David Price

Load updated EPIM DPR2 test cases

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<DocumentAlias namingSystem="EC">TRYM Copex Report</DocumentAlias>
<DocumentDate>2012-03-04T00:00:00.0Z</DocumentDate>
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<documentClass namingSystem="EC">DPR 2.0</documentClass>
<documentClass namingSystem="ERH">dpr2</documentClass>
<FileCreationInformation>
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<SoftwareName>Energy Components</SoftwareName>
<FileCreator>Dong E&amp;P Norge AS</FileCreator>
<Comment>NA</Comment>
</FileCreationInformation>
<Owner>Dong E&amp;P Norge AS</Owner>
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<kind>DPR 2.0</kind>
<title>TRYM</title>
<date>2012-02-28</date>
<dateEnd>2012-02-28</dateEnd>
<month>2012-02</month>
<year>2012</year>
<reportVersion>2.0</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_fluidSample">
<name>TRYM-LIQUID-CHARACTERISTICS-1</name>
<sampleType>separator oil</sampleType>
<facility kind="field" namingSystem="NPD" uidRef="18081500">TRYM</facility>
<acquisitionDate>2012-02-11</acquisitionDate>
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</object>
<object xsi:type="obj_fluidSample">
<name>TRYM-GAS-CHARACTERISTICS-1</name>
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<facility kind="field" namingSystem="NPD" uidRef="18081500">TRYM</facility>
<acquisitionDate>2012-02-09</acquisitionDate>
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<specificGravity>0.716</specificGravity>
<rvp uom="bar">231</rvp>
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<fluidSampleComposition>
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</fluidSampleComposition>
<fluidSampleComposition>
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<fluidSampleComposition>
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<fluidSampleComposition>
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</fluidSampleComposition>
</object><object xsi:type="obj_fluidSample">
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<sampleType>separator oil</sampleType>
<facility kind="field" namingSystem="NPD" uidRef="18081500">TRYM</facility>
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<customData>
<extensionNameValue>
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<name>ValidTo</name>
<value>2012-02-20T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
</customData>
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<name>TRYM-GAS-CHARACTERISTICS-2</name>
<sampleType>separator gas</sampleType>
<facility kind="field" namingSystem="NPD" uidRef="18081500">TRYM</facility>
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<customData>
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<name>ValidFrom</name>
<value>2012-02-09T00:00:00.0Z</value>
<dataType>dateTime</dataType>
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<extensionNameValue>
<name>ValidTo</name>
<value>2012-02-26T00:00:00.0Z</value>
<dataType>dateTime</dataType>
</extensionNameValue>
</customData>
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<object xsi:type="obj_fluidAnalysisResult">
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<isPrimary>true</isPrimary>
<componentName>C7+</componentName>
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<specificGravity>0.716</specificGravity>
<rvp uom="bar">231</rvp>
</fluidSampleComposition>
<fluidSampleComposition>
<isPrimary>false</isPrimary>
<componentName>C1</componentName>
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<fluidSampleComposition>
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<componentName>C3</componentName>
<componentKind>frac</componentKind>
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</fluidSampleComposition>
<fluidSampleComposition>
<isPrimary>false</isPrimary>
<componentName>C6+</componentName>
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<molePercent uom="%">2.5</molePercent>
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<fluidSampleComposition>
<isPrimary>false</isPrimary>
<componentName>CO2</componentName>
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<molePercent uom="%">1.000</molePercent>
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<fluidSampleComposition>
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<fluidSampleComposition>
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<fluidSampleComposition>
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<fluidSampleComposition>
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<fluidSampleComposition>
<isPrimary>false</isPrimary>
