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David Price
5a74ed94 1 parent fe2ecb1f

Added mprp subset test cases

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1 +<?xml version="1.0" encoding="UTF-8"?>
2 +<objects xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance"
3 + xmlns="http://www.epim.no/schemas/mprml/1" version="1.0(MPRML)">
4 + <documentInfo>
5 + <DocumentName namingSystem="EC">ÅSGARD February 2012</DocumentName>
6 + <DocumentAlias namingSystem="EC">ÅSGARD Copex Report</DocumentAlias>
7 + <DocumentDate>2012-03-05T00:00:00.0Z</DocumentDate>
8 + <documentClass namingSystem="EC">Statoil Petroleum AS</documentClass>
9 + <documentClass namingSystem="EC">Copex</documentClass>
10 + <documentClass namingSystem="ERH">mprp</documentClass>
11 + <FileCreationInformation>
12 +
13 + <FileCreationDate>2012-03-15T00:00:00.0Z</FileCreationDate>
14 +
15 + <SoftwareName>Energy Components</SoftwareName>
16 + <FileCreator>Statoil Petroleum AS</FileCreator>
17 + <Comment>NA</Comment>
18 + </FileCreationInformation>
19 + <Owner>Statoil Petroleum AS</Owner>
20 + </documentInfo>
21 + <context xsi:type="obj_report">
22 + <kind>Copex</kind>
23 +
24 + <title>ÅSGARD</title>
25 + <date>2012-02-01</date>
26 + <dateEnd>2012-02-29</dateEnd>
27 + <month>2012-02</month>
28 + <year>2012</year>
29 + <reportVersion>2.0</reportVersion>
30 + <reportStatus>final</reportStatus>
31 + <installation kind="field" namingSystem="NPD" uidRef="43765">ÅSGARD</installation>
32 + <operator>
33 + <name>Statoil Petroleum AS</name>
34 + <role>Operating company</role>
35 + </operator>
36 + </context>
37 + <object xsi:type="obj_fluidSample">
38 + <name>ÅSGARD-LIQUID-CHARACTERISTICS-1</name>
39 + <sampleType>separator oil</sampleType>
40 + <facility kind="field" namingSystem="NPD" uidRef="43765">ÅSGARD</facility>
41 + <acquisitionDate>2012-01-14</acquisitionDate>
42 + <customData>
43 + <extensionNameValue>
44 + <name>ValidFrom</name>
45 + <value>2012-01-14T00:00:00.0Z</value>
46 + <dataType>dateTime</dataType>
47 + </extensionNameValue>
48 + <extensionNameValue>
49 + <name>ValidTo</name>
50 + <value>2012-01-25T00:00:00.0Z</value>
51 + <dataType>dateTime</dataType>
52 + </extensionNameValue>
53 + </customData>
54 + </object>
55 + <object xsi:type="obj_fluidSample">
56 + <name>ÅSGARD-GAS-CHARACTERISTICS-1</name>
57 + <sampleType>separator gas</sampleType>
58 + <facility kind="field" namingSystem="NPD" uidRef="43765">ÅSGARD</facility>
59 + <acquisitionDate>2012-01-14</acquisitionDate>
60 + <customData>
61 + <extensionNameValue>
62 + <name>ValidFrom</name>
63 + <value>2012-01-14T00:00:00.0Z</value>
64 + <dataType>dateTime</dataType>
65 + </extensionNameValue>
66 + <extensionNameValue>
67 + <name>ValidTo</name>
68 + <value>2012-01-25T00:00:00.0Z</value>
69 + <dataType>dateTime</dataType>
70 + </extensionNameValue>
71 + </customData>
72 + </object>
73 + <object xsi:type="obj_fluidAnalysisResult">
74 + <nameFluidSample>ÅSGARD-LIQUID-CHARACTERISTICS-1</nameFluidSample>
75 + <name>ÅSGARD liquid characteristics</name>
76 + <fluidSampleComposition>
77 + <isPrimary>true</isPrimary>
78 + <componentName>C7+</componentName>
79 + <componentKind>frac</componentKind>
80 + <molecularWeight>21.340</molecularWeight>
81 + <specificGravity>0.716</specificGravity>
82 + <rvp uom="bar">231</rvp>
83 + </fluidSampleComposition>
84 + <fluidSampleComposition>
85 + <isPrimary>false</isPrimary>
86 + <componentName>C1</componentName>
87 + <componentKind>frac</componentKind>
