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1 | -<?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> | ||
2 | - <DocumentName namingSystem="EC">ÅSGARD March 2012</DocumentName> | ||
3 | - <DocumentAlias namingSystem="EC">ÅSGARD Copex Report</DocumentAlias> | ||
4 | - <DocumentDate>2012-03-06T00:00:00.0Z</DocumentDate> | ||
5 | - <documentClass namingSystem="EC">Statoil Petroleum AS</documentClass> | ||
6 | - <documentClass namingSystem="EC">DPR 2.0</documentClass> | ||
7 | - <documentClass namingSystem="ERH">dpr2</documentClass><FileCreationInformation> | ||
8 | - | ||
9 | - <FileCreationDate>2012-03-16T00:00:00.0Z</FileCreationDate> | ||
10 | - | ||
11 | - <SoftwareName>Energy Components</SoftwareName> | ||
12 | - <FileCreator>Statoil Petroleum AS</FileCreator> | ||
13 | - <Comment>NA</Comment> | ||
14 | - </FileCreationInformation> | ||
15 | - <Owner>Statoil Petroleum AS</Owner> | ||
16 | - </documentInfo><context xsi:type="obj_report"> | ||
17 | - <kind>DPR 2.0</kind> | ||
18 | - | ||
19 | - <title>ÅSGARD</title> | ||
20 | - <date>2012-03-01</date> | ||
21 | - <dateEnd>2012-03-01</dateEnd> | ||
22 | - <month>2012-03</month> | ||
23 | - <year>2012</year> | ||
24 | - <reportVersion>1.2</reportVersion> | ||
25 | - <reportStatus>final</reportStatus> | ||
26 | - <installation kind="field" namingSystem="NPD" uidRef="43765">ÅSGARD</installation> | ||
27 | - <operator> | ||
28 | - <name>Statoil Petroleum AS</name> | ||
29 | - <role>Operating company</role> | ||
30 | - </operator> | ||
31 | - </context><object xsi:type="obj_productionOperation"> | ||
32 | - <name>ÅSGARD operation report</name> | ||
33 | - <installation kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</installation> | ||
34 | - <periodKind>day</periodKind> | ||
35 | - <dTimStart>2012-03-01T00:00:00.0Z</dTimStart> | ||
36 | - <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd> | ||
37 | - <operator> | ||
38 | - <name>Statoil Petroleum AS</name> | ||
39 | - <role>Operator</role> | ||
40 | - <personName> | ||
41 | - <prefix>Mr</prefix> | ||
42 | - <first>Test</first> | ||
43 | - <last>Dong</last> | ||
44 | - </personName> | ||
45 | - <address> | ||
46 | - <name>Statoil Petroleum AS</name> | ||
47 | - <street>Rosenberggate 99</street> | ||
48 | - <city>Stavanger</city> | ||
49 | - <country>Norway</country> | ||
50 | - <postalCode>4002</postalCode> | ||
51 | - </address> | ||
52 | - </operator> | ||
53 | - <title>ÅSGARD operation report</title> | ||
54 | - <geographicContext> | ||
55 | - <country>Norway</country> | ||
56 | - <field namingSystem="DONG">ÅSGARD</field> | ||
57 | - | ||
58 | - </geographicContext> | ||
59 | - <issueDate>2012-03-02</issueDate> | ||
60 | - <issuedBy> | ||
61 | - <name>Statoil Petroleum AS</name> | ||
62 | - <role>Operator</role> | ||
63 | - <personName> | ||
64 | - <prefix>Mr</prefix> | ||
65 | - <first>Test</first> | ||
66 | - <last>Dong</last> | ||
67 | - </personName> | ||
68 | - </issuedBy> | ||
69 | - <approvalDate>2012-03-02</approvalDate> | ||
70 | - <approver> | ||
71 | - <name>Statoil Petroleum AS</name> | ||
72 | - <role>Platformssjef</role> | ||
73 | - <personName> | ||
74 | - <prefix>Mr</prefix> | ||
75 | - <first>Test</first> | ||
76 | - <last>Dong</last> | ||
