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David Price
b23088b5 1 parent 020baddb

Update of DPR2 TRYM and ASGARD and MPRG+MPRP ASGARD test files from EPIM

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Showing 22 changed files with 500 additions and 311 deletions
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1 -<?xml version="1.0" encoding="UTF-8"?>
2 -<objects xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance"
3 - xmlns="http://www.epim.no/schemas/mprml/1" version="1.0(MPRML)">
4 - <documentInfo>
5 - <DocumentName namingSystem="EC">TRYM February 2012</DocumentName>
6 - <DocumentAlias namingSystem="EC">TRYM Copex Report</DocumentAlias>
7 - <DocumentDate>2012-03-05T00:00:00.0Z</DocumentDate>
8 - <documentClass namingSystem="EC">Dong E&amp;P Norge AS</documentClass>
9 - <documentClass namingSystem="EC">DPR 2.0</documentClass>
10 - <documentClass namingSystem="ERH">dpr2</documentClass>
11 - <FileCreationInformation>
12 -
13 - <FileCreationDate>2012-03-15T00:00:00.0Z</FileCreationDate>
14 -
15 - <SoftwareName>Energy Components</SoftwareName>
16 - <FileCreator>Dong E&amp;P Norge AS</FileCreator>
17 - <Comment>NA</Comment>
18 - </FileCreationInformation>
19 - <Owner>Dong E&amp;P Norge AS</Owner>
20 - </documentInfo>
21 - <context xsi:type="obj_report">
22 - <kind>DPR 2.0</kind>
23 -
24 - <title>TRYM</title>
25 - <date>2012-02-01</date>
26 - <dateEnd>2012-02-01</dateEnd>
27 - <month>2012-02</month>
28 - <year>2012</year>
29 - <reportVersion>1.1</reportVersion>
30 - <reportStatus>final</reportStatus>
31 - <installation kind="field" namingSystem="NPD" uidRef="18081500">TRYM</installation>
32 - <operator>
33 - <name>Dong E&amp;P Norge AS</name>
34 - <role>Operating company</role>
35 - </operator>
36 - </context>
37 - <object xsi:type="obj_productVolume">
38 - <name>TRYM</name>
39 - <installation kind="field" namingSystem="NPD" uidRef="18081500">TRYM</installation>
40 - <facility>
41 - <name kind="field" namingSystem="NPD" uidRef="18081500">TRYM</name>
42 - <facilityParent1 namingSystem="String" uidRef="x" kind="block valve">String</facilityParent1>
43 - <facilityParent2 namingSystem="String" uidRef="x" kind="block valve">String</facilityParent2>
44 - <facilityAlias namingSystem="String">String</facilityAlias>
45 - <facilityAlias namingSystem="String">String</facilityAlias>
46 - <contextFacility namingSystem="String" uidRef="x" kind="block valve">String</contextFacility>
47 - <contextFacility namingSystem="String" uidRef="x" kind="block valve">String</contextFacility>
48 -
49 -
50 - <downtimeReason uid="a5c6a140-8ae8-11e2-b65a-78acc03c3a5e">
51 - <who>MR Who</who>
52 - <role>Platform manager</role>
53 - <dTimStart>2012-02-01T02:00:00.0Z</dTimStart>
54 - <dTimEnd>2012-02-29T04:00:00.0Z</dTimEnd>
55 - <remark>If the position of the trace in (99c) were only relatively inaccessible to movement, a descriptively</remark>
56 - </downtimeReason>
57 - <downtimeReason uid="a5c6a141-8ae8-11e2-abf3-78acc03c3a5e">
58 - <who>Mr Who2</who>
59 - <role>Platform manager 2</role>
60 - <dTimStart>2012-02-01T06:00:00.0Z</dTimStart>
61 - <dTimEnd>2012-02-29T14:00:00.0Z</dTimEnd>
62 - <remark>Let us continue to suppose that the fundamental error of regarding functional notions as categorial </remark>
63 - </downtimeReason>
64 - <flow uid="TRY_SALEABLE_PRODUCTION">
65 - <name>Trym saleable volumes</name>
66 - <kind>production</kind>
67 - <qualifier>saleable</qualifier>
68 - <version>2012-02-01T02:00:00.0Z</version>