88 + <weightPercent uom="%">0.1</weightPercent>
89 + <molePercent uom="%">0.1</molePercent>
90 + </fluidSampleComposition>
91 + <fluidSampleComposition>
92 + <isPrimary>false</isPrimary>
93 + <componentName>C2</componentName>
94 + <componentKind>frac</componentKind>
95 + <weightPercent uom="%">0.4</weightPercent>
96 + <molePercent uom="%">0.4</molePercent>
97 + </fluidSampleComposition>
98 + <fluidSampleComposition>
99 + <isPrimary>false</isPrimary>
100 + <componentName>C3</componentName>
101 + <componentKind>frac</componentKind>
102 + <weightPercent uom="%">0.64</weightPercent>
103 + <molePercent uom="%">0.64</molePercent>
104 + </fluidSampleComposition>
105 + <fluidSampleComposition>
106 + <isPrimary>false</isPrimary>
107 + <componentName>C6+</componentName>
108 + <componentKind>frac</componentKind>
109 + <weightPercent uom="%">2.5</weightPercent>
110 + <molePercent uom="%">2.5</molePercent>
111 + </fluidSampleComposition>
112 + <fluidSampleComposition>
113 + <isPrimary>false</isPrimary>
114 + <componentName>CO2</componentName>
115 + <componentKind>frac</componentKind>
116 + <weightPercent uom="%">1.000</weightPercent>
117 + <molePercent uom="%">1.000</molePercent>
118 + </fluidSampleComposition>
119 + <fluidSampleComposition>
120 + <isPrimary>false</isPrimary>
121 + <componentName>IC4</componentName>
122 + <componentKind>frac</componentKind>
123 + <weightPercent uom="%">1.460</weightPercent>
124 + <molePercent uom="%">1.460</molePercent>
125 + </fluidSampleComposition>
126 + <fluidSampleComposition>
127 + <isPrimary>false</isPrimary>
128 + <componentName>IC5</componentName>
129 + <componentKind>frac</componentKind>
130 + <weightPercent uom="%">6.000</weightPercent>
131 + <molePercent uom="%">6.000</molePercent>
132 + </fluidSampleComposition>
133 + <fluidSampleComposition>
134 + <isPrimary>false</isPrimary>
135 + <componentName>N2</componentName>
136 + <componentKind>frac</componentKind>
137 + <weightPercent uom="%">1.9000</weightPercent>
138 + <molePercent uom="%">1.9000</molePercent>
139 + </fluidSampleComposition>
140 + <fluidSampleComposition>
141 + <isPrimary>false</isPrimary>
142 + <componentName>NC4</componentName>
143 + <componentKind>frac</componentKind>
144 + <weightPercent uom="%">4.0000</weightPercent>
145 + <molePercent uom="%">4.0000</molePercent>
146 + </fluidSampleComposition>
147 + <fluidSampleComposition>
148 + <isPrimary>false</isPrimary>
149 + <componentName>NC5</componentName>
150 + <componentKind>frac</componentKind>
151 + <weightPercent uom="%">82.0000</weightPercent>
152 + <molePercent uom="%">82.0000</molePercent>
153 + </fluidSampleComposition>
154 + </object>
155 + <object xsi:type="obj_fluidAnalysisResult">
156 + <nameFluidSample>ÅSGARD-GAS-CHARACTERISTICS-1</nameFluidSample>
157 + <name>ÅSGARD gas characteristics</name>
158 + <fluidSampleComposition>
159 + <isPrimary>true</isPrimary>
160 + <componentName>gas</componentName>
161 + <componentKind>frac</componentKind>
162 + <molecularWeight>21.340</molecularWeight>
163 + <specificGravity>0.716</specificGravity>
164 + </fluidSampleComposition>
165 + <fluidSampleComposition>
166 + <isPrimary>false</isPrimary>
167 + <componentName>C1</componentName>
168 + <componentKind>frac</componentKind>
169 + <weightPercent uom="%">0.1</weightPercent>
170 + <molePercent uom="%">0.1</molePercent>
171 + </fluidSampleComposition>
172 + <fluidSampleComposition>
173 + <isPrimary>false</isPrimary>
174 + <componentName>C2</componentName>
175 + <componentKind>frac</componentKind>
176 + <weightPercent uom="%">0.4</weightPercent>