<componentName>NC5</componentName>
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</fluidSampleComposition>
</object>
<object xsi:type="obj_fluidAnalysisResult">
<nameFluidSample>TRYM-GAS-CHARACTERISTICS-2</nameFluidSample>
<name>TRYM gas characteristics</name>
<fluidSampleComposition>
<isPrimary>true</isPrimary>
<componentName>gas</componentName>
<componentKind>frac</componentKind>
<molecularWeight>21.340</molecularWeight>
<specificGravity>0.716</specificGravity>
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<fluidSampleComposition>
<isPrimary>false</isPrimary>
<componentName>C1</componentName>
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<fluidSampleComposition>
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<componentName>C2</componentName>
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<fluidSampleComposition>
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<fluidSampleComposition>
<isPrimary>false</isPrimary>
<componentName>C6+</componentName>
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<fluidSampleComposition>
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<fluidSampleComposition>
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<fluidSampleComposition>
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<fluidSampleComposition>
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<fluidSampleComposition>
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<weightPercent uom="%">82.0000</weightPercent>
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</fluidSampleComposition>
</object><object xsi:type="obj_fluidSample">
<name>TRYM-LIQUID-CHARACTERISTICS-3</name>
<sampleType>separator oil</sampleType>
<facility kind="field" namingSystem="NPD" uidRef="18081500">TRYM</facility>
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<value>2012-02-27T00:00:00.0Z</value>
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<value>2012-02-26T00:00:00.0Z</value>
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</object>
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<name>TRYM liquid characteristics</name>
<fluidSampleComposition>
<isPrimary>true</isPrimary>
<componentName>C7+</componentName>
<componentKind>frac</componentKind>
<molecularWeight>21.340</molecularWeight>
<specificGravity>0.716</specificGravity>
<rvp uom="bar">231</rvp>
</fluidSampleComposition>
<fluidSampleComposition>
<isPrimary>false</isPrimary>
<componentName>C1</componentName>
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<weightPercent uom="%">0.1</weightPercent>
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</fluidSampleComposition>
<fluidSampleComposition>
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<fluidSampleComposition>
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<fluidSampleComposition>
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<componentName>C6+</componentName>
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<fluidSampleComposition>
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<fluidSampleComposition>
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<fluidSampleComposition>
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<fluidSampleComposition>
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</object>
<object xsi:type="obj_fluidAnalysisResult">
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<molecularWeight>21.340</molecularWeight>
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</fluidSampleComposition>
<fluidSampleComposition>
<isPrimary>false</isPrimary>
<componentName>C1</componentName>
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<fluidSampleComposition>
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<fluidSampleComposition>
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<componentName>C3</componentName>
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<weightPercent uom="%">0.64</weightPercent>
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<fluidSampleComposition>
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<fluidSampleComposition>
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<fluidSampleComposition>
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\ No newline at end of file
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<DocumentDate>2012-03-04T00:00:00.0Z</DocumentDate>
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<documentClass namingSystem="ERH">dpr2</documentClass>
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<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>2012-02-28</date>
<dateEnd>2012-02-28</dateEnd>
<month>2012-02</month>