69 - <versionSource>version src 255</versionSource>
70 - <gor uom="Euc">48.25</gor>
71 - <gorMTD uom="m3/m3">33.03</gorMTD>
72 - <waterConcMass uom="%">89.99</waterConcMass>
73 - <waterConcVol uom="ppm">72.85</waterConcVol>
74 - <atmosphere uom="Pa">13.71</atmosphere>
75 - <volumeValue>
76 - <volume status="comm failure" uom="m3">134.26</volume>
77 - <grossCalorificValue uom="J/m3">862.8</grossCalorificValue>
78 - <temp uom="K">88.52</temp>
79 - <pres uom="Pa">46.23</pres>
80 - </volumeValue>
81 - <volume status="bad calibration" uom="m3">11.89</volume>
82 - <volumeStd status="bad calibration" uom="m3">15.4</volumeStd>
83 - <flowRate status="bad calibration" uom="m3/s">77.85</flowRate>
84 - <temp uom="K">22.68</temp>
85 - <pres uom="Pa">88.49</pres>
86 - <absoluteMinPres uom="Pa">67.96</absoluteMinPres>
87 - <portDiff uid="a5c6a142-8ae8-11e2-a16c-78acc03c3a5e">
88 - <port uidRef="a5c6a143-8ae8-11e2-9fb7-78acc03c3a5e">Port 1</port>
89 - <presDiff uom="Pa">64.99</presDiff>
90 - <tempDiff uom="K">52.23</tempDiff>
91 - <chokeSize uom="in/32">78.15</chokeSize>
92 - <chokeRelative uom="%">18.46</chokeRelative>
93 - </portDiff>
94 - <portDiff uid="a5c6a144-8ae8-11e2-9abb-78acc03c3a5e">
95 - <port uidRef="a5c6a145-8ae8-11e2-9ed8-78acc03c3a5e">Port 2</port>
96 - <presDiff uom="Pa">79.65</presDiff>
97 - <tempDiff uom="K">31.38</tempDiff>
98 - <chokeSize uom="in/32">61.63</chokeSize>
99 - <chokeRelative uom="%">76.93</chokeRelative>
100 - </portDiff>
101 - <mass uom="kg">741.86</mass>
102 - <work uom="MJ">900.63</work>
103 - <efficiency uom="%">44.64</efficiency>
104 - <rvp uom="Pa">473.2</rvp>
105 - <tvp uom="bar">672.31</tvp>
106 - <bsw uom="%">56.58</bsw>
107 - <bswPrevious uom="m3/m3">34.61</bswPrevious>
108 - <densityValue>
109 - <density uom="kg/m3">37.41</density>
110 - <temp uom="K">53.03</temp>
111 - <pres uom="Pa">79.19</pres>
112 - </densityValue>
113 - <density uom="kg/m3">412.02</density>
114 - <densityFlowRate uom="Mg/a">328.63</densityFlowRate>
115 - <densityStd uom="kg/m3">667.03</densityStd>
116 - <concentration uom="ppm">62.47</concentration>
117 - <molecularWeight>40.34</molecularWeight>
118 - <weightPercent uom="%">38.31</weightPercent>
119 - <molePercent uom="%">53.15</molePercent>
120 - <moleAmt uom="kmol">80.5</moleAmt>
121 - <sg uom="Euc">78.32</sg>
122 - <hcDewpoint uom="K">539.52</hcDewpoint>
123 - <waterDewpoint uom="K">647.14</waterDewpoint>
124 - <wobbeIndex uom="J/m3">703.54</wobbeIndex>
125 - <grossCalorificValueStd uom="J/m3">999.35</grossCalorificValueStd>
126 - <rvpStabilizedCrude uom="Pa">218.7</rvpStabilizedCrude>
127 - <bswStabilizedCrude uom="Euc">473.17</bswStabilizedCrude>
128 - <densityStabilizedCrude uom="kg/m3">90.92</densityStabilizedCrude>
129 - <product>
130 - <kind>oil - net</kind>
131 - <name namingSystem="TEST411">Test product name 187</name>
132 - <splitFactor>0.11</splitFactor>
133 - <gor uom="Euc">82.69</gor>
134 - <gorMTD uom="m3/m3">63.83</gorMTD>
135 - <waterConcMass uom="%">18.93</waterConcMass>
136 - <waterConcVol uom="ppm">63.88</waterConcVol>
137 - <atmosphere uom="Pa">25.5</atmosphere>
138 - <volumeValue>
139 - <volume status="device failure" uom="m3">505.2</volume>
140 - <grossCalorificValue uom="J/m3">619.52</grossCalorificValue>
141 - <temp uom="K">92.1</temp>
142 - <pres uom="Pa">13.05</pres>
143 - </volumeValue>
144 - <volume status="bad calibration" uom="m3">86.05</volume>
145 - <volumeStd status="bad calibration" uom="m3">50.84</volumeStd>
