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David Price
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Upload of results of file split for testing

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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>
<dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
<remark>For any transformation which is sufficiently diversified in application to be of any interest, the t</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, 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>
<supplyShipComment>
<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>
<supplyShipComment>
<dTimStart>2012-03-01T06:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T08:00:00.0Z</dTimEnd>
<remark>Thus a subset of English sentences interesting on quite independent grounds is to be regarded as a d</remark>
</supplyShipComment>
<standbyVesselComment>
<dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
<remark>It appears that the systematic use of complex symbols is to be regarded as problems of phonemic and </remark>
</standbyVesselComment>
<basketMovement>
<dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
<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>
<dTimEnd>2012-03-01T04:00:00.0Z</dTimEnd>
<remark>A consequence of the approach just outlined is that the systematic use of complex symbols delimits t</remark>
</basketMovement>
<activity>
<dTimStart>2012-03-01T06:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T08:00:00.0Z</dTimEnd>
<remark>In the discussion of resumptive pronouns following (81), the theory of syntactic features developed </remark>
</activity>
<activity>
<dTimStart>2012-03-01T09:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T11:00:00.0Z</dTimEnd>
<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>
<oilGrossStdTempPres uom="m3">5381.62</oilGrossStdTempPres>
<oilGrossTotalStdTempPres uom="m3">6615.82</oilGrossTotalStdTempPres>
<oilNetStdTempPres uom="m3">5342.1</oilNetStdTempPres>
<oilNetMonthToDateStdTempPres uom="m3">5241.47</oilNetMonthToDateStdTempPres>
<densityStdTempPres uom="kg/m3">719.05</densityStdTempPres>
<rvp uom="Pa">132.25</rvp>
<bsw uom="Euc">197.35</bsw>
<salt uom="kg/m3">116.05</salt>
<comment>
<dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
<remark>This suggests that a case of semigrammaticalness of a different sort does not affect the structure o</remark>
</comment>
<comment>
<dTimStart>2012-03-01T01:00:00.0Z</dTimStart>
<dTimEnd>2012-03-01T02:00:00.0Z</dTimEnd>
<remark>In the discussion of resumptive pronouns following (81), a case of semigrammaticalness of a differen</remark>
</comment>
</cargoShipOperation>
<operationalComment>
<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>
<dTimEnd>2012-03-01T12:00:00.0Z</dTimEnd>
<comment>For any transformation which is sufficiently diversified in application to be of any interest, the t</comment>
</operationalComment>
</productionActivity>
</installationReport>
</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="a5939051-bad4-11e1-acc2-c0f8dae91040">
<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>A consequence of the approach just outlined is that the speaker-hearer's linguistic intuition delimi</remark>
</downtimeReason>
<downtimeReason uid="a5939052-bad4-11e1-9b76-c0f8dae91040">
<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>To characterize a linguistic level L, a descriptively adequate grammar does not readily tolerate the</remark>
</downtimeReason>
<flow>
<kind>production</kind>
<qualifier>saleable</qualifier>
<version>2012-03-01T22:00:00.0Z</version>
<versionSource>version src 914</versionSource>
<gor uom="Euc">53.07</gor>
<gorMTD uom="m3/m3">51.46</gorMTD>
<waterConcMass uom="%">91.44</waterConcMass>
<waterConcVol uom="ppm">49.19</waterConcVol>
<atmosphere uom="Pa">75.38</atmosphere>
<volumeValue>
<volume status="questionable" uom="m3">785.16</volume>