<year>2012</year>
<reportVersion>2.0</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_wellTest">
<nameWell>3/7-A-1</nameWell>
<name>Injection well test for well 3/7-A-1</name>
<wellContext>
<field namingSystem="NPD">TRYM</field>
</wellContext>
<testDate>2012-02-28T00:00:00.0Z</testDate>
<previousTestDate>2012-02-10T00:00:00.0Z</previousTestDate>
<lastValidTest>2012-02-23T00:00:00.0Z</lastValidTest>
<testReason>other</testReason>
<testType>combined test</testType>
<standardTempPres>0 degC 1 atm</standardTempPres>
<fluidLevelTest>
<fluidLevel uom="m">135.03</fluidLevel>
<baseUsableWater uom="m">135.03</baseUsableWater>
<testedBy>Presumably, the desc</testedBy>
</fluidLevelTest>
</object>
<object xsi:type="obj_wellTest">
<nameWell>3/7-A-1</nameWell>
<name>Injection well test for well 3/7-A-1</name>
<wellContext>
<field namingSystem="NPD">TRYM</field>
</wellContext>
<testDate>2012-02-28T00:00:00.0Z</testDate>
<previousTestDate>2012-02-15T00:00:00.0Z</previousTestDate>
<lastValidTest>2012-02-21T00:00:00.0Z</lastValidTest>
<testReason>revision</testReason>
<testType>combined test</testType>
<injectionTest>
<testDuration uom="h">6</testDuration>
<testInterval>
<mdTop uom="m">2697.65</mdTop>
<mdBase uom="m">2767.45</mdBase>
<wellbore>3/7-A-1</wellbore>
<testedFormation>Brent</testedFormation>
<valvePosition uom="ft/m">2750.15</valvePosition>
</testInterval>
<InjectedFluid>gas</InjectedFluid>
<wellTestCumulative>
<cumulativeOil uom="m3">3727.78</cumulativeOil>
<cumulativeGas uom="m3">46490.79</cumulativeGas>
<cumulativeWater uom="m3">2561.8</cumulativeWater>
</wellTestCumulative>
<chokeOrificeSize uom="in/64">78.69</chokeOrificeSize>
<minimumAnnularPressure uom="bar">166.33</minimumAnnularPressure>
<maximumAnnularPressure uom="bar">225.55</maximumAnnularPressure>
<wellheadFlowingPressure uom="bar">74.44</wellheadFlowingPressure>
<wellheadMaximumPressure uom="bar">98.51</wellheadMaximumPressure>
<injectionTestResults>
<oilVolume>
<volumeStdTempPres uom="m3">3725.2</volumeStdTempPres>
<densityStdTempPres uom="kg/m3">785.74</densityStdTempPres>
</oilVolume>
<oilRate>
<fluidRateStdTempPres uom="m3/h">568.89</fluidRateStdTempPres>
</oilRate>
<gasVolume>
<volumeStdTempPres uom="m3">6319.14</volumeStdTempPres>
<densityStdTempPres uom="kg/m3">1.22</densityStdTempPres>
</gasVolume>
<gasRate>
<fluidRateStdTempPres uom="m3/h">3550.3</fluidRateStdTempPres>
</gasRate>
<waterVolume>
<volumeStdTempPres uom="m3">114.5</volumeStdTempPres>
</waterVolume>
<waterRate>
<fluidRateStdTempPres uom="m3/h">123.22</fluidRateStdTempPres>
</waterRate>
</injectionTestResults>
</injectionTest>
</object>
<object xsi:type="obj_wellTest">
<nameWell>3/7-A-1</nameWell>
<name>Production well test for well 3/7-A-1</name>
<wellContext>
<field namingSystem="NPD">TRYM</field>
</wellContext>
<testDate>2012-02-28T00:00:00.0Z</testDate>
<previousTestDate>2012-02-10T00:00:00.0Z</previousTestDate>
<lastValidTest>2012-02-23T00:00:00.0Z</lastValidTest>
<testReason>initial</testReason>
<testType>pressure buildup</testType>
<productionTest>
<testDuration uom="h">5</testDuration>
<bottomholeData>
<bottomholePres uom="bar">129.95</bottomholePres>
<bottomholeTemp uom="degC">107.41</bottomholeTemp>
</bottomholeData>
<separatorData>
<separatorPressure uom="bar">71.29</separatorPressure>
<separatorTemperature uom="degC">54.09</separatorTemperature>
</separatorData>
<operatingMethod>flowing</operatingMethod>
<productionTestResults>
<oilVolume>
<volumeStdTempPres uom="m3">1973.99</volumeStdTempPres>
<volume uom="m3">1993.0</volume>
<densityStdTempPres uom="kg/m3">745.3</densityStdTempPres>
</oilVolume>
<oilRate>
<fluidRate uom="m3/h">553.13</fluidRate>
<fluidRateStdTempPres uom="m3/h">629.01</fluidRateStdTempPres>
</oilRate>
<gasVolume>
<volumeStdTempPres uom="m3">2038.86</volumeStdTempPres>
<volume uom="m3">2037.09</volume>
<densityStdTempPres uom="kg/m3">1.24</densityStdTempPres>
</gasVolume>
<gasRate>
<fluidRate uom="m3/h">2329.36</fluidRate>
<fluidRateStdTempPres uom="m3/h">2107.52</fluidRateStdTempPres>
</gasRate>
<waterVolume>
<volumeStdTempPres uom="m3">2223.27</volumeStdTempPres>
<volume uom="m3">1941.59</volume>
</waterVolume>
<waterRate>
<fluidRate uom="m3/h">2301.54</fluidRate>
<fluidRateStdTempPres uom="m3/h">2181.24</fluidRateStdTempPres>
</waterRate>
<gasOilRatio uom="%">57.9</gasOilRatio>
<basicSedimentAndWater uom="%">2.78</basicSedimentAndWater>
<oilPotential uom="1000m3/d">170.91</oilPotential>
<gasPotential uom="1000m3/d">186.52</gasPotential>
<sandVolume uom="m3">1.23</sandVolume>
</productionTestResults>
</productionTest>
</object>
</objects>
\ No newline at end of file