67</volumeStd>
<flowRate status="bad calibration" uom="m3/s">44.96</flowRate>
<temp uom="K">17.72</temp>
<pres uom="Pa">46.28</pres>
<absoluteMinPres uom="Pa">64.07</absoluteMinPres>
<portDiff uid="a594efde-bad4-11e1-86cc-c0f8dae91040">
<port uidRef="a594efdf-bad4-11e1-91c2-c0f8dae91040">Port 1</port>
<presDiff uom="Pa">96.58</presDiff>
<tempDiff uom="K">79.73</tempDiff>
<chokeSize uom="in/32">20.6</chokeSize>
<chokeRelative uom="%">31.66</chokeRelative>
</portDiff>
<portDiff uid="a594efe0-bad4-11e1-bc0c-c0f8dae91040">
<port uidRef="a594efe1-bad4-11e1-8572-c0f8dae91040">Port 2</port>
<presDiff uom="Pa">40.89</presDiff>
<tempDiff uom="K">23.78</tempDiff>
<chokeSize uom="in/32">34.33</chokeSize>
<chokeRelative uom="%">28.36</chokeRelative>
</portDiff>
<mass uom="kg">187.26</mass>
<work uom="MJ">405.07</work>
<efficiency uom="%">28.9</efficiency>
<rvp uom="Pa">177.55</rvp>
<tvp uom="bar">274.51</tvp>
<bsw uom="%">92.53</bsw>
<bswPrevious uom="m3/m3">83.52</bswPrevious>
<densityValue>
<density uom="kg/m3">559.56</density>
<temp uom="K">56.64</temp>
<pres uom="Pa">83.99</pres>
</densityValue>
<density uom="kg/m3">193.63</density>
<densityFlowRate uom="Mg/a">81.49</densityFlowRate>
<densityStd uom="kg/m3">248.0</densityStd>
<concentration uom="ppm">78.23</concentration>
<molecularWeight>33.74</molecularWeight>
<weightPercent uom="%">16.32</weightPercent>
<molePercent uom="%">75.53</molePercent>
<moleAmt uom="kmol">58.38</moleAmt>
<sg uom="Euc">52.82</sg>
<hcDewpoint uom="K">568.81</hcDewpoint>
<waterDewpoint uom="K">289.99</waterDewpoint>
<wobbeIndex uom="J/m3">761.31</wobbeIndex>
<grossCalorificValueStd uom="J/m3">77.95</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">857.14</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">641.83</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">877.1</densityStabilizedCrude>
<product>
<kind>oil - net</kind>
<name namingSystem="TEST461">Test product name 963</name>
<splitFactor>0.88</splitFactor>
<gor uom="Euc">85.02</gor>
<gorMTD uom="m3/m3">65.93</gorMTD>
<waterConcMass uom="%">52.36</waterConcMass>
<waterConcVol uom="ppm">57.95</waterConcVol>
<atmosphere uom="Pa">64.13</atmosphere>
<volumeValue>
<volume status="range limit" uom="m3">146.14</volume>
<grossCalorificValue uom="J/m3">391.77</grossCalorificValue>
<temp uom="K">51.18</temp>
<pres uom="Pa">65.31</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">62.37</volume>
<volumeStd status="bad calibration" uom="m3">34.97</volumeStd>
<flowRate status="bad calibration" uom="m3/s">61.68</flowRate>
<temp uom="K">31.15</temp>
<pres uom="Pa">58.89</pres>
<absoluteMinPres uom="Pa">68.44</absoluteMinPres>
<portDiff uid="a59516f0-bad4-11e1-b4d5-c0f8dae91040">
<port uidRef="a59516f1-bad4-11e1-8ab5-c0f8dae91040">Port 1</port>
<presDiff uom="Pa">87.12</presDiff>
<tempDiff uom="K">12.2</tempDiff>
<chokeSize uom="in/32">46.71</chokeSize>
<chokeRelative uom="%">78.09</chokeRelative>
</portDiff>
<portDiff uid="a59516f2-bad4-11e1-9b39-c0f8dae91040">
<port uidRef="a59516f3-bad4-11e1-8b42-c0f8dae91040">Port 2</port>
<presDiff uom="Pa">75.38</presDiff>
<tempDiff uom="K">48.86</tempDiff>
<chokeSize uom="in/32">24.95</chokeSize>
<chokeRelative uom="%">60.77</chokeRelative>
</portDiff>
<mass uom="kg">288.91</mass>
<work uom="MJ">14.37</work>
<efficiency uom="%">60.8</efficiency>
<rvp uom="Pa">805.05</rvp>
<tvp uom="bar">499.5</tvp>
<bsw uom="%">85.77</bsw>
<bswPrevious uom="m3/m3">55.49</bswPrevious>
<densityValue>
<density uom="kg/m3">494.4</density>
<temp uom="K">70.43</temp>
<pres uom="Pa">59.66</pres>
</densityValue>
<density uom="kg/m3">663.33</density>
<densityFlowRate uom="Mg/a">170.49</densityFlowRate>
<densityStd uom="kg/m3">251.24</densityStd>
<concentration uom="ppm">48.7</concentration>
<molecularWeight>71.03</molecularWeight>
<weightPercent uom="%">47.07</weightPercent>
<molePercent uom="%">47.44</molePercent>
<moleAmt uom="kmol">26.12</moleAmt>
<sg uom="Euc">70.4</sg>
<hcDewpoint uom="K">177.28</hcDewpoint>
<waterDewpoint uom="K">775.28</waterDewpoint>
<wobbeIndex uom="J/m3">556.7</wobbeIndex>
<grossCalorificValueStd uom="J/m3">585.16</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">549.22</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">124.52</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">540.43</densityStabilizedCrude>