77 | - </personName> | ||
78 | - </approver> | ||
79 | - <installationReport uid="b13e8911-f359-11e1-a8ee-d067e534860e"> | ||
80 | - <installation kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</installation> | ||
81 | - <bedsAvailable>10</bedsAvailable> | ||
82 | - <crewCount type="catering crew">1</crewCount> | ||
83 | - <crewCount type="contractor crew">4</crewCount> | ||
84 | - <crewCount type="own crew">5</crewCount> | ||
85 | - <work uom="h">23</work> | ||
86 | - <workMonthToDate uom="d">15</workMonthToDate> | ||
87 | - <workYearToDate uom="d">67</workYearToDate> | ||
88 | - <operationalHSE> | ||
89 | - <IncidentCount>1</IncidentCount> | ||
90 | - <sinceLostTime uom="d">10</sinceLostTime> | ||
91 | - <sincePreventionExercise uom="d">21</sincePreventionExercise> | ||
92 | - <sinceDefinedSituation uom="d">4</sinceDefinedSituation> | ||
93 | - <alarmCount>0</alarmCount> | ||
94 | - <safetyIntroCount>0</safetyIntroCount> | ||
95 | - <safetyDescription>It must be emphasized, once ag</safetyDescription> | ||
96 | - <safety> | ||
97 | - <meantimeIncident uom="d">0</meantimeIncident> | ||
98 | - <safetyCount period="day" type="lost time incident">1</safetyCount> | ||
99 | - <safetyCount period="day" type="sick on board">1</safetyCount> | ||
100 | - <comment> | ||
101 | - <dTimStart>2012-03-01T00:00:00.0Z</dTimStart> | ||
102 | - <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd> | ||
103 | - <remark>Furthermore, an important property of these three types of EC is not to be considered in determining</remark> | ||
104 | - </comment> | ||
105 | - </safety> | ||
106 | - <weather> | ||
107 | - <dTim>2012-03-01T00:00:00.0Z</dTim> | ||
108 | - <agency>Weather agency</agency> | ||
109 | - <barometricPressure uom="Pa">58.32</barometricPressure> | ||
110 | - <beaufortScaleNumber>10</beaufortScaleNumber> | ||
111 | - <tempSurfaceMn uom="degC">15</tempSurfaceMn> | ||
112 | - <tempSurfaceMx uom="degC">19</tempSurfaceMx> | ||
113 | - <tempWindChill uom="degC">19</tempWindChill> | ||
114 | - <tempsea uom="degC">13</tempsea> | ||
115 | - <visibility uom="m">638</visibility> | ||
116 | - <aziWave uom="rad">1</aziWave> | ||
117 | - <htWave uom="m">5</htWave> | ||
118 | - <significantWave uom="m">3</significantWave> | ||
119 | - <maxWave uom="m">7</maxWave> | ||
120 | - <periodWave uom="s">6</periodWave> | ||
121 | - <aziWind uom="rad">4</aziWind> | ||
122 | - <velWind uom="m/s">6</velWind> | ||
123 | - <typePrecip>rain</typePrecip> | ||
124 | - <amtPrecip uom="m">5</amtPrecip> | ||
125 | - <coverCloud>459</coverCloud> | ||
126 | - <ceilingCloud uom="m">178</ceilingCloud> | ||
127 | - <currentSea uom="m/s">1</currentSea> | ||
128 | - <aziCurrentSea uom="rad">1</aziCurrentSea> | ||
129 | - <comments>For one thing, the appearance of parasitic gaps in domains relatively inaccessible to ordinary extra</comments> | ||
130 | - </weather> | ||
131 | - | ||
132 | - </operationalHSE> | ||
133 | - | ||
134 | - <productionActivity> | ||
135 | - <lostProduction> | ||
136 | - <volumeAndReason reasonLost="extended maint turnaround export" uom="m3">1515.91</volumeAndReason> | ||
137 | - <volumeAndReason reasonLost="extended maint turnaround" uom="m3">1407.18</volumeAndReason> | ||
138