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David Price
26a4e8f9 1 parent 0c9be1fb

Added smaller test case and put html back to include all sections.

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Showing 2 changed files with 653 additions and 2 deletions
......@@ -80,10 +80,10 @@ WHERE {
<dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:ProductionVolumes" />
<!-- <dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:ProductFlows" /> -->
<dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:ProductFlows" />
/>
<dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:InjectionVolumes" />
<!-- <dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:ProductFlowsInjection" /> -->
<dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:ProductFlowsInjection" />
<dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:ImportVolumes" />
<dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:ProductFlowsImport" />
......
<?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&amp;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&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>1.2</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="flow meter" namingSystem="DONG" uidRef="NaN">MPD5</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>
<flow>
<kind>production</kind>
<qualifier>metered - fiscal</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>
<temp uom="K">42.37</temp>
<pres uom="Pa">49.16</pres>
<absoluteMinPres uom="Pa">88.0</absoluteMinPres>
<portDiff uid="f69e7840-12d9-11e2-9fb0-d067e534860e">
<port uidRef="f69e7841-12d9-11e2-a6f4-d067e534860e">Port 1</port>
<presDiff uom="Pa">87.58</presDiff>
<tempDiff uom="K">57.77</tempDiff>
<chokeSize uom="in/32">48.65</chokeSize>
<chokeRelative uom="%">51.8</chokeRelative>
</portDiff>
<portDiff uid="f69e7842-12d9-11e2-8ef2-d067e534860e">
<port uidRef="f69e7843-12d9-11e2-b996-d067e534860e">Port 2</port>
<presDiff uom="Pa">62.4</presDiff>
<tempDiff uom="K">47.76</tempDiff>
<chokeSize uom="in/32">13.91</chokeSize>
<chokeRelative uom="%">36.32</chokeRelative>
</portDiff>
<mass uom="kg">228.08</mass>
<work uom="MJ">734.51</work>
<efficiency uom="%">82.97</efficiency>
<rvp uom="Pa">495.36</rvp>
<tvp uom="bar">933.07</tvp>
<bsw uom="%">39.55</bsw>
<bswPrevious uom="m3/m3">10.83</bswPrevious>
<densityValue>
<density uom="kg/m3">223.18</density>
<temp uom="K">38.89</temp>
<pres uom="Pa">96.93</pres>
</densityValue>
<density uom="kg/m3">646.61</density>
<densityFlowRate uom="Mg/a">203.95</densityFlowRate>
<densityStd uom="kg/m3">683.08</densityStd>
<concentration uom="ppm">35.23</concentration>
<molecularWeight>91.21</molecularWeight>
<weightPercent uom="%">69.45</weightPercent>
<molePercent uom="%">75.76</molePercent>
<moleAmt uom="kmol">84.87</moleAmt>
<sg uom="Euc">53.08</sg>
<hcDewpoint uom="K">537.34</hcDewpoint>
<waterDewpoint uom="K">809.28</waterDewpoint>
<wobbeIndex uom="J/m3">118.37</wobbeIndex>
<grossCalorificValueStd uom="J/m3">491.47</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">270.17</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">73.17</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">365.74</densityStabilizedCrude>
<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><product>
<kind>gas</kind>
<name namingSystem="TEST89">Test product name 134</name>