<grossCalorificValue uom="J/m3">641.22</grossCalorificValue>
<temp uom="K">35.18</temp>
<pres uom="Pa">94.73</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">18.01</volume>
<volumeStd status="bad calibration" uom="m3">16.78</volumeStd>
<flowRate status="bad calibration" uom="m3/s">25.65</flowRate>
<temp uom="K">61.2</temp>
<pres uom="Pa">41.65</pres>
<absoluteMinPres uom="Pa">65.2</absoluteMinPres>
<portDiff uid="a593b75e-bad4-11e1-8a2f-c0f8dae91040">
<port uidRef="a593b75f-bad4-11e1-9811-c0f8dae91040">Port 1</port>
<presDiff uom="Pa">77.05</presDiff>
<tempDiff uom="K">20.15</tempDiff>
<chokeSize uom="in/32">71.74</chokeSize>
<chokeRelative uom="%">23.04</chokeRelative>
</portDiff>
<portDiff uid="a593b760-bad4-11e1-852b-c0f8dae91040">
<port uidRef="a593b761-bad4-11e1-913c-c0f8dae91040">Port 2</port>
<presDiff uom="Pa">29.37</presDiff>
<tempDiff uom="K">33.5</tempDiff>
<chokeSize uom="in/32">55.86</chokeSize>
<chokeRelative uom="%">62.26</chokeRelative>
</portDiff>
<mass uom="kg">596.23</mass>
<work uom="MJ">116.13</work>
<efficiency uom="%">58.88</efficiency>
<rvp uom="Pa">761.31</rvp>
<tvp uom="bar">609.35</tvp>
<bsw uom="%">38.95</bsw>
<bswPrevious uom="m3/m3">37.52</bswPrevious>
<densityValue>
<density uom="kg/m3">154.93</density>
<temp uom="K">43.99</temp>
<pres uom="Pa">84.69</pres>
</densityValue>
<density uom="kg/m3">134.58</density>
<densityFlowRate uom="Mg/a">291.27</densityFlowRate>
<densityStd uom="kg/m3">422.56</densityStd>
<concentration uom="ppm">27.37</concentration>
<molecularWeight>42.48</molecularWeight>
<weightPercent uom="%">90.64</weightPercent>
<molePercent uom="%">98.52</molePercent>
<moleAmt uom="kmol">22.78</moleAmt>
<sg uom="Euc">59.65</sg>
<hcDewpoint uom="K">918.59</hcDewpoint>
<waterDewpoint uom="K">505.72</waterDewpoint>
<wobbeIndex uom="J/m3">783.46</wobbeIndex>
<grossCalorificValueStd uom="J/m3">35.94</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">973.12</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">854.65</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">610.47</densityStabilizedCrude>
<product>
<kind>oil - net</kind>
<name namingSystem="TEST17">Test product name 507</name>
<splitFactor>0.67</splitFactor>
<gor uom="Euc">45.98</gor>
<gorMTD uom="m3/m3">54.61</gorMTD>
<waterConcMass uom="%">24.57</waterConcMass>
<waterConcVol uom="ppm">49.63</waterConcVol>
<atmosphere uom="Pa">96.97</atmosphere>
<volumeValue>
<volume status="questionable" uom="m3">882.04</volume>
<grossCalorificValue uom="J/m3">412.16</grossCalorificValue>
<temp uom="K">60.27</temp>
<pres uom="Pa">76.05</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">92.12</volume>
<volumeStd status="bad calibration" uom="m3">18.65</volumeStd>
<flowRate status="bad calibration" uom="m3/s">60.29</flowRate>
<temp uom="K">98.91</temp>
<pres uom="Pa">82.78</pres>
<absoluteMinPres uom="Pa">34.27</absoluteMinPres>
<portDiff uid="a593b762-bad4-11e1-a353-c0f8dae91040">
<port uidRef="a593b763-bad4-11e1-9822-c0f8dae91040">Port 1</port>
<presDiff uom="Pa">67.4</presDiff>
<tempDiff uom="K">54.21</tempDiff>
<chokeSize uom="in/32">79.02</chokeSize>
<chokeRelative uom="%">44.15</chokeRelative>
</portDiff>
<portDiff uid="a593b764-bad4-11e1-ace2-c0f8dae91040">
<port uidRef="a593b765-bad4-11e1-9607-c0f8dae91040">Port 2</port>
<presDiff uom="Pa">41.6</presDiff>
<tempDiff uom="K">90.5</tempDiff>
<chokeSize uom="in/32">65.45</chokeSize>
<chokeRelative uom="%">57.19</chokeRelative>
</portDiff>
<mass uom="kg">79.45</mass>
<work uom="MJ">181.12</work>
<efficiency uom="%">33.95</efficiency>
<rvp uom="Pa">705.54</rvp>
<tvp uom="bar">153.81</tvp>
<bsw uom="%">32.3</bsw>
<bswPrevious uom="m3/m3">95.5</bswPrevious>
<densityValue>
<density uom="kg/m3">175.98</density>
<temp uom="K">56.57</temp>
<pres uom="Pa">45.46</pres>
</densityValue>
<density uom="kg/m3">36.16</density>
<densityFlowRate uom="Mg/a">274.98</densityFlowRate>
<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