FlowFromTank-DPR2.0.xml
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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>2012-03-04T00:00:00.0Z</DocumentDate>
<documentClass namingSystem="EC">Dong E&P Norge AS</documentClass>
<documentClass namingSystem="EC">DPR 2.0</documentClass>
<documentClass namingSystem="ERH">dpr2</documentClass>
<FileCreationInformation>
<FileCreationDate>2012-03-14T00:00:00.0Z</FileCreationDate>
<SoftwareName>Energy Components</SoftwareName>
<FileCreator>Dong E&P Norge AS</FileCreator>
<Comment>NA</Comment>
</FileCreationInformation>
<Owner>Dong E&P Norge AS</Owner>
</documentInfo>
<context xsi:type="obj_report">
<kind>DPR 2.0</kind>
<title>OSELVAR</title>
<date>2012-02-28</date>
<dateEnd>2012-02-28</dateEnd>
<month>2012-02</month>
<year>2012</year>
<reportVersion>1.2</reportVersion>
<reportStatus>final</reportStatus>
<installation kind="field" namingSystem="NPD">OSELVAR</installation>
<operator>
<name>Dong E&P Norge AS</name>
<role>Operating company</role>
</operator>
</context>
<object xsi:type="obj_productVolume">
<name>OSELVAR</name>
<installation kind="field" namingSystem="NPD">OSELVAR</installation>
<standardTempPres>0 degC 1 atm</standardTempPres>
<facility>
<name kind="tank" namingSystem="DONG" uidRef="NaN">TK0420</name>
<flow>
<name>OSL MEG TANK1 CONS MEAS CHEM</name>
<kind>consume</kind>
<qualifier>measured</qualifier>
<version>2012-02-28T21:00:00.0Z</version>
<versionSource>version src 726</versionSource>
<gor uom="Euc">55.81</gor>
<gorMTD uom="m3/m3">95.86</gorMTD>
<waterConcMass uom="%">99.52</waterConcMass>
<waterConcVol uom="ppm">27.17</waterConcVol>
<atmosphere uom="Pa">41.37</atmosphere>
<volumeValue>
<volume status="comm failure" uom="m3">339.12</volume>
<grossCalorificValue uom="J/m3">987.06</grossCalorificValue>
<temp uom="K">66.34</temp>
<pres uom="Pa">58.84</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">95.52</volume>
<volumeStd status="bad calibration" uom="m3">40.08</volumeStd>
<flowRate status="bad calibration" uom="m3/s">82.26</flowRate>
<product>
<kind>oil - gross</kind>
<name namingSystem="TEST484">Test product name 791</name>
<splitFactor>0.29</splitFactor>
<gor uom="Euc">43.79</gor>
<gorMTD uom="m3/m3">38.14</gorMTD>
<waterConcMass uom="%">46.18</waterConcMass>
<waterConcVol uom="ppm">39.2</waterConcVol>
<atmosphere uom="Pa">79.21</atmosphere>
<volumeValue>
<volume status="comm failure" uom="m3">915.72</volume>
<grossCalorificValue uom="J/m3">244.95</grossCalorificValue>
<temp uom="K">68.94</temp>
<pres uom="Pa">33.34</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">23.78</volume>
<volumeStd status="bad calibration" uom="m3">77.03</volumeStd>
<flowRate status="bad calibration" uom="m3/s">46.36</flowRate>
<temp uom="K">13.23</temp>
<pres uom="Pa">34.92</pres>
<absoluteMinPres uom="Pa">36.61</absoluteMinPres>
<portDiff uid="f69e9f51-12d9-11e2-b954-d067e534860e">
<port uidRef="f69e9f52-12d9-11e2-b96d-d067e534860e">Port 1</port>
<presDiff uom="Pa">29.48</presDiff>
<tempDiff uom="K">35.77</tempDiff>
<chokeSize uom="in/32">65.85</chokeSize>
<chokeRelative uom="%">65.02</chokeRelative>
</portDiff>
<portDiff uid="f69e9f53-12d9-11e2-b64e-d067e534860e">
<port uidRef="f69e9f54-12d9-11e2-bbea-d067e534860e">Port 2</port>
<presDiff uom="Pa">54.02</presDiff>
<tempDiff uom="K">99.07</tempDiff>
<chokeSize uom="in/32">64.92</chokeSize>
<chokeRelative uom="%">60.85</chokeRelative>
</portDiff>
<mass uom="kg">195.62</mass>
<work uom="MJ">728.23</work>
<efficiency uom="%">23.73</efficiency>
<rvp uom="Pa">150.85</rvp>
<tvp uom="bar">772.75</tvp>
<bsw uom="%">39.02</bsw>
<bswPrevious uom="m3/m3">34.27</bswPrevious>
<densityValue>
<density uom="kg/m3">552.48</density>
<temp uom="K">39.99</temp>
<pres uom="Pa">26.03</pres>
</densityValue>
<density uom="kg/m3">378.88</density>
<densityFlowRate uom="Mg/a">496.24</densityFlowRate>
<densityStd uom="kg/m3">300.14</densityStd>
<concentration uom="ppm">28.08</concentration>
<molecularWeight>90.61</molecularWeight>
<weightPercent uom="%">65.51</weightPercent>
<molePercent uom="%">57.58</molePercent>
<moleAmt uom="kmol">16.98</moleAmt>
<sg uom="Euc">18.21</sg>
<hcDewpoint uom="K">261.68</hcDewpoint>
<waterDewpoint uom="K">664.2</waterDewpoint>
<wobbeIndex uom="J/m3">635.05</wobbeIndex>
<grossCalorificValueStd uom="J/m3">976.34</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">931.43</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">596.37</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">678.95</densityStabilizedCrude>