177 + <molePercent uom="%">0.4</molePercent>
178 + </fluidSampleComposition>
179 + <fluidSampleComposition>
180 + <isPrimary>false</isPrimary>
181 + <componentName>C3</componentName>
182 + <componentKind>frac</componentKind>
183 + <weightPercent uom="%">0.64</weightPercent>
184 + <molePercent uom="%">0.64</molePercent>
185 + </fluidSampleComposition>
186 + <fluidSampleComposition>
187 + <isPrimary>false</isPrimary>
188 + <componentName>C6+</componentName>
189 + <componentKind>frac</componentKind>
190 + <weightPercent uom="%">2.5</weightPercent>
191 + <molePercent uom="%">2.5</molePercent>
192 + </fluidSampleComposition>
193 + <fluidSampleComposition>
194 + <isPrimary>false</isPrimary>
195 + <componentName>CO2</componentName>
196 + <componentKind>frac</componentKind>
197 + <weightPercent uom="%">1.000</weightPercent>
198 + <molePercent uom="%">1.000</molePercent>
199 + </fluidSampleComposition>
200 + <fluidSampleComposition>
201 + <isPrimary>false</isPrimary>
202 + <componentName>IC4</componentName>
203 + <componentKind>frac</componentKind>
204 + <weightPercent uom="%">1.460</weightPercent>
205 + <molePercent uom="%">1.460</molePercent>
206 + </fluidSampleComposition>
207 + <fluidSampleComposition>
208 + <isPrimary>false</isPrimary>
209 + <componentName>IC5</componentName>
210 + <componentKind>frac</componentKind>
211 + <weightPercent uom="%">6.000</weightPercent>
212 + <molePercent uom="%">6.000</molePercent>
213 + </fluidSampleComposition>
214 + <fluidSampleComposition>
215 + <isPrimary>false</isPrimary>
216 + <componentName>N2</componentName>
217 + <componentKind>frac</componentKind>
218 + <weightPercent uom="%">1.9000</weightPercent>
219 + <molePercent uom="%">1.9000</molePercent>
220 + </fluidSampleComposition>
221 + <fluidSampleComposition>
222 + <isPrimary>false</isPrimary>
223 + <componentName>NC4</componentName>
224 + <componentKind>frac</componentKind>
225 + <weightPercent uom="%">4.0000</weightPercent>
226 + <molePercent uom="%">4.0000</molePercent>
227 + </fluidSampleComposition>
228 + <fluidSampleComposition>
229 + <isPrimary>false</isPrimary>
230 + <componentName>NC5</componentName>
231 + <componentKind>frac</componentKind>
232 + <weightPercent uom="%">82.0000</weightPercent>
233 + <molePercent uom="%">82.0000</molePercent>
234 + </fluidSampleComposition>
235 + </object>
236 +</objects>
...\ No newline at end of file ...\ No newline at end of file
1 +<?xml version="1.0" encoding="UTF-8"?>
2 +<objects xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance"
3 + xmlns="http://www.epim.no/schemas/mprml/1" version="1.0(MPRML)">
4 + <documentInfo>
5 + <DocumentName namingSystem="EC">ÅSGARD February 2012</DocumentName>
6 + <DocumentAlias namingSystem="EC">ÅSGARD Copex Report</DocumentAlias>
7 + <DocumentDate>2012-03-05T00:00:00.0Z</DocumentDate>
8 + <documentClass namingSystem="EC">Statoil Petroleum AS</documentClass>
9 + <documentClass namingSystem="EC">Copex</documentClass>
10 + <documentClass namingSystem="ERH">mprp</documentClass>
11 + <FileCreationInformation>
12 +
13 + <FileCreationDate>2012-03-15T00:00:00.0Z</FileCreationDate>
14 +
15 + <SoftwareName>Energy Components</SoftwareName>
16 + <FileCreator>Statoil Petroleum AS</FileCreator>
17 + <Comment>NA</Comment>
18 + </FileCreationInformation>
19 + <Owner>Statoil Petroleum AS</Owner>
20 + </documentInfo>
21 + <context xsi:type="obj_report">
22 + <kind>Copex</kind>
23 +
24 + <title>ÅSGARD</title>
25 + <date>2012-02-01</date>
26 + <dateEnd>2012-02-29</dateEnd>