<splitFactor>0.35</splitFactor>
<gor uom="Euc">81.81</gor>
<gorMTD uom="m3/m3">30.8</gorMTD>
<waterConcMass uom="%">23.14</waterConcMass>
<waterConcVol uom="ppm">54.55</waterConcVol>
<atmosphere uom="Pa">64.06</atmosphere>
<volumeValue>
<volume status="questionable" uom="m3">155.7</volume>
<grossCalorificValue uom="J/m3">565.14</grossCalorificValue>
<temp uom="K">41.76</temp>
<pres uom="Pa">58.9</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">88.77</volume>
<volumeStd status="bad calibration" uom="m3">48.18</volumeStd>
<flowRate status="bad calibration" uom="m3/s">37.2</flowRate>
<temp uom="K">64.54</temp>
<pres uom="Pa">36.49</pres>
<absoluteMinPres uom="Pa">76.62</absoluteMinPres>
<portDiff uid="f69eed70-12d9-11e2-8d9d-d067e534860e">
<port uidRef="f69eed71-12d9-11e2-9b3f-d067e534860e">Port 1</port>
<presDiff uom="Pa">13.53</presDiff>
<tempDiff uom="K">27.0</tempDiff>
<chokeSize uom="in/32">30.02</chokeSize>
<chokeRelative uom="%">70.1</chokeRelative>
</portDiff>
<portDiff uid="f69eed72-12d9-11e2-b723-d067e534860e">
<port uidRef="f69eed73-12d9-11e2-bfbd-d067e534860e">Port 2</port>
<presDiff uom="Pa">38.76</presDiff>
<tempDiff uom="K">33.56</tempDiff>
<chokeSize uom="in/32">39.89</chokeSize>
<chokeRelative uom="%">33.36</chokeRelative>
</portDiff>
<mass uom="kg">424.13</mass>
<work uom="MJ">471.08</work>
<efficiency uom="%">93.23</efficiency>
<rvp uom="Pa">343.49</rvp>
<tvp uom="bar">629.63</tvp>
<bsw uom="%">99.94</bsw>
<bswPrevious uom="m3/m3">37.07</bswPrevious>
<densityValue>
<density uom="kg/m3">690.34</density>
<temp uom="K">41.0</temp>
<pres uom="Pa">51.18</pres>
</densityValue>
<density uom="kg/m3">38.48</density>
<densityFlowRate uom="Mg/a">182.48</densityFlowRate>
<densityStd uom="kg/m3">586.26</densityStd>
<concentration uom="ppm">55.22</concentration>
<molecularWeight>52.44</molecularWeight>
<weightPercent uom="%">52.12</weightPercent>
<molePercent uom="%">51.16</molePercent>
<moleAmt uom="kmol">12.76</moleAmt>
<sg uom="Euc">74.24</sg>
<hcDewpoint uom="K">925.57</hcDewpoint>
<waterDewpoint uom="K">453.77</waterDewpoint>
<wobbeIndex uom="J/m3">555.38</wobbeIndex>
<grossCalorificValueStd uom="J/m3">840.12</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">461.22</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">449.05</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">159.86</densityStabilizedCrude>
<componentContent uid="f69f1480-12d9-11e2-a165-d067e534860e">
<kind>gas - rich</kind>
<referenceKind>water</referenceKind>
<gor uom="Euc">23.54</gor>
<gorMTD uom="m3/m3">27.09</gorMTD>
<waterConcMass uom="%">18.96</waterConcMass>
<waterConcVol uom="ppm">24.05</waterConcVol>
<atmosphere uom="Pa">79.31</atmosphere>
<volumeValue>
<volume status="sensor failure" uom="m3">842.51</volume>
<grossCalorificValue uom="J/m3">932.26</grossCalorificValue>
<temp uom="K">10.91</temp>
<pres uom="Pa">77.87</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">43.39</volume>
<volumeStd status="bad calibration" uom="m3">95.9</volumeStd>
<flowRate status="bad calibration" uom="m3/s">10.02</flowRate>
<temp uom="K">18.52</temp>
<pres uom="Pa">73.22</pres>
<absoluteMinPres uom="Pa">11.99</absoluteMinPres>
<portDiff uid="f69f1481-12d9-11e2-990a-d067e534860e">
<port uidRef="f69f1482-12d9-11e2-8fc5-d067e534860e">Port 1</port>
<presDiff uom="Pa">70.59</presDiff>