146 - <flowRate status="bad calibration" uom="m3/s">81.66</flowRate>
147 - <temp uom="K">12.39</temp>
148 - <pres uom="Pa">23.36</pres>
149 - <absoluteMinPres uom="Pa">85.53</absoluteMinPres>
150 - <portDiff uid="a5c6a146-8ae8-11e2-a53c-78acc03c3a5e">
151 - <port uidRef="a5c6a147-8ae8-11e2-9d3d-78acc03c3a5e">Port 1</port>
152 - <presDiff uom="Pa">68.18</presDiff>
153 - <tempDiff uom="K">26.62</tempDiff>
154 - <chokeSize uom="in/32">54.61</chokeSize>
155 - <chokeRelative uom="%">53.42</chokeRelative>
156 - </portDiff>
157 - <portDiff uid="a5c6a148-8ae8-11e2-a4d1-78acc03c3a5e">
158 - <port uidRef="a5c6a149-8ae8-11e2-aab3-78acc03c3a5e">Port 2</port>
159 - <presDiff uom="Pa">33.9</presDiff>
160 - <tempDiff uom="K">83.62</tempDiff>
161 - <chokeSize uom="in/32">50.9</chokeSize>
162 - <chokeRelative uom="%">90.59</chokeRelative>
163 - </portDiff>
164 - <mass uom="kg">413.44</mass>
165 - <work uom="MJ">634.56</work>
166 - <efficiency uom="%">76.94</efficiency>
167 - <rvp uom="Pa">659.3</rvp>
168 - <tvp uom="bar">800.3</tvp>
169 - <bsw uom="%">16.46</bsw>
170 - <bswPrevious uom="m3/m3">42.44</bswPrevious>
171 - <densityValue>
172 - <density uom="kg/m3">440.19</density>
173 - <temp uom="K">50.6</temp>
174 - <pres uom="Pa">45.21</pres>
175 - </densityValue>
176 - <density uom="kg/m3">100.46</density>
177 - <densityFlowRate uom="Mg/a">662.64</densityFlowRate>
178 - <densityStd uom="kg/m3">265.49</densityStd>
179 - <concentration uom="ppm">61.62</concentration>
180 - <molecularWeight>59.0</molecularWeight>
181 - <weightPercent uom="%">63.08</weightPercent>
182 - <molePercent uom="%">92.99</molePercent>
183 - <moleAmt uom="kmol">49.5</moleAmt>
184 - <sg uom="Euc">55.69</sg>
185 - <hcDewpoint uom="K">164.87</hcDewpoint>
186 - <waterDewpoint uom="K">865.69</waterDewpoint>
187 - <wobbeIndex uom="J/m3">378.96</wobbeIndex>
188 - <grossCalorificValueStd uom="J/m3">123.58</grossCalorificValueStd>
189 - <rvpStabilizedCrude uom="Pa">57.65</rvpStabilizedCrude>
190 - <bswStabilizedCrude uom="Euc">230.87</bswStabilizedCrude>
191 - <densityStabilizedCrude uom="kg/m3">87.87</densityStabilizedCrude>
192 - <componentContent uid="a5c6a14a-8ae8-11e2-b107-78acc03c3a5e">
193 - <kind>condensate</kind>
194 - <referenceKind>oil</referenceKind>
195 - <gor uom="Euc">60.51</gor>
196 - <gorMTD uom="m3/m3">18.36</gorMTD>
197 - <waterConcMass uom="%">40.9</waterConcMass>
198 - <waterConcVol uom="ppm">86.33</waterConcVol>
199 - <atmosphere uom="Pa">88.88</atmosphere>
200 - <volumeValue>
201 - <volume status="bad calibration" uom="m3">312.64</volume>
202 - <grossCalorificValue uom="J/m3">17.24</grossCalorificValue>
203 - <temp uom="K">71.58</temp>
204 - <pres uom="Pa">84.36</pres>
205 - </volumeValue>
206 - <volume status="bad calibration" uom="m3">60.48</volume>
207 - <volumeStd status="bad calibration" uom="m3">15.54</volumeStd>
208 - <flowRate status="bad calibration" uom="m3/s">52.91</flowRate>
209 - <temp uom="K">52.17</temp>
210 - <pres uom="Pa">62.3</pres>
211 - <absoluteMinPres uom="Pa">12.62</absoluteMinPres>
212 - <portDiff uid="a5c91240-8ae8-11e2-ae52-78acc03c3a5e">
213 - <port uidRef="a5c91241-8ae8-11e2-8794-78acc03c3a5e">Port 1</port>
214 - <presDiff uom="Pa">51.38</presDiff>
215 - <tempDiff uom="K">61.09</tempDiff>
216 - <chokeSize uom="in/32">42.97</chokeSize>
217 - <chokeRelative uom="%">52.18</chokeRelative>
218 - </portDiff>
219 - <portDiff uid="a5c91242-8ae8-11e2-9489-78acc03c3a5e">
