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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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<?xml version="1.0" encoding="UTF-8"?>
<objects xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance"
xmlns="http://www.epim.no/schemas/mprml/1" version="1.0(MPRML)">
<documentInfo>
<DocumentName namingSystem="EC">TRYM February 2012</DocumentName>
<DocumentAlias namingSystem="EC">TRYM Copex Report</DocumentAlias>
<DocumentDate>2012-03-05T00:00:00.0Z</DocumentDate>
<documentClass namingSystem="EC">Dong E&amp;P Norge AS</documentClass>
<documentClass namingSystem="EC">DPR 2.0</documentClass>
<documentClass namingSystem="ERH">dpr2</documentClass>
<FileCreationInformation>
<FileCreationDate>2012-03-15T00:00:00.0Z</FileCreationDate>
<SoftwareName>Energy Components</SoftwareName>
<FileCreator>Dong E&amp;P Norge AS</FileCreator>
<Comment>NA</Comment>
</FileCreationInformation>
<Owner>Dong E&amp;P Norge AS</Owner>
</documentInfo>
<context xsi:type="obj_report">
<kind>DPR 2.0</kind>
<title>TRYM</title>
<date>2012-02-01</date>
<dateEnd>2012-02-01</dateEnd>
<month>2012-02</month>
<year>2012</year>
<reportVersion>1.1</reportVersion>
<reportStatus>final</reportStatus>
<installation kind="field" namingSystem="NPD" uidRef="18081500">TRYM</installation>
<operator>
<name>Dong E&amp;P Norge AS</name>
<role>Operating company</role>
</operator>
</context>
<object xsi:type="obj_productVolume">
<name>TRYM</name>
<installation kind="field" namingSystem="NPD" uidRef="18081500">TRYM</installation>
<facility>
<name kind="field" namingSystem="NPD" uidRef="18081500">TRYM</name>
<facilityParent1 namingSystem="String" uidRef="x" kind="block valve">String</facilityParent1>
<facilityParent2 namingSystem="String" uidRef="x" kind="block valve">String</facilityParent2>
<facilityAlias namingSystem="String">String</facilityAlias>
<facilityAlias namingSystem="String">String</facilityAlias>
<contextFacility namingSystem="String" uidRef="x" kind="block valve">String</contextFacility>
<contextFacility namingSystem="String" uidRef="x" kind="block valve">String</contextFacility>
<downtimeReason uid="a5c6a140-8ae8-11e2-b65a-78acc03c3a5e">
<who>MR Who</who>
<role>Platform manager</role>
<dTimStart>2012-02-01T02:00:00.0Z</dTimStart>
<dTimEnd>2012-02-29T04:00:00.0Z</dTimEnd>
<remark>If the position of the trace in (99c) were only relatively inaccessible to movement, a descriptively</remark>
</downtimeReason>
<downtimeReason uid="a5c6a141-8ae8-11e2-abf3-78acc03c3a5e">
<who>Mr Who2</who>
<role>Platform manager 2</role>
<dTimStart>2012-02-01T06:00:00.0Z</dTimStart>
<dTimEnd>2012-02-29T14:00:00.0Z</dTimEnd>
<remark>Let us continue to suppose that the fundamental error of regarding functional notions as categorial </remark>
</downtimeReason>
<flow uid="TRY_SALEABLE_PRODUCTION">
<name>Trym saleable volumes</name>
<kind>production</kind>
<qualifier>saleable</qualifier>
<version>2012-02-01T02:00:00.0Z</version>
<versionSource>version src 255</versionSource>
<gor uom="Euc">48.25</gor>
<gorMTD uom="m3/m3">33.03</gorMTD>
<waterConcMass uom="%">89.99</waterConcMass>
<waterConcVol uom="ppm">72.85</waterConcVol>
<atmosphere uom="Pa">13.71</atmosphere>