<tempDiff uom="K">42.92</tempDiff>
<chokeSize uom="in/32">36.46</chokeSize>
<chokeRelative uom="%">94.03</chokeRelative>
</portDiff>
<portDiff uid="f69f1483-12d9-11e2-a8e7-d067e534860e">
<port uidRef="f69f1484-12d9-11e2-8bf6-d067e534860e">Port 2</port>
<presDiff uom="Pa">92.91</presDiff>
<tempDiff uom="K">97.58</tempDiff>
<chokeSize uom="in/32">27.32</chokeSize>
<chokeRelative uom="%">82.78</chokeRelative>
</portDiff>
<mass uom="kg">942.65</mass>
<work uom="MJ">880.63</work>
<efficiency uom="%">49.0</efficiency>
<rvp uom="Pa">950.93</rvp>
<tvp uom="bar">883.82</tvp>
<bsw uom="%">34.92</bsw>
<bswPrevious uom="m3/m3">33.45</bswPrevious>
<densityValue>
<density uom="kg/m3">14.99</density>
<temp uom="K">16.89</temp>
<pres uom="Pa">49.56</pres>
</densityValue>
<density uom="kg/m3">56.3</density>
<densityFlowRate uom="Mg/a">187.6</densityFlowRate>
<densityStd uom="kg/m3">223.77</densityStd>
<concentration uom="ppm">99.99</concentration>
<molecularWeight>94.47</molecularWeight>
<weightPercent uom="%">37.43</weightPercent>
<molePercent uom="%">88.11</molePercent>
<moleAmt uom="kmol">20.01</moleAmt>
<sg uom="Euc">71.85</sg>
<hcDewpoint uom="K">33.41</hcDewpoint>
<waterDewpoint uom="K">164.98</waterDewpoint>
<wobbeIndex uom="J/m3">483.69</wobbeIndex>
<grossCalorificValueStd uom="J/m3">532.71</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">908.47</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">376.38</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">170.86</densityStabilizedCrude>
</componentContent>
<period>
<kind>day</kind>
<dateStart>2012-02-28</dateStart>
<dateEnd>2012-02-28</dateEnd>
<gor uom="Euc">83.69</gor>
<gorMTD uom="m3/m3">53.5</gorMTD>
<waterConcMass uom="%">58.37</waterConcMass>
<waterConcVol uom="ppm">67.0</waterConcVol>
<atmosphere uom="Pa">30.13</atmosphere>
<volumeValue>
<volume uom="m3">81.96</volume><temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">50.61</volume>
<volumeStd status="bad calibration" uom="m3">96.63</volumeStd>
<flowRate status="bad calibration" uom="m3/s">60.16</flowRate>
<temp uom="K">45.55</temp>
<pres uom="Pa">12.93</pres>
<absoluteMinPres uom="Pa">51.49</absoluteMinPres>
<mass uom="kg">316.62</mass>
<work uom="kW.h">38.93</work>
<efficiency uom="%">96.08</efficiency>
<rvp uom="kpsi">287.31</rvp>
<tvp uom="bar">591.38</tvp>
<bsw uom="%">50.89</bsw>
<bswPrevious uom="m3/m3">56.04</bswPrevious>
<densityValue>
<density uom="kg/m3">0.5</density>
<temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</densityValue>
<density uom="kg/m3">539.46</density>
<densityFlowRate uom="Mg/a">250.26</densityFlowRate>
<densityStd uom="kg/m3">320.16</densityStd>
<concentration uom="ppm">57.74</concentration>
<molecularWeight>63.04</molecularWeight>
<weightPercent uom="%">24.47</weightPercent>
<molePercent uom="%">65.38</molePercent>
<moleAmt uom="kmol">17.54</moleAmt>
<sg uom="Euc">92.05</sg>
<hcDewpoint uom="K">303.28</hcDewpoint>
<waterDewpoint uom="K">964.34</waterDewpoint>
<wobbeIndex uom="J/m3">956.94</wobbeIndex>
<grossCalorificValueStd uom="J/m3">79.96</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">324.6</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">126.43</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">557.09</densityStabilizedCrude>
</period>
</product><product>
<kind>water</kind>