27 + <month>2012-02</month>
28 + <year>2012</year>
29 + <reportVersion>2.0</reportVersion>
30 + <reportStatus>final</reportStatus>
31 + <installation kind="field" namingSystem="NPD" uidRef="43765">ÅSGARD</installation>
32 + <operator>
33 + <name>Statoil Petroleum AS</name>
34 + <role>Operating company</role>
35 + </operator>
36 + </context>
37 + <object xsi:type="obj_wellTest">
38 + <nameWell>6407/2-Z-3 H</nameWell>
39 + <name>Injection well test for well 6407/2-Z-3 H</name>
40 + <wellContext>
41 + <field namingSystem="NPD">ÅSGARD</field>
42 + </wellContext>
43 + <testDate>2012-02-01T00:00:00.0Z</testDate>
44 + <previousTestDate>2012-01-17T00:00:00.0Z</previousTestDate>
45 + <lastValidTest>2012-01-31T00:00:00.0Z</lastValidTest>
46 + <testReason>other</testReason>
47 + <testType>Gas - flow after flow</testType>
48 + <standardTempPres>0 degC 1 atm</standardTempPres>
49 + <fluidLevelTest>
50 +
51 + <fluidLevel uom="m">101.29</fluidLevel>
52 + <baseUsableWater uom="m">122.96</baseUsableWater>
53 + <testedBy>This suggests that t</testedBy>
54 +
55 + </fluidLevelTest>
56 + </object>
57 + <object xsi:type="obj_wellTest">
58 + <nameWell>6407/2-Z-3 H</nameWell>
59 + <name>Injection well test for well 6407/2-Z-3 H</name>
60 + <wellContext>
61 + <field namingSystem="NPD">ÅSGARD</field>
62 + </wellContext>
63 + <testDate>2012-02-01T00:00:00.0Z</testDate>
64 + <previousTestDate>2012-01-13T00:00:00.0Z</previousTestDate>
65 + <lastValidTest>2012-01-26T00:00:00.0Z</lastValidTest>
66 + <testReason>initial</testReason>
67 + <testType>Max sandfree rate</testType>
68 + <injectionTest>
69 + <testDuration uom="h">3</testDuration>
70 + <testInterval>
71 + <mdTop uom="m">2517.21</mdTop>
72 + <mdBase uom="m">2715.18</mdBase>
73 + <wellbore>6407/2-Z-3 H</wellbore>
74 + <testedFormation>Brent</testedFormation>
75 + <valvePosition uom="ft/m">2716.95</valvePosition>
76 + </testInterval>
77 + <InjectedFluid>water</InjectedFluid>
78 + <wellTestCumulative>
79 + <cumulativeOil uom="m3">3579.44</cumulativeOil>
80 + <cumulativeGas uom="m3">48655.3</cumulativeGas>
81 + <cumulativeWater uom="m3">1427.6</cumulativeWater>
82 + </wellTestCumulative>
83 + <chokeOrificeSize uom="in/64">57.7</chokeOrificeSize>
84 + <minimumAnnularPressure uom="bar">178.7</minimumAnnularPressure>
85 + <maximumAnnularPressure uom="bar">234.64</maximumAnnularPressure>
86 + <wellheadFlowingPressure uom="bar">78.88</wellheadFlowingPressure>
87 + <wellheadMaximumPressure uom="bar">122.94</wellheadMaximumPressure>
88 + <injectionTestResults>
89 + <oilVolume>
90 + <volumeStdTempPres uom="m3">3662.56</volumeStdTempPres>
91 + <densityStdTempPres uom="kg/m3">768.57</densityStdTempPres>
92 + </oilVolume>
93 + <oilRate>
94 + <fluidRateStdTempPres uom="m3/h">648.63</fluidRateStdTempPres>
95 + </oilRate>
96 + <gasVolume>
97 + <volumeStdTempPres uom="m3">6604.51</volumeStdTempPres>
98 + <densityStdTempPres uom="kg/m3">1.93</densityStdTempPres>
99 + </gasVolume>
100 + <gasRate>
101 + <fluidRateStdTempPres uom="m3/h">3591.99</fluidRateStdTempPres>
102 + </gasRate>
103 + <waterVolume>
104 + <volumeStdTempPres uom="m3">199.38</volumeStdTempPres>
105 + </waterVolume>
106 + <waterRate>
107 + <fluidRateStdTempPres uom="m3/h">129.94</fluidRateStdTempPres>
108 + </waterRate>
109 + </injectionTestResults>
110 + </injectionTest>
111 + </object>
112 + <object xsi:type="obj_wellTest">
113 + <nameWell>6407/2-Z-3 H</nameWell>
114 + <name>Production well test for well 6407/2-Z-3 H</name>
115 + <wellContext>