220 - <port uidRef="a5c91243-8ae8-11e2-8437-78acc03c3a5e">Port 2</port>
221 - <presDiff uom="Pa">84.67</presDiff>
222 - <tempDiff uom="K">40.75</tempDiff>
223 - <chokeSize uom="in/32">76.06</chokeSize>
224 - <chokeRelative uom="%">88.08</chokeRelative>
225 - </portDiff>
226 - <mass uom="kg">467.73</mass>
227 - <work uom="MJ">840.23</work>
228 - <efficiency uom="%">33.86</efficiency>
229 - <rvp uom="Pa">991.18</rvp>
230 - <tvp uom="bar">755.73</tvp>
231 - <bsw uom="%">78.2</bsw>
232 - <bswPrevious uom="m3/m3">91.4</bswPrevious>
233 - <densityValue>
234 - <density uom="kg/m3">241.87</density>
235 - <temp uom="K">33.79</temp>
236 - <pres uom="Pa">32.72</pres>
237 - </densityValue>
238 - <density uom="kg/m3">576.9</density>
239 - <densityFlowRate uom="Mg/a">105.41</densityFlowRate>
240 - <densityStd uom="kg/m3">55.76</densityStd>
241 - <concentration uom="ppm">20.34</concentration>
242 - <molecularWeight>16.71</molecularWeight>
243 - <weightPercent uom="%">57.89</weightPercent>
244 - <molePercent uom="%">38.67</molePercent>
245 - <moleAmt uom="kmol">67.02</moleAmt>
246 - <sg uom="Euc">21.22</sg>
247 - <hcDewpoint uom="K">715.1</hcDewpoint>
248 - <waterDewpoint uom="K">100.26</waterDewpoint>
249 - <wobbeIndex uom="J/m3">289.8</wobbeIndex>
250 - <grossCalorificValueStd uom="J/m3">363.38</grossCalorificValueStd>
251 - <rvpStabilizedCrude uom="Pa">407.89</rvpStabilizedCrude>
252 - <bswStabilizedCrude uom="Euc">704.82</bswStabilizedCrude>
253 - <densityStabilizedCrude uom="kg/m3">257.23</densityStabilizedCrude>
254 - </componentContent>
255 - <period>
256 - <kind>month</kind>
257 - <dateStart>2012-02-01</dateStart>
258 - <dateEnd>2012-02-29</dateEnd>
259 - <gor uom="Euc">55.03</gor>
260 - <gorMTD uom="m3/m3">71.04</gorMTD>
261 - <waterConcMass uom="%">67.41</waterConcMass>
262 - <waterConcVol uom="ppm">31.52</waterConcVol>
263 - <atmosphere uom="Pa">81.95</atmosphere>
264 - <volumeValue>
265 -
266 - <volume uom="m3">615.87</volume><temp uom="degC">15</temp>
267 - <pres uom="atm">1</pres>
268 - </volumeValue>
269 - <volume status="bad calibration" uom="m3">31.27</volume>
270 - <volumeStd status="bad calibration" uom="m3">43.03</volumeStd>
271 - <flowRate status="bad calibration" uom="m3/s">57.45</flowRate>
272 - <temp uom="K">41.0</temp>
273 - <pres uom="Pa">48.88</pres>
274 - <absoluteMinPres uom="Pa">55.29</absoluteMinPres>
275 -
276 - <mass uom="kg">224.73</mass>
277 - <work uom="kW.h">491.2</work>
278 - <efficiency uom="%">15.12</efficiency>
279 - <rvp uom="kPa">900.96</rvp>
280 - <tvp uom="bar">827.62</tvp>
281 - <bsw uom="%">58.3</bsw>
282 - <bswPrevious uom="m3/m3">51.07</bswPrevious>
283 - <densityValue>
284 -
285 - <density uom="kg/m3">786.94</density>
286 - <temp uom="degC">15</temp>
287 - <pres uom="atm">1</pres>
288 - </densityValue>
289 - <density uom="kg/m3">334.31</density>
290 - <densityFlowRate uom="Mg/a">290.09</densityFlowRate>
291 - <densityStd uom="kg/m3">412.8</densityStd>
292 - <concentration uom="ppm">53.22</concentration>
293 - <molecularWeight>50.39</molecularWeight>
294 - <weightPercent uom="%">12.68</weightPercent>
295 - <molePercent uom="%">97.96</molePercent>
296 - <moleAmt uom="kmol">68.2</moleAmt>
297 - <sg uom="Euc">18.88</sg>
298 - <hcDewpoint uom="K">339.08</hcDewpoint>
299 - <waterDewpoint uom="K">722.12</waterDewpoint>
300 - <wobbeIndex uom="J/m3">108.08</wobbeIndex>
301 - <grossCalorificValueStd uom="J/m3">230.02</grossCalorificValueStd>
302 - <rvpStabilizedCrude uom="Pa">322.68</rvpStabilizedCrude>