<name namingSystem="TEST492">Test product name 655</name>
<splitFactor>0.72</splitFactor>
<gor uom="Euc">10.87</gor>
<gorMTD uom="m3/m3">77.14</gorMTD>
<waterConcMass uom="%">55.98</waterConcMass>
<waterConcVol uom="ppm">54.46</waterConcVol>
<atmosphere uom="Pa">37.76</atmosphere>
<volumeValue>
<volume status="bad calibration" uom="m3">992.46</volume>
<grossCalorificValue uom="J/m3">263.11</grossCalorificValue>
<temp uom="K">16.57</temp>
<pres uom="Pa">52.71</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">89.7</volume>
<volumeStd status="bad calibration" uom="m3">66.59</volumeStd>
<flowRate status="bad calibration" uom="m3/s">26.87</flowRate>
<temp uom="K">20.42</temp>
<pres uom="Pa">28.88</pres>
<absoluteMinPres uom="Pa">63.17</absoluteMinPres>
<portDiff uid="f69f3b8f-12d9-11e2-91f0-d067e534860e">
<port uidRef="f69f3b90-12d9-11e2-b43f-d067e534860e">Port 1</port>
<presDiff uom="Pa">90.36</presDiff>
<tempDiff uom="K">64.66</tempDiff>
<chokeSize uom="in/32">71.9</chokeSize>
<chokeRelative uom="%">24.08</chokeRelative>
</portDiff>
<portDiff uid="f69f3b91-12d9-11e2-a8a0-d067e534860e">
<port uidRef="f69f3b92-12d9-11e2-b517-d067e534860e">Port 2</port>
<presDiff uom="Pa">91.32</presDiff>
<tempDiff uom="K">73.49</tempDiff>
<chokeSize uom="in/32">63.36</chokeSize>
<chokeRelative uom="%">26.84</chokeRelative>
</portDiff>
<mass uom="kg">867.38</mass>
<work uom="MJ">871.2</work>
<efficiency uom="%">34.13</efficiency>
<rvp uom="Pa">442.65</rvp>
<tvp uom="bar">238.71</tvp>
<bsw uom="%">12.41</bsw>
<bswPrevious uom="m3/m3">74.68</bswPrevious>
<densityValue>
<density uom="kg/m3">539.95</density>
<temp uom="K">71.73</temp>
<pres uom="Pa">49.76</pres>
</densityValue>
<density uom="kg/m3">41.59</density>
<densityFlowRate uom="Mg/a">153.51</densityFlowRate>
<densityStd uom="kg/m3">598.39</densityStd>
<concentration uom="ppm">21.95</concentration>
<molecularWeight>12.52</molecularWeight>
<weightPercent uom="%">10.43</weightPercent>
<molePercent uom="%">95.49</molePercent>
<moleAmt uom="kmol">56.42</moleAmt>
<sg uom="Euc">74.0</sg>
<hcDewpoint uom="K">801.24</hcDewpoint>
<waterDewpoint uom="K">969.94</waterDewpoint>
<wobbeIndex uom="J/m3">38.9</wobbeIndex>
<grossCalorificValueStd uom="J/m3">981.48</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">515.47</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">697.51</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">980.07</densityStabilizedCrude>
<componentContent uid="f69f629e-12d9-11e2-b238-d067e534860e">
<kind>helium gas</kind>
<referenceKind>C6-</referenceKind>
<gor uom="Euc">68.06</gor>
<gorMTD uom="m3/m3">38.09</gorMTD>
<waterConcMass uom="%">62.31</waterConcMass>
<waterConcVol uom="ppm">50.92</waterConcVol>
<atmosphere uom="Pa">31.94</atmosphere>
<volumeValue>
<volume status="questionable" uom="m3">297.12</volume>
<grossCalorificValue uom="J/m3">213.93</grossCalorificValue>
<temp uom="K">97.33</temp>
<pres uom="Pa">94.81</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">11.66</volume>
<volumeStd status="bad calibration" uom="m3">68.73</volumeStd>
<flowRate status="bad calibration" uom="m3/s">68.35</flowRate>
<temp uom="K">33.24</temp>
<pres uom="Pa">78.61</pres>
<absoluteMinPres uom="Pa">31.57</absoluteMinPres>
<portDiff uid="f69f629f-12d9-11e2-82b6-d067e534860e">