<volumeValue>
<volume status="comm failure" uom="m3">134.26</volume>
<grossCalorificValue uom="J/m3">862.8</grossCalorificValue>
<temp uom="K">88.52</temp>
<pres uom="Pa">46.23</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">11.89</volume>
<volumeStd status="bad calibration" uom="m3">15.4</volumeStd>
<flowRate status="bad calibration" uom="m3/s">77.85</flowRate>
<temp uom="K">22.68</temp>
<pres uom="Pa">88.49</pres>
<absoluteMinPres uom="Pa">67.96</absoluteMinPres>
<portDiff uid="a5c6a142-8ae8-11e2-a16c-78acc03c3a5e">
<port uidRef="a5c6a143-8ae8-11e2-9fb7-78acc03c3a5e">Port 1</port>
<presDiff uom="Pa">64.99</presDiff>
<tempDiff uom="K">52.23</tempDiff>
<chokeSize uom="in/32">78.15</chokeSize>
<chokeRelative uom="%">18.46</chokeRelative>
</portDiff>
<portDiff uid="a5c6a144-8ae8-11e2-9abb-78acc03c3a5e">
<port uidRef="a5c6a145-8ae8-11e2-9ed8-78acc03c3a5e">Port 2</port>
<presDiff uom="Pa">79.65</presDiff>
<tempDiff uom="K">31.38</tempDiff>
<chokeSize uom="in/32">61.63</chokeSize>
<chokeRelative uom="%">76.93</chokeRelative>
</portDiff>
<mass uom="kg">741.86</mass>
<work uom="MJ">900.63</work>
<efficiency uom="%">44.64</efficiency>
<rvp uom="Pa">473.2</rvp>
<tvp uom="bar">672.31</tvp>
<bsw uom="%">56.58</bsw>
<bswPrevious uom="m3/m3">34.61</bswPrevious>
<densityValue>
<density uom="kg/m3">37.41</density>
<temp uom="K">53.03</temp>
<pres uom="Pa">79.19</pres>
</densityValue>
<density uom="kg/m3">412.02</density>
<densityFlowRate uom="Mg/a">328.63</densityFlowRate>
<densityStd uom="kg/m3">667.03</densityStd>
<concentration uom="ppm">62.47</concentration>
<molecularWeight>40.34</molecularWeight>
<weightPercent uom="%">38.31</weightPercent>
<molePercent uom="%">53.15</molePercent>
<moleAmt uom="kmol">80.5</moleAmt>
<sg uom="Euc">78.32</sg>
<hcDewpoint uom="K">539.52</hcDewpoint>
<waterDewpoint uom="K">647.14</waterDewpoint>
<wobbeIndex uom="J/m3">703.54</wobbeIndex>
<grossCalorificValueStd uom="J/m3">999.35</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">218.7</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">473.17</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">90.92</densityStabilizedCrude>
<product>
<kind>oil - net</kind>
<name namingSystem="TEST411">Test product name 187</name>
<splitFactor>0.11</splitFactor>
<gor uom="Euc">82.69</gor>
<gorMTD uom="m3/m3">63.83</gorMTD>
<waterConcMass uom="%">18.93</waterConcMass>
<waterConcVol uom="ppm">63.88</waterConcVol>
<atmosphere uom="Pa">25.5</atmosphere>
<volumeValue>
<volume status="device failure" uom="m3">505.2</volume>
<grossCalorificValue uom="J/m3">619.52</grossCalorificValue>
<temp uom="K">92.1</temp>
<pres uom="Pa">13.05</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">86.05</volume>
<volumeStd status="bad calibration" uom="m3">50.84</volumeStd>
<flowRate status="bad calibration" uom="m3/s">81.66</flowRate>
<temp uom="K">12.39</temp>
<pres uom="Pa">23.36</pres>
<absoluteMinPres uom="Pa">85.53</absoluteMinPres>
<portDiff uid="a5c6a146-8ae8-11e2-a53c-78acc03c3a5e">
<port uidRef="a5c6a147-8ae8-11e2-9d3d-78acc03c3a5e">Port 1</port>
<presDiff uom="Pa">68.18</presDiff>
<tempDiff uom="K">26.62</tempDiff>
<chokeSize uom="in/32">54.61</chokeSize>
<chokeRelative uom="%">53.42</chokeRelative>