303 - <bswStabilizedCrude uom="Euc">84.89</bswStabilizedCrude>
304 - <densityStabilizedCrude uom="kg/m3">124.95</densityStabilizedCrude>
305 - </period>
306 -
307 - </product>
308 - </flow>
309 - </facility>
310 - </object>
311 -</objects>
...\ No newline at end of file ...\ No newline at end of file
1 +<?xml version="1.0" encoding="UTF-8"?>
2 +<objects xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance"
3 + xmlns="http://www.epim.no/schemas/mprml/1" version="1.0(MPRML)">
4 + <documentInfo>
5 + <DocumentName namingSystem="EC">ÅSGARD January 2012</DocumentName>
6 + <DocumentAlias namingSystem="EC">ÅSGARD Copex Report</DocumentAlias>
7 + <DocumentDate>2012-02-05T00:00:00.0Z</DocumentDate>
8 + <documentClass namingSystem="EC">Statoil Petroleum AS</documentClass>
9 + <documentClass namingSystem="EC">Copex</documentClass>
10 + <documentClass namingSystem="ERH">mprg</documentClass>
11 + <FileCreationInformation>
12 + <FileCreationDate>2012-02-05T00:00:00.0Z</FileCreationDate>
13 +
14 + <SoftwareName>Energy Components</SoftwareName>
15 + <FileCreator>Statoil Petroleum AS</FileCreator>
16 + <Comment>NA</Comment>
17 + </FileCreationInformation>
18 + <Owner>Statoil Petroleum AS</Owner>
19 + </documentInfo>
20 + <context xsi:type="obj_report">
21 + <kind>Copex</kind>
22 +
23 + <title>ÅSGARD</title>
24 + <date>2012-01-01</date>
25 + <dateEnd>2012-01-31</dateEnd>
26 + <month>2012-01</month>
27 + <year>2012</year>
28 + <reportVersion>1.1</reportVersion>
29 + <reportStatus>preliminary</reportStatus>
30 + <installation kind="field" namingSystem="NPD" uidRef="43765">ÅSGARD</installation>
31 + <operator>
32 + <name>Statoil Petroleum AS</name>
33 + <role>Operating company</role>
34 + </operator>
35 + </context>
36 + <object xsi:type="obj_productVolume">
37 + <name>KRISTIN</name>
38 + <installation kind="field" namingSystem="NPD" uidRef="1854729">KRISTIN</installation>
39 + <facility>
40 + <name kind="field" namingSystem="NPD" uidRef="1854729">KRISTIN</name>
41 +
42 + <flow uid="KRISTIN_SALEABLE_PRODUCTION">
43 + <name>Kristin saleable volumes</name>
44 + <kind>production</kind>
45 + <qualifier>saleable</qualifier>
46 + <product>
47 + <kind>oil - net</kind>
48 + <period>
49 + <kind>month</kind>
50 + <dateStart>2012-01-01</dateStart>
51 + <dateEnd>2012-01-31</dateEnd>
52 + <volumeValue>
53 +
54 + <volume uom="m3">101952.5</volume><temp uom="degC">15</temp>
55 + <pres uom="atm">1</pres>
56 + </volumeValue>
57 +
58 + <mass uom="kg">84401518.61</mass>
59 + <densityValue>
60 +
61 + <density uom="kg/m3">774.07</density>
62 + <temp uom="degC">15</temp>
63 + <pres uom="atm">1</pres>
64 + </densityValue>
65 + </period>
66 +
67 + </product>
68 + </flow>
69 +
70 +
71 +
72 + <flow uid="KRISTIN_ALLOCATED_PRODUCTION">
73 + <name>Kristin allocated volumes</name>
74 + <kind>production</kind>
75 + <qualifier>allocated</qualifier>
76 + <product>
77 + <kind>oil - net</kind>
78 + <period>
79 + <kind>month</kind>
80 + <dateStart>2012-01-01</dateStart>
81 + <dateEnd>2012-01-31</dateEnd>
82 + <volumeValue>
83 +
84 + <volume uom="m3">268450.47</volume><temp uom="degC">15</temp>
85 + <pres uom="atm">1</pres>
86 + </volumeValue>
87 +
88 + <mass uom="kg">32174682.0</mass>
89 + <densityValue>
90 +
91 + <density uom="kg/m3">757.27</density>
92 + <temp uom="degC">15</temp>
93 + <pres uom="atm">1</pres>
94 + </densityValue>
95 + </period>
96 +
97 + </product><product>
98 + <kind>gas</kind>
99 + <period>
100 + <kind>month</kind>