<port uidRef="f69f62a0-12d9-11e2-babf-d067e534860e">Port 1</port>
<presDiff uom="Pa">63.63</presDiff>
<tempDiff uom="K">77.25</tempDiff>
<chokeSize uom="in/32">54.35</chokeSize>
<chokeRelative uom="%">51.92</chokeRelative>
</portDiff>
<portDiff uid="f69f62a1-12d9-11e2-8e0f-d067e534860e">
<port uidRef="f69f62a2-12d9-11e2-a28a-d067e534860e">Port 2</port>
<presDiff uom="Pa">85.92</presDiff>
<tempDiff uom="K">44.32</tempDiff>
<chokeSize uom="in/32">98.99</chokeSize>
<chokeRelative uom="%">16.74</chokeRelative>
</portDiff>
<mass uom="kg">301.51</mass>
<work uom="MJ">557.83</work>
<efficiency uom="%">50.41</efficiency>
<rvp uom="Pa">199.92</rvp>
<tvp uom="bar">729.42</tvp>
<bsw uom="%">92.07</bsw>
<bswPrevious uom="m3/m3">54.9</bswPrevious>
<densityValue>
<density uom="kg/m3">186.65</density>
<temp uom="K">52.69</temp>
<pres uom="Pa">92.63</pres>
</densityValue>
<density uom="kg/m3">253.61</density>
<densityFlowRate uom="Mg/a">643.56</densityFlowRate>
<densityStd uom="kg/m3">122.83</densityStd>
<concentration uom="ppm">79.95</concentration>
<molecularWeight>13.99</molecularWeight>
<weightPercent uom="%">49.41</weightPercent>
<molePercent uom="%">97.73</molePercent>
<moleAmt uom="kmol">18.81</moleAmt>
<sg uom="Euc">87.28</sg>
<hcDewpoint uom="K">446.11</hcDewpoint>
<waterDewpoint uom="K">265.29</waterDewpoint>
<wobbeIndex uom="J/m3">35.13</wobbeIndex>
<grossCalorificValueStd uom="J/m3">939.76</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">811.94</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">432.27</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">200.32</densityStabilizedCrude>
</componentContent>
<period>
<kind>day</kind>
<dateStart>2012-02-28</dateStart>
<dateEnd>2012-02-28</dateEnd>
<gor uom="Euc">14.18</gor>
<gorMTD uom="m3/m3">69.09</gorMTD>
<waterConcMass uom="%">10.12</waterConcMass>
<waterConcVol uom="ppm">33.84</waterConcVol>
<atmosphere uom="Pa">97.44</atmosphere>
<volumeValue>
<volume uom="m3">93.62</volume><temp uom="degC">15</temp>
<pres uom="atm">1</pres>
</volumeValue>
<volume status="bad calibration" uom="m3">43.01</volume>
<volumeStd status="bad calibration" uom="m3">73.07</volumeStd>
<flowRate status="bad calibration" uom="m3/s">93.19</flowRate>
<temp uom="K">58.9</temp>
<pres uom="Pa">60.81</pres>
<absoluteMinPres uom="Pa">88.81</absoluteMinPres>
<work uom="MJ">772.09</work>
<efficiency uom="%">40.88</efficiency>
<rvp uom="kpsi">504.32</rvp>
<tvp uom="bar">481.8</tvp>
<bsw uom="%">35.78</bsw>
<bswPrevious uom="m3/m3">99.21</bswPrevious>
<density uom="kg/m3">221.11</density>
<densityFlowRate uom="Mg/a">128.23</densityFlowRate>
<densityStd uom="kg/m3">54.54</densityStd>
<concentration uom="ppm">24.08</concentration>
<molecularWeight>43.89</molecularWeight>
<weightPercent uom="%">54.36</weightPercent>
<molePercent uom="%">90.16</molePercent>
<moleAmt uom="kmol">32.38</moleAmt>
<sg uom="Euc">64.29</sg>
<hcDewpoint uom="K">27.64</hcDewpoint>
<waterDewpoint uom="K">112.08</waterDewpoint>
<wobbeIndex uom="J/m3">272.03</wobbeIndex>
<grossCalorificValueStd uom="J/m3">823.1</grossCalorificValueStd>
<rvpStabilizedCrude uom="Pa">101.55</rvpStabilizedCrude>
<bswStabilizedCrude uom="Euc">168.24</bswStabilizedCrude>
<densityStabilizedCrude uom="kg/m3">450.74</densityStabilizedCrude>
</period>
</product>
</flow>
</facility>
</object>
</objects>
\ No newline at end of file