116 + <field namingSystem="NPD">ÅSGARD</field>
117 + </wellContext>
118 + <testDate>2012-02-01T00:00:00.0Z</testDate>
119 + <previousTestDate>2012-01-16T00:00:00.0Z</previousTestDate>
120 + <lastValidTest>2012-01-30T00:00:00.0Z</lastValidTest>
121 + <testReason>periodic</testReason>
122 + <testType>Oil - flow after flow</testType>
123 + <productionTest>
124 + <testDuration uom="h">10</testDuration>
125 + <bottomholeData>
126 + <bottomholePres uom="bar">143.16</bottomholePres>
127 + <bottomholeTemp uom="degC">107.27</bottomholeTemp>
128 + </bottomholeData>
129 + <separatorData>
130 + <separatorPressure uom="bar">71.83</separatorPressure>
131 + <separatorTemperature uom="degC">37.03</separatorTemperature>
132 + </separatorData>
133 + <operatingMethod>pumping</operatingMethod>
134 + <productionTestResults>
135 + <oilVolume>
136 + <volumeStdTempPres uom="m3">2345.49</volumeStdTempPres>
137 + <volume uom="m3">2227.98</volume>
138 + <densityStdTempPres uom="kg/m3">723.77</densityStdTempPres>
139 + </oilVolume>
140 + <oilRate>
141 + <fluidRate uom="m3/h">532.38</fluidRate>
142 + <fluidRateStdTempPres uom="m3/h">681.37</fluidRateStdTempPres>
143 + </oilRate>
144 + <gasVolume>
145 + <volumeStdTempPres uom="m3">2042.84</volumeStdTempPres>
146 + <volume uom="m3">2366.18</volume>
147 + <densityStdTempPres uom="kg/m3">1.29</densityStdTempPres>
148 + </gasVolume>
149 + <gasRate>
150 + <fluidRate uom="m3/h">2293.39</fluidRate>
151 + <fluidRateStdTempPres uom="m3/h">1933.77</fluidRateStdTempPres>
152 + </gasRate>
153 + <waterVolume>
154 + <volumeStdTempPres uom="m3">2146.85</volumeStdTempPres>
155 + <volume uom="m3">2481.26</volume>
156 + </waterVolume>
157 + <waterRate>
158 + <fluidRate uom="m3/h">1953.56</fluidRate>
159 + <fluidRateStdTempPres uom="m3/h">2402.76</fluidRateStdTempPres>
160 + </waterRate>
161 + <gasOilRatio uom="%">46.6</gasOilRatio>
162 + <basicSedimentAndWater uom="%">4.7</basicSedimentAndWater>
163 + <oilPotential uom="1000m3/d">108.46</oilPotential>
164 + <gasPotential uom="1000m3/d">148.95</gasPotential>
165 + <sandVolume uom="m3">1.4</sandVolume>
166 + </productionTestResults>
167 + </productionTest>
168 + </object><object xsi:type="obj_wellTest">
169 + <nameWell>6506/11-E-3 H</nameWell>
170 + <name>Injection well test for well 6506/11-E-3 H</name>
171 + <wellContext>
172 + <field namingSystem="NPD">ÅSGARD</field>
173 + </wellContext>
174 + <testDate>2012-02-01T00:00:00.0Z</testDate>
175 + <previousTestDate>2012-01-17T00:00:00.0Z</previousTestDate>
176 + <lastValidTest>2012-01-30T00:00:00.0Z</lastValidTest>
177 + <testReason>other</testReason>
178 + <testType>Gas - flow after flow</testType>
179 + <standardTempPres>0 degC 1 atm</standardTempPres>
180 + <fluidLevelTest>
181 +
182 + <fluidLevel uom="m">160.42</fluidLevel>
183 + <baseUsableWater uom="m">135.87</baseUsableWater>
184 + <testedBy>For one thing, a cas</testedBy>
185 +
186 + </fluidLevelTest>
187 + </object>
188 + <object xsi:type="obj_wellTest">
189 + <nameWell>6506/11-E-3 H</nameWell>
190 + <name>Injection well test for well 6506/11-E-3 H</name>
191 + <wellContext>
192 + <field namingSystem="NPD">ÅSGARD</field>
193 + </wellContext>
194 + <testDate>2012-02-01T00:00:00.0Z</testDate>
195 + <previousTestDate>2012-01-19T00:00:00.0Z</previousTestDate>
196 + <lastValidTest>2012-01-23T00:00:00.0Z</lastValidTest>
197 + <testReason>initial</testReason>
198 + <testType>Max sandfree rate</testType>
199 + <injectionTest>
200 + <testDuration uom="h">13</testDuration>
201 + <testInterval>