101 + <dateStart>2012-01-01</dateStart>
102 + <dateEnd>2012-01-31</dateEnd>
103 + <volumeValue>
104 +
105 + <volume uom="m3">201065.05</volume><temp uom="degC">15</temp>
106 + <pres uom="atm">1</pres>
107 + </volumeValue>
108 +
109 + <mass uom="kg">35541182.56</mass>
110 + <densityValue>
111 + <density uom="kg/m3">0.7</density>
112 +
113 + <temp uom="degC">15</temp>
114 + <pres uom="atm">1</pres>
115 + </densityValue>
116 + </period>
117 +
118 + </product><product>
119 + <kind>condensate - net</kind>
120 + <period>
121 + <kind>month</kind>
122 + <dateStart>2012-01-01</dateStart>
123 + <dateEnd>2012-01-31</dateEnd>
124 + <volumeValue>
125 +
126 + <volume uom="m3">255563.75</volume><temp uom="degC">15</temp>
127 + <pres uom="atm">1</pres>
128 + </volumeValue>
129 +
130 + <mass uom="kg">34560058.23</mass>
131 + <densityValue>
132 +
133 + <density uom="kg/m3">776.07</density>
134 + <temp uom="degC">15</temp>
135 + <pres uom="atm">1</pres>
136 + </densityValue>
137 + </period>
138 +
139 + </product><product>
140 + <kind>water</kind>
141 + <period>
142 + <kind>month</kind>
143 + <dateStart>2012-01-01</dateStart>
144 + <dateEnd>2012-01-31</dateEnd>
145 + <volumeValue>
146 +
147 + <volume uom="m3">269306.2</volume><temp uom="degC">15</temp>
148 + <pres uom="atm">1</pres>
149 + </volumeValue>
150 +
151 +
152 +
153 + </period>
154 +
155 + </product>
156 + </flow>
157 +
158 +
159 +
160 + <flow uid="KRISTIN_GAS_INJECTION_TOT">
161 + <name>Kristin injected gas</name>
162 + <kind>injection</kind>
163 + <qualifier>allocated</qualifier>
164 + <product>
165 + <kind>gas</kind>
166 + <period>
167 + <kind>month</kind>
168 + <dateStart>2012-01-01</dateStart>
169 + <dateEnd>2012-01-31</dateEnd>
170 + <volumeValue>
171 +
172 + <volume uom="m3">229560.79</volume><temp uom="degC">15</temp>
173 + <pres uom="atm">1</pres>
174 + </volumeValue>
175 +
176 + <mass uom="kg">39685285.41</mass>
177 + <densityValue>
178 + <density uom="kg/m3">0.93</density>
179 +
180 + <temp uom="degC">15</temp>
181 + <pres uom="atm">1</pres>
182 + </densityValue>
183 + </period>
184 +
185 + </product>
186 + </flow>
187 +
188 +
189 +
190 +
191 +
192 +
193 +
194 + <flow uid="KRISTIN_CHEMICAL_INJECTION">
195 + <name>Kristin injection of chemicals</name>
196 +
197 + <kind>injection</kind>
198 + <qualifier>measured</qualifier>
199 + <product>
200 + <kind>chemical</kind>
201 + <name>Wax inhibitor</name>
202 + <period>
203 + <kind>month</kind>
204 + <dateStart>2012-01-01</dateStart>
205 + <dateEnd>2012-01-31</dateEnd>
206 + <volumeValue>
207 +
208 + <volume uom="L">2292.35</volume>
209 + <temp uom="degC">15</temp>
210 + <pres uom="atm">1</pres>
211 + </volumeValue>
212 +
213 + </period>
214 + </product><product>
215 + <kind>chemical</kind>
216 + <name>Scale inhibitor</name>
217 + <period>
218 + <kind>month</kind>
219 + <dateStart>2012-01-01</dateStart>
220 + <dateEnd>2012-01-31</dateEnd>
221 + <volumeValue>
222 +
223 + <volume uom="L">1353.31</volume>
224 + <temp uom="degC">15</temp>
225 + <pres uom="atm">1</pres>
226 + </volumeValue>
227 +
228 + </period>
229 + </product><product>
230 + <kind>chemical</kind>
231 + <name>Methanol</name>
232 + <period>
233 + <kind>month</kind>
234 + <dateStart>2012-01-01</dateStart>
235 + <dateEnd>2012-01-31</dateEnd>
236 + <volumeValue>
237 +
238 + <volume uom="L">1558.79</volume>
239 + <temp uom="degC">15</temp>
240 + <pres uom="atm">1</pres>
241 + </volumeValue>
242 +
243 + </period>
244 + </product>