</portDiff>
<portDiff uid="a5c6a148-8ae8-11e2-a4d1-78acc03c3a5e">
<port uidRef="a5c6a149-8ae8-11e2-aab3-78acc03c3a5e">Port 2</port>
<presDiff uom="Pa">33.9</presDiff>
<tempDiff uom="K">83.62</tempDiff>
<chokeSize uom="in/32">50.9</chokeSize>
<chokeRelative uom="%">90.59</chokeRelative>
</portDiff>
<mass uom="kg">413.44</mass>
<work uom="MJ">634.56</work>
<efficiency uom="%">76.94</efficiency>
<rvp uom="Pa">659.3</rvp>
<tvp uom="bar">800.3</tvp>
<bsw uom="%">16.46</bsw>
<bswPrevious uom="m3/m3">42.44</bswPrevious>
<densityValue>
<density uom="kg/m3">440.19</density>
<temp uom="K">50.6</temp>
<pres uom="Pa">45.21</pres>
</densityValue>
<density uom="kg/m3">100.46</density>
<densityFlowRate uom="Mg/a">662.64</densityFlowRate>
<densityStd uom="kg/m3">265.49</densityStd>
<concentration uom="ppm">61.62</concentration>
<molecularWeight>59.0</molecularWeight>
<weightPercent uom="%">63.08</weightPercent>
<molePercent uom="%">92.99</molePercent>
<moleAmt uom="kmol">49.5</moleAmt>
<sg uom="Euc">55.69</sg>
<hcDewpoint uom="K">164.87</hcDewpoint>
<waterDewpoint uom="K">865.69</waterDewpoint>
<wobbeIndex uom="J/m3">378.96</wobbeIndex>
<grossCalorificValueStd uom="J/m3">123.58</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">57.65</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">230.87</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">87.87</densityStabilizedCrude>
<componentContent uid="a5c6a14a-8ae8-11e2-b107-78acc03c3a5e">
<kind>condensate</kind>
<referenceKind>oil</referenceKind>
<gor uom="Euc">60.51</gor>
<gorMTD uom="m3/m3">18.36</gorMTD>
<waterConcMass uom="%">40.9</waterConcMass>
<waterConcVol uom="ppm">86.33</waterConcVol>
<atmosphere uom="Pa">88.88</atmosphere>
<volumeValue>
<volume status="bad calibration" uom="m3">312.64</volume>
<grossCalorificValue uom="J/m3">17.24</grossCalorificValue>
<temp uom="K">71.58</temp>
<pres uom="Pa">84.36</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">60.48</volume>
<volumeStd status="bad calibration" uom="m3">15.54</volumeStd>
<flowRate status="bad calibration" uom="m3/s">52.91</flowRate>
<temp uom="K">52.17</temp>
<pres uom="Pa">62.3</pres>
<absoluteMinPres uom="Pa">12.62</absoluteMinPres>
<portDiff uid="a5c91240-8ae8-11e2-ae52-78acc03c3a5e">
<port uidRef="a5c91241-8ae8-11e2-8794-78acc03c3a5e">Port 1</port>
<presDiff uom="Pa">51.38</presDiff>
<tempDiff uom="K">61.09</tempDiff>
<chokeSize uom="in/32">42.97</chokeSize>
<chokeRelative uom="%">52.18</chokeRelative>
</portDiff>
<portDiff uid="a5c91242-8ae8-11e2-9489-78acc03c3a5e">
<port uidRef="a5c91243-8ae8-11e2-8437-78acc03c3a5e">Port 2</port>
<presDiff uom="Pa">84.67</presDiff>
<tempDiff uom="K">40.75</tempDiff>
<chokeSize uom="in/32">76.06</chokeSize>
<chokeRelative uom="%">88.08</chokeRelative>
</portDiff>
<mass uom="kg">467.73</mass>
<work uom="MJ">840.23</work>
<efficiency uom="%">33.86</efficiency>
<rvp uom="Pa">991.18</rvp>
<tvp uom="bar">755.73</tvp>
<bsw uom="%">78.2</bsw>
<bswPrevious uom="m3/m3">91.4</bswPrevious>
<densityValue>
<density uom="kg/m3">241.87</density>
<temp uom="K">33.79</temp>
<pres uom="Pa">32.72</pres>
</densityValue>
<density uom="kg/m3">576.9</density>
<densityFlowRate uom="Mg/a">105.41</densityFlowRate>
<densityStd uom="kg/m3">55.76</densityStd>
<concentration uom="ppm">20.34</concentration>
<molecularWeight>16.71</molecularWeight>
<weightPercent uom="%">57.89</weightPercent>
<molePercent uom="%">38.67</molePercent>
<moleAmt uom="kmol">67.02</moleAmt>
<sg uom="Euc">21.22</sg>
<hcDewpoint uom="K">715.1</hcDewpoint>
<waterDewpoint uom="K">100.26</waterDewpoint>
<wobbeIndex uom="J/m3">289.8</wobbeIndex>
<grossCalorificValueStd uom="J/m3">363.38</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">407.89</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">704.82</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">257.23</densityStabilizedCrude>
</componentContent>
<period>
<kind>month</kind>
<dateStart>2012-02-01</dateStart>
<dateEnd>2012-02-29</dateEnd>
<gor uom="Euc">55.03</gor>
<gorMTD uom="m3/m3">71.04</gorMTD>
<waterConcMass uom="%">67.41</waterConcMass>
<waterConcVol uom="ppm">31.52</waterConcVol>
<atmosphere uom="Pa">81.95</atmosphere>
<volumeValue>
<volume uom="m3">615.87</volume><temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">31.27</volume>
<volumeStd status="bad calibration" uom="m3">43.03</volumeStd>
<flowRate status="bad calibration" uom="m3/s">57.45</flowRate>
<temp uom="K">41.0</temp>
<pres uom="Pa">48.88</pres>
<absoluteMinPres uom="Pa">55.29</absoluteMinPres>
<mass uom="kg">224.73</mass>
<work uom="kW.h">491.2</work>
<efficiency uom="%">15.12</efficiency>
<rvp uom="kPa">900.96</rvp>
<tvp uom="bar">827.62</tvp>
<bsw uom="%">58.3</bsw>
<bswPrevious uom="m3/m3">51.07</bswPrevious>
<densityValue>
<density uom="kg/m3">786.94</density>
<temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</densityValue>
<density uom="kg/m3">334.31</density>
<densityFlowRate uom="Mg/a">290.09</densityFlowRate>
<densityStd uom="kg/m3">412.8</densityStd>
<concentration uom="ppm">53.22</concentration>
<molecularWeight>50.39</molecularWeight>
<weightPercent uom="%">12.68</weightPercent>
<molePercent uom="%">97.96</molePercent>
<moleAmt uom="kmol">68.2</moleAmt>
<sg uom="Euc">18.88</sg>
<hcDewpoint uom="K">339.08</hcDewpoint>
<waterDewpoint uom="K">722.12</waterDewpoint>
<wobbeIndex uom="J/m3">108.08</wobbeIndex>
<grossCalorificValueStd uom="J/m3">230.02</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">322.68</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">84.89</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">124.95</densityStabilizedCrude>
</period>
</product>
</flow>
</facility>
</object>
</objects>
\ No newline at end of file
<?xml version="1.0" encoding="UTF-8"?>
<objects xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance"
xmlns="http://www.epim.no/schemas/mprml/1" version="1.0(MPRML)">
<documentInfo>
<DocumentName namingSystem="EC">ÅSGARD January 2012</DocumentName>
<DocumentAlias namingSystem="EC">ÅSGARD Copex Report</DocumentAlias>
<DocumentDate>2012-02-05T00:00:00.0Z</DocumentDate>
<documentClass namingSystem="EC">Statoil Petroleum AS</documentClass>
<documentClass namingSystem="EC">Copex</documentClass>
<documentClass namingSystem="ERH">mprg</documentClass>
<FileCreationInformation>
<FileCreationDate>2012-02-05T00:00:00.0Z</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>Copex</kind>
<title>ÅSGARD</title>
<date>2012-01-01</date>
<dateEnd>2012-01-31</dateEnd>
<month>2012-01</month>
<year>2012</year>
<reportVersion>1.1</reportVersion>
<reportStatus>preliminary</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_productVolume">
<name>KRISTIN</name>
<installation kind="field" namingSystem="NPD" uidRef="1854729">KRISTIN</installation>
<facility>
<name kind="field" namingSystem="NPD" uidRef="1854729">KRISTIN</name>
<flow uid="KRISTIN_SALEABLE_PRODUCTION">
<name>Kristin saleable volumes</name>
<kind>production</kind>
<qualifier>saleable</qualifier>
<product>
<kind>oil - net</kind>
<period>
<kind>month</kind>
<dateStart>2012-01-01</dateStart>
<dateEnd>2012-01-31</dateEnd>
<volumeValue>
<volume uom="m3">101952.5</volume><temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</volumeValue>
<mass uom="kg">84401518.61</mass>
<densityValue>
<density uom="kg/m3">774.07</density>
<temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</densityValue>
</period>
</product>
</flow>
<flow uid="KRISTIN_ALLOCATED_PRODUCTION">
<name>Kristin allocated volumes</name>
<kind>production</kind>
<qualifier>allocated</qualifier>
<product>
<kind>oil - net</kind>
<period>
<kind>month</kind>
<dateStart>2012-01-01</dateStart>
<dateEnd>2012-01-31</dateEnd>
<volumeValue>
<volume uom="m3">268450.47</volume><temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</volumeValue>
<mass uom="kg">32174682.0</mass>
<densityValue>
<density uom="kg/m3">757.27</density>
<temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</densityValue>
</period>
</product><product>
<kind>gas</kind>
<period>
<kind>month</kind>
<dateStart>2012-01-01</dateStart>
<dateEnd>2012-01-31</dateEnd>
<volumeValue>
<volume uom="m3">201065.05</volume><temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</volumeValue>
<mass uom="kg">35541182.56</mass>
<densityValue>
<density uom="kg/m3">0.7</density>
<temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</densityValue>
</period>
</product><product>
<kind>condensate - net</kind>
<period>
<kind>month</kind>
<dateStart>2012-01-01</dateStart>
<dateEnd>2012-01-31</dateEnd>
<volumeValue>
<volume uom="m3">255563.75</volume><temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</volumeValue>
<mass uom="kg">34560058.23</mass>
<densityValue>
<density uom="kg/m3">776.07</density>
<temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</densityValue>
</period>
</product><product>
<kind>water</kind>
<period>
<kind>month</kind>
<dateStart>2012-01-01</dateStart>
<dateEnd>2012-01-31</dateEnd>
<volumeValue>
<volume uom="m3">269306.2</volume><temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</volumeValue>
</period>
</product>
</flow>
<flow uid="KRISTIN_GAS_INJECTION_TOT">
<name>Kristin injected gas</name>
<kind>injection</kind>
<qualifier>allocated</qualifier>
<product>
<kind>gas</kind>
<period>
<kind>month</kind>
<dateStart>2012-01-01</dateStart>
<dateEnd>2012-01-31</dateEnd>
<volumeValue>
<volume uom="m3">229560.79</volume><temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</volumeValue>
<mass uom="kg">39685285.41</mass>
<densityValue>
<density uom="kg/m3">0.93</density>
<temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</densityValue>
</period>
</product>
</flow>
<flow uid="KRISTIN_CHEMICAL_INJECTION">
<name>Kristin injection of chemicals</name>
<kind>injection</kind>
<qualifier>measured</qualifier>
<product>
<kind>chemical</kind>
<name>Wax inhibitor</name>
<period>
<kind>month</kind>
<dateStart>2012-01-01</dateStart>
<dateEnd>2012-01-31</dateEnd>
<volumeValue>
<volume uom="L">2292.35</volume>
<temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</volumeValue>
</period>
</product><product>
<kind>chemical</kind>
<name>Scale inhibitor</name>
<period>
<kind>month</kind>
<dateStart>2012-01-01</dateStart>
<dateEnd>2012-01-31</dateEnd>
<volumeValue>
<volume uom="L">1353.31</volume>
<temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</volumeValue>
</period>
</product><product>
<kind>chemical</kind>
<name>Methanol</name>
<period>
<kind>month</kind>
<dateStart>2012-01-01</dateStart>
<dateEnd>2012-01-31</dateEnd>
<volumeValue>
<volume uom="L">1558.79</volume>
<temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</volumeValue>
</period>
</product>
</flow><flow uid="KRISTIN_FISCAL_FIELD_VOLUMES">
<name>Kristin measured total volumes</name>
<kind>production</kind>
<qualifier>metered - fiscal</qualifier>
<product>
<kind>oil - net</kind>
<period>
<kind>month</kind>
<dateStart>2012-01-01</dateStart>
<dateEnd>2012-01-31</dateEnd>
<volumeValue>
<volume uom="m3">127491.0</volume><temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</volumeValue>
<mass uom="kg">74071145.34</mass>
<densityValue>
<density uom="kg/m3">768.05</density>
<temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</densityValue>
</period>
</product><product>
<kind>gas</kind>
<period>
<kind>month</kind>
<dateStart>2012-01-01</dateStart>
<dateEnd>2012-01-31</dateEnd>
<volumeValue>
<volume uom="m3">108383.31</volume><temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</volumeValue>
<mass uom="kg">70079142.44</mass>
<densityValue>
<density uom="kg/m3">0.76</density>
<temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</densityValue>
</period>
</product><product>
<kind>water</kind>
<period>
<kind>month</kind>
<dateStart>2012-01-01</dateStart>
<dateEnd>2012-01-31</dateEnd>
<volumeValue>
<volume uom="m3">106565.38</volume><temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</volumeValue>
</period>
</product>
</flow>
<flow uid="KRISTIN_ALLOCATED_INVENTORY_TOT">
<name>Kristin total allocated inventory</name>
<kind>inventory</kind>
<qualifier>allocated</qualifier>
<product>
<kind>oil - net</kind>
<period>
<kind>month</kind>
<dateStart>2012-01-01</dateStart>
<dateEnd>2012-01-31</dateEnd>
<volumeValue>
<volume uom="m3">101471.53</volume>
<temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</volumeValue>
<mass uom="kg">86757279.07</mass>
<densityValue>
<density uom="kg/m3">762.24</density>
<temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</densityValue>
<balanceSet>
<kind>closing balance</kind>
<balanceDetail>
<owner>PETORO</owner>
<volumeValue>
<volume uom="m3">31466.321453</volume>
<temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</volumeValue>
<mass uom="kg">26903432.2396</mass>
</balanceDetail><balanceDetail>
<owner>TOTAL</owner>
<volumeValue>
<volume uom="m3">4119.744118</volume>
<temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</volumeValue>