202 + <mdTop uom="m">2558.03</mdTop>
203 + <mdBase uom="m">2678.69</mdBase>
204 + <wellbore>6506/11-E-3 H</wellbore>
205 + <testedFormation>Brent</testedFormation>
206 + <valvePosition uom="ft/m">2739.76</valvePosition>
207 + </testInterval>
208 + <InjectedFluid>CO2</InjectedFluid>
209 + <wellTestCumulative>
210 + <cumulativeOil uom="m3">3595.22</cumulativeOil>
211 + <cumulativeGas uom="m3">45556.05</cumulativeGas>
212 + <cumulativeWater uom="m3">1852.62</cumulativeWater>
213 + </wellTestCumulative>
214 + <chokeOrificeSize uom="in/64">80.45</chokeOrificeSize>
215 + <minimumAnnularPressure uom="bar">192.25</minimumAnnularPressure>
216 + <maximumAnnularPressure uom="bar">237.74</maximumAnnularPressure>
217 + <wellheadFlowingPressure uom="bar">89.76</wellheadFlowingPressure>
218 + <wellheadMaximumPressure uom="bar">120.85</wellheadMaximumPressure>
219 + <injectionTestResults>
220 + <oilVolume>
221 + <volumeStdTempPres uom="m3">3641.03</volumeStdTempPres>
222 + <densityStdTempPres uom="kg/m3">779.63</densityStdTempPres>
223 + </oilVolume>
224 + <oilRate>
225 + <fluidRateStdTempPres uom="m3/h">544.26</fluidRateStdTempPres>
226 + </oilRate>
227 + <gasVolume>
228 + <volumeStdTempPres uom="m3">6580.12</volumeStdTempPres>
229 + <densityStdTempPres uom="kg/m3">1.67</densityStdTempPres>
230 + </gasVolume>
231 + <gasRate>
232 + <fluidRateStdTempPres uom="m3/h">3660.31</fluidRateStdTempPres>
233 + </gasRate>
234 + <waterVolume>
235 + <volumeStdTempPres uom="m3">162.87</volumeStdTempPres>
236 + </waterVolume>
237 + <waterRate>
238 + <fluidRateStdTempPres uom="m3/h">117.13</fluidRateStdTempPres>
239 + </waterRate>
240 + </injectionTestResults>
241 + </injectionTest>
242 + </object>
243 + <object xsi:type="obj_wellTest">
244 + <nameWell>6506/11-E-3 H</nameWell>
245 + <name>Production well test for well 6506/11-E-3 H</name>
246 + <wellContext>
247 + <field namingSystem="NPD">ÅSGARD</field>
248 + </wellContext>
249 + <testDate>2012-02-01T00:00:00.0Z</testDate>
250 + <previousTestDate>2012-01-18T00:00:00.0Z</previousTestDate>
251 + <lastValidTest>2012-01-31T00:00:00.0Z</lastValidTest>
252 + <testReason>revision</testReason>
253 + <testType>Gas - flow after flow</testType>
254 + <productionTest>
255 + <testDuration uom="h">12</testDuration>
256 + <bottomholeData>
257 + <bottomholePres uom="bar">128.84</bottomholePres>
258 + <bottomholeTemp uom="degC">102.9</bottomholeTemp>
259 + </bottomholeData>
260 + <separatorData>
261 + <separatorPressure uom="bar">54.38</separatorPressure>
262 + <separatorTemperature uom="degC">37.16</separatorTemperature>
263 + </separatorData>
264 + <operatingMethod>flowing</operatingMethod>
265 + <productionTestResults>
266 + <oilVolume>
267 + <volumeStdTempPres uom="m3">2495.51</volumeStdTempPres>
268 + <volume uom="m3">2053.18</volume>
269 + <densityStdTempPres uom="kg/m3">757.79</densityStdTempPres>
270 + </oilVolume>
271 + <oilRate>
272 + <fluidRate uom="m3/h">539.86</fluidRate>
273 + <fluidRateStdTempPres uom="m3/h">644.94</fluidRateStdTempPres>
274 + </oilRate>
275 + <gasVolume>
276 + <volumeStdTempPres uom="m3">2182.7</volumeStdTempPres>
277 + <volume uom="m3">1949.7</volume>
278 + <densityStdTempPres uom="kg/m3">1.58</densityStdTempPres>
279 + </gasVolume>
280 + <gasRate>
281 + <fluidRate uom="m3/h">2179.25</fluidRate>
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...\ No newline at end of file ...\ No newline at end of file
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...\ No newline at end of file ...\ No newline at end of file