245 + </flow><flow uid="KRISTIN_FISCAL_FIELD_VOLUMES">
246 + <name>Kristin measured total volumes</name>
247 + <kind>production</kind>
248 + <qualifier>metered - fiscal</qualifier>
249 + <product>
250 + <kind>oil - net</kind>
251 + <period>
252 + <kind>month</kind>
253 + <dateStart>2012-01-01</dateStart>
254 + <dateEnd>2012-01-31</dateEnd>
255 + <volumeValue>
256 +
257 + <volume uom="m3">127491.0</volume><temp uom="degC">15</temp>
258 + <pres uom="atm">1</pres>
259 + </volumeValue>
260 +
261 + <mass uom="kg">74071145.34</mass>
262 + <densityValue>
263 +
264 + <density uom="kg/m3">768.05</density>
265 + <temp uom="degC">15</temp>
266 + <pres uom="atm">1</pres>
267 + </densityValue>
268 + </period>
269 +
270 + </product><product>
271 + <kind>gas</kind>
272 + <period>
273 + <kind>month</kind>
274 + <dateStart>2012-01-01</dateStart>
275 + <dateEnd>2012-01-31</dateEnd>
276 + <volumeValue>
277 +
278 + <volume uom="m3">108383.31</volume><temp uom="degC">15</temp>
279 + <pres uom="atm">1</pres>
280 + </volumeValue>
281 +
282 + <mass uom="kg">70079142.44</mass>
283 + <densityValue>
284 + <density uom="kg/m3">0.76</density>
285 +
286 + <temp uom="degC">15</temp>
287 + <pres uom="atm">1</pres>
288 + </densityValue>
289 + </period>
290 +
291 + </product><product>
292 + <kind>water</kind>
293 + <period>
294 + <kind>month</kind>
295 + <dateStart>2012-01-01</dateStart>
296 + <dateEnd>2012-01-31</dateEnd>
297 + <volumeValue>
298 +
299 + <volume uom="m3">106565.38</volume><temp uom="degC">15</temp>
300 + <pres uom="atm">1</pres>
301 + </volumeValue>
302 +
303 +
304 +
305 + </period>
306 +
307 + </product>
308 + </flow>
309 +
310 +
311 +
312 +
313 + <flow uid="KRISTIN_ALLOCATED_INVENTORY_TOT">
314 + <name>Kristin total allocated inventory</name>
315 + <kind>inventory</kind>
316 + <qualifier>allocated</qualifier>
317 + <product>
318 + <kind>oil - net</kind>
319 + <period>
320 + <kind>month</kind>
321 + <dateStart>2012-01-01</dateStart>
322 + <dateEnd>2012-01-31</dateEnd>
323 + <volumeValue>
324 + <volume uom="m3">101471.53</volume>
325 + <temp uom="degC">15</temp>
326 + <pres uom="atm">1</pres>
327 + </volumeValue>
328 +
329 + <mass uom="kg">86757279.07</mass>
330 +
331 + <densityValue>
332 + <density uom="kg/m3">762.24</density>
333 + <temp uom="degC">15</temp>
334 + <pres uom="atm">1</pres>
335 + </densityValue>
336 + <balanceSet>
337 + <kind>closing balance</kind>
338 + <balanceDetail>
339 + <owner>PETORO</owner>
340 + <volumeValue>
341 + <volume uom="m3">31466.321453</volume>
342 + <temp uom="degC">15</temp>
343 + <pres uom="atm">1</pres>
344 + </volumeValue>
345 + <mass uom="kg">26903432.2396</mass>
346 + </balanceDetail><balanceDetail>
347 + <owner>TOTAL</owner>
348 + <volumeValue>
349 + <volume uom="m3">4119.744118</volume>
350 + <temp uom="degC">15</temp>
351 + <pres uom="atm">1</pres>
352 + </volumeValue>
353 + <mass uom="kg">3522345.53024</mass>
354 + </balanceDetail><balanceDetail>
355 + <owner>STATOIL</owner>
356 + <volumeValue>
357 + <volume uom="m3">54327.857162</volume>
358 + <temp uom="degC">15</temp>
359 + <pres uom="atm">1</pres>
360 + </volumeValue>
361 + <mass uom="kg">46449847.2141</mass>
362 + </balanceDetail><balanceDetail>
363 + <owner>EXXONMOBIL PROD</owner>
364 + <volumeValue>
365 + <volume uom="m3">2496.199638</volume>
366 + <temp uom="degC">15</temp>
367 + <pres uom="atm">1</pres>
368 + </volumeValue>
369 + <mass uom="kg">2134229.06512</mass>
370 + </balanceDetail><balanceDetail>
371 + <owner>ENI NORGE</owner>