<mass uom="kg">3522345.53024</mass>
</balanceDetail><balanceDetail>
<owner>STATOIL</owner>
<volumeValue>
<volume uom="m3">54327.857162</volume>
<temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</volumeValue>
<mass uom="kg">46449847.2141</mass>
</balanceDetail><balanceDetail>
<owner>EXXONMOBIL PROD</owner>
<volumeValue>
<volume uom="m3">2496.199638</volume>
<temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</volumeValue>
<mass uom="kg">2134229.06512</mass>
</balanceDetail><balanceDetail>
<owner>ENI NORGE</owner>
<volumeValue>
<volume uom="m3">9061.407629</volume>
<temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</volumeValue>
<mass uom="kg">7747425.02095</mass>
</balanceDetail>
</balanceSet>
</period>
</product>
</flow>
<flow uid="KRISTIN_ALLOCATED_GAS_SALES">
<name>Kristin allocated gas sales</name>
<kind>sale</kind>
<qualifier>allocated</qualifier>
<product>
<kind>gas - dry</kind>
<period>
<kind>month</kind>
<dateStart>2012-01-01</dateStart>
<dateEnd>2012-01-31</dateEnd>
<balanceSet>
<kind>transaction</kind>
<volumeValue>
<volume uom="m3">775.4</volume>
<temp uom="degC">0</temp>
<pres uom="atm">1</pres>
</volumeValue>
<work uom="MJ">20800.38</work>
<balanceDetail>
<owner>STATOIL</owner>
<seller>STATOIL</seller>
<salesAdministrator>STATOIL</salesAdministrator>
<buyer>EXXONMOBIL GAS DE</buyer>
<volumeValue>
<volume uom="m3">512.67</volume>
<temp uom="degC">0</temp>
<pres uom="atm">1</pres>
</volumeValue>
<work uom="MJ">23118.03</work>
</balanceDetail><balanceDetail>
<owner>STATOIL</owner>
<seller>STATOIL</seller>
<salesAdministrator>STATOIL</salesAdministrator>
<buyer>DONG DK</buyer>
<volumeValue>
<volume uom="m3">262.73</volume>
<temp uom="degC">0</temp>
<pres uom="atm">1</pres>
</volumeValue>
<work uom="MJ">27169.3</work>
</balanceDetail>
</balanceSet><balanceSet>
<kind>transaction</kind>
<volumeValue>
<volume uom="m3">975.26</volume>
<temp uom="degC">0</temp>
<pres uom="atm">1</pres>
</volumeValue>
<work uom="MJ">43368.46</work>
<balanceDetail>
<owner>STATOIL</owner>
<seller>STATOIL</seller>
<salesAdministrator>STATOIL</salesAdministrator>
<buyer>NATURGAS VEST</buyer>
<volumeValue>
<volume uom="m3">843.19</volume>
<temp uom="degC">0</temp>
<pres uom="atm">1</pres>
</volumeValue>
<work uom="MJ">27742.43</work>
</balanceDetail><balanceDetail>
<owner>STATOIL</owner>
<seller>STATOIL</seller>
<salesAdministrator>STATOIL</salesAdministrator>
<buyer>EXXONMOBIL GAS DE</buyer>
<volumeValue>
<volume uom="m3">132.07</volume>
<temp uom="degC">0</temp>
<pres uom="atm">1</pres>
</volumeValue>
<work uom="MJ">8762.27</work>
</balanceDetail>
</balanceSet><balanceSet>
<kind>transaction</kind>
<volumeValue>
<volume uom="m3">936.38</volume>
<temp uom="degC">0</temp>
<pres uom="atm">1</pres>
</volumeValue>
<work uom="MJ">17147.72</work>
<balanceDetail>
<owner>STATOIL</owner>
<seller>STATOIL</seller>
<salesAdministrator>STATOIL</salesAdministrator>
<buyer>NATURGAS VEST</buyer>
<volumeValue>
<volume uom="m3">936.38</volume>
<temp uom="degC">0</temp>
<pres uom="atm">1</pres>
</volumeValue>
<work uom="MJ">27534.9</work>
</balanceDetail>
</balanceSet>
</period>
</product>
</flow>
</facility>
</object>
</objects>
\ No newline at end of file