<componentContent uid="a59516f4-bad4-11e1-90c0-c0f8dae91040">
<kind>aqueous</kind>
<referenceKind>neopentane</referenceKind>
<gor uom="Euc">53.44</gor>
<gorMTD uom="m3/m3">47.79</gorMTD>
<waterConcMass uom="%">96.69</waterConcMass>
<waterConcVol uom="ppm">79.13</waterConcVol>
<atmosphere uom="Pa">63.3</atmosphere>
<volumeValue>
<volume status="sensor failure" uom="m3">57.17</volume>
<grossCalorificValue uom="J/m3">264.73</grossCalorificValue>
<temp uom="K">11.05</temp>
<pres uom="Pa">84.52</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">79.24</volume>
<volumeStd status="bad calibration" uom="m3">90.56</volumeStd>
<flowRate status="bad calibration" uom="m3/s">42.01</flowRate>
<temp uom="K">27.55</temp>
<pres uom="Pa">47.34</pres>
<absoluteMinPres uom="Pa">75.07</absoluteMinPres>
<portDiff uid="a59516f5-bad4-11e1-9971-c0f8dae91040">
<port uidRef="a5953e00-bad4-11e1-9080-c0f8dae91040">Port 1</port>
<presDiff uom="Pa">65.18</presDiff>
<tempDiff uom="K">92.33</tempDiff>
<chokeSize uom="in/32">49.71</chokeSize>
<chokeRelative uom="%">16.17</chokeRelative>
</portDiff>
<portDiff uid="a5953e01-bad4-11e1-ac32-c0f8dae91040">
<port uidRef="a5953e02-bad4-11e1-93d8-c0f8dae91040">Port 2</port>
<presDiff uom="Pa">89.36</presDiff>
<tempDiff uom="K">46.85</tempDiff>
<chokeSize uom="in/32">89.93</chokeSize>
<chokeRelative uom="%">43.86</chokeRelative>
</portDiff>
<mass uom="kg">742.25</mass>
<work uom="MJ">656.82</work>
<efficiency uom="%">27.55</efficiency>
<rvp uom="Pa">66.57</rvp>
<tvp uom="bar">543.79</tvp>
<bsw uom="%">40.6</bsw>
<bswPrevious uom="m3/m3">15.09</bswPrevious>
<densityValue>
<density uom="kg/m3">665.18</density>
<temp uom="K">37.11</temp>
<pres uom="Pa">38.39</pres>
</densityValue>
<density uom="kg/m3">358.27</density>
<densityFlowRate uom="Mg/a">525.76</densityFlowRate>
<densityStd uom="kg/m3">615.11</densityStd>
<concentration uom="ppm">29.01</concentration>
<molecularWeight>35.13</molecularWeight>
<weightPercent uom="%">70.55</weightPercent>
<molePercent uom="%">64.15</molePercent>
<moleAmt uom="kmol">81.69</moleAmt>
<sg uom="Euc">20.94</sg>
<hcDewpoint uom="K">162.95</hcDewpoint>
<waterDewpoint uom="K">585.5</waterDewpoint>
<wobbeIndex uom="J/m3">371.93</wobbeIndex>
<grossCalorificValueStd uom="J/m3">582.81</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">641.21</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">932.05</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">172.79</densityStabilizedCrude>
</componentContent>
<period>
<kind>day</kind>
<dateStart>2012-03-01</dateStart>
<dateEnd>2012-03-01</dateEnd>
<gor uom="Euc">19.78</gor>
<gorMTD uom="m3/m3">37.1</gorMTD>
<waterConcMass uom="%">65.31</waterConcMass>
<waterConcVol uom="ppm">25.1</waterConcVol>
<atmosphere uom="Pa">87.71</atmosphere>
<volumeValue>
<volume uom="m3">1840.26</volume><temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">46.21</volume>
<volumeStd status="bad calibration" uom="m3">91.31</volumeStd>
<flowRate status="bad calibration" uom="m3/s">83.51</flowRate>
<temp uom="K">94.43</temp>
<pres uom="Pa">49.54</pres>
<absoluteMinPres uom="Pa">95.99</absoluteMinPres>
<mass uom="kg">227.68</mass>
<work uom="J">673.21</work>
<efficiency uom="%">95.47</efficiency>
<rvp uom="atm">913.47</rvp>
<tvp uom="bar">66.26</tvp>
<bsw uom="%">11.43</bsw>
<bswPrevious uom="m3/m3">17.01</bswPrevious>
<densityValue>
<density uom="kg/m3">729.18</density>
<temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</densityValue>
<density uom="kg/m3">22.79</density>
<densityFlowRate uom="Mg/a">552.38</densityFlowRate>
<densityStd uom="kg/m3">648.4</densityStd>
<concentration uom="ppm">18.68</concentration>
<molecularWeight>70.94</molecularWeight>
<weightPercent uom="%">75.94</weightPercent>
<molePercent uom="%">95.19</molePercent>
<moleAmt uom="kmol">39.95</moleAmt>
<sg uom="Euc">66.04</sg>
<hcDewpoint uom="K">510.83</hcDewpoint>
<waterDewpoint uom="K">758.31</waterDewpoint>
<wobbeIndex uom="J/m3">22.63</wobbeIndex>
<grossCalorificValueStd uom="J/m3">439.77</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">161.28</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">103.29</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">600.54</densityStabilizedCrude>
</period>
</product>
</flow>
</facility>
</object></objects>
\ No newline at end of file