372 + <volumeValue>
373 + <volume uom="m3">9061.407629</volume>
374 + <temp uom="degC">15</temp>
375 + <pres uom="atm">1</pres>
376 + </volumeValue>
377 + <mass uom="kg">7747425.02095</mass>
378 + </balanceDetail>
379 + </balanceSet>
380 + </period>
381 +
382 + </product>
383 + </flow>
384 +
385 +
386 +
387 +
388 +
389 + <flow uid="KRISTIN_ALLOCATED_GAS_SALES">
390 + <name>Kristin allocated gas sales</name>
391 + <kind>sale</kind>
392 + <qualifier>allocated</qualifier>
393 + <product>
394 + <kind>gas - dry</kind>
395 + <period>
396 + <kind>month</kind>
397 + <dateStart>2012-01-01</dateStart>
398 + <dateEnd>2012-01-31</dateEnd>
399 +
400 + <balanceSet>
401 + <kind>transaction</kind>
402 +
403 + <volumeValue>
404 + <volume uom="m3">775.4</volume>
405 + <temp uom="degC">0</temp>
406 + <pres uom="atm">1</pres>
407 + </volumeValue>
408 +
409 + <work uom="MJ">20800.38</work>
410 + <balanceDetail>
411 + <owner>STATOIL</owner>
412 + <seller>STATOIL</seller>
413 + <salesAdministrator>STATOIL</salesAdministrator>
414 + <buyer>EXXONMOBIL GAS DE</buyer>
415 + <volumeValue>
416 + <volume uom="m3">512.67</volume>
417 + <temp uom="degC">0</temp>
418 + <pres uom="atm">1</pres>
419 + </volumeValue>
420 +
421 + <work uom="MJ">23118.03</work>
422 + </balanceDetail><balanceDetail>
423 + <owner>STATOIL</owner>
424 + <seller>STATOIL</seller>
425 + <salesAdministrator>STATOIL</salesAdministrator>
426 + <buyer>DONG DK</buyer>
427 + <volumeValue>
428 + <volume uom="m3">262.73</volume>
429 + <temp uom="degC">0</temp>
430 + <pres uom="atm">1</pres>
431 + </volumeValue>
432 +
433 + <work uom="MJ">27169.3</work>
434 + </balanceDetail>
435 + </balanceSet><balanceSet>
436 + <kind>transaction</kind>
437 +
438 + <volumeValue>
439 + <volume uom="m3">975.26</volume>
440 + <temp uom="degC">0</temp>
441 + <pres uom="atm">1</pres>
442 + </volumeValue>
443 +
444 + <work uom="MJ">43368.46</work>
445 + <balanceDetail>
446 + <owner>STATOIL</owner>
447 + <seller>STATOIL</seller>
448 + <salesAdministrator>STATOIL</salesAdministrator>
449 + <buyer>NATURGAS VEST</buyer>
450 + <volumeValue>
451 + <volume uom="m3">843.19</volume>
452 + <temp uom="degC">0</temp>
453 + <pres uom="atm">1</pres>
454 + </volumeValue>
455 +
456 + <work uom="MJ">27742.43</work>
457 + </balanceDetail><balanceDetail>
458 + <owner>STATOIL</owner>
459 + <seller>STATOIL</seller>
460 + <salesAdministrator>STATOIL</salesAdministrator>
461 + <buyer>EXXONMOBIL GAS DE</buyer>
462 + <volumeValue>
463 + <volume uom="m3">132.07</volume>
464 + <temp uom="degC">0</temp>
465 + <pres uom="atm">1</pres>
466 + </volumeValue>
467 +
468 + <work uom="MJ">8762.27</work>
469 + </balanceDetail>
470 + </balanceSet><balanceSet>
471 + <kind>transaction</kind>
472 +
473 + <volumeValue>
474 + <volume uom="m3">936.38</volume>
475 + <temp uom="degC">0</temp>
476 + <pres uom="atm">1</pres>
477 + </volumeValue>
478 +
479 + <work uom="MJ">17147.72</work>
480 + <balanceDetail>
481 + <owner>STATOIL</owner>
482 + <seller>STATOIL</seller>
483 + <salesAdministrator>STATOIL</salesAdministrator>
484 + <buyer>NATURGAS VEST</buyer>
485 + <volumeValue>
486 + <volume uom="m3">936.38</volume>
487 + <temp uom="degC">0</temp>
488 + <pres uom="atm">1</pres>
489 + </volumeValue>
490 +
491 + <work uom="MJ">27534.9</work>
492 + </balanceDetail>
493 + </balanceSet>
494 + </period>
495 + </product>
496 + </flow>
497 +
498 + </facility>
499 + </object>
500 +</objects>
...\ No newline at end of file ...\ No newline at end of file