<componentContent uid="f69e9f55-12d9-11e2-bda3-d067e534860e">
<kind>oil - net</kind>
<referenceKind>vapor</referenceKind>
<gor uom="Euc">64.75</gor>
<gorMTD uom="m3/m3">70.72</gorMTD>
<waterConcMass uom="%">31.95</waterConcMass>
<waterConcVol uom="ppm">88.44</waterConcVol>
<atmosphere uom="Pa">87.8</atmosphere>
<volumeValue>
<volume status="questionable" uom="m3">758.79</volume>
<grossCalorificValue uom="J/m3">743.79</grossCalorificValue>
<temp uom="K">28.91</temp>
<pres uom="Pa">37.78</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">27.49</volume>
<volumeStd status="bad calibration" uom="m3">16.75</volumeStd>
<flowRate status="bad calibration" uom="m3/s">44.69</flowRate>
<temp uom="K">23.86</temp>
<pres uom="Pa">42.98</pres>
<absoluteMinPres uom="Pa">13.58</absoluteMinPres>
<portDiff uid="f69ec661-12d9-11e2-a856-d067e534860e">
<port uidRef="f69ec662-12d9-11e2-ba09-d067e534860e">Port 1</port>
<presDiff uom="Pa">68.14</presDiff>
<tempDiff uom="K">30.85</tempDiff>
<chokeSize uom="in/32">19.01</chokeSize>
<chokeRelative uom="%">35.48</chokeRelative>
</portDiff>
<portDiff uid="f69ec663-12d9-11e2-896f-d067e534860e">
<port uidRef="f69ec664-12d9-11e2-9f42-d067e534860e">Port 2</port>
<presDiff uom="Pa">38.84</presDiff>
<tempDiff uom="K">51.72</tempDiff>
<chokeSize uom="in/32">56.47</chokeSize>
<chokeRelative uom="%">53.79</chokeRelative>
</portDiff>
<mass uom="kg">349.36</mass>
<work uom="MJ">235.95</work>
<efficiency uom="%">62.82</efficiency>
<rvp uom="Pa">975.21</rvp>
<tvp uom="bar">878.48</tvp>
<bsw uom="%">26.81</bsw>
<bswPrevious uom="m3/m3">35.68</bswPrevious>
<densityValue>
<density uom="kg/m3">74.09</density>
<temp uom="K">83.37</temp>
<pres uom="Pa">15.41</pres>
</densityValue>
<density uom="kg/m3">414.68</density>
<densityFlowRate uom="Mg/a">621.95</densityFlowRate>
<densityStd uom="kg/m3">618.24</densityStd>
<concentration uom="ppm">25.04</concentration>
<molecularWeight>92.78</molecularWeight>
<weightPercent uom="%">42.47</weightPercent>
<molePercent uom="%">64.66</molePercent>
<moleAmt uom="kmol">98.37</moleAmt>
<sg uom="Euc">77.2</sg>
<hcDewpoint uom="K">84.09</hcDewpoint>
<waterDewpoint uom="K">576.56</waterDewpoint>
<wobbeIndex uom="J/m3">568.53</wobbeIndex>
<grossCalorificValueStd uom="J/m3">925.43</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">324.93</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">268.91</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">703.27</densityStabilizedCrude>
</componentContent>
<period>
<kind>day</kind>
<dateStart>2012-02-28</dateStart>
<dateEnd>2012-02-28</dateEnd>
<gor uom="Euc">91.18</gor>
<gorMTD uom="m3/m3">50.18</gorMTD>
<waterConcMass uom="%">18.4</waterConcMass>
<waterConcVol uom="ppm">99.56</waterConcVol>
<atmosphere uom="Pa">82.72</atmosphere>
<volumeValue>
<volume uom="m3">1844.83</volume><temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">21.98</volume>
<volumeStd status="bad calibration" uom="m3">83.58</volumeStd>
<flowRate status="bad calibration" uom="m3/s">44.68</flowRate>
<temp uom="K">62.0</temp>
<pres uom="Pa">57.99</pres>
<absoluteMinPres uom="Pa">98.21</absoluteMinPres>
<mass uom="kg">900.4</mass>
<work uom="J">510.98</work>
<efficiency uom="%">56.43</efficiency>
<rvp uom="Pa">942.18</rvp>
<tvp uom="bar">171.81</tvp>
<bsw uom="%">21.04</bsw>
<bswPrevious uom="m3/m3">76.96</bswPrevious>
<densityValue>
<density uom="kg/m3">701.36</density>
<temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</densityValue>
<density uom="kg/m3">329.8</density>
<densityFlowRate uom="Mg/a">466.61</densityFlowRate>
<densityStd uom="kg/m3">139.14</densityStd>
<concentration uom="ppm">28.48</concentration>
<molecularWeight>84.1</molecularWeight>
<weightPercent uom="%">90.22</weightPercent>
<molePercent uom="%">19.83</molePercent>
<moleAmt uom="kmol">30.7</moleAmt>
<sg uom="Euc">60.02</sg>
<hcDewpoint uom="K">143.79</hcDewpoint>
<waterDewpoint uom="K">551.42</waterDewpoint>
<wobbeIndex uom="J/m3">327.48</wobbeIndex>
<grossCalorificValueStd uom="J/m3">501.58</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">376.43</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">498.53</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">528.55</densityStabilizedCrude>
</period>
</product>
</flow>
</facility>
</object>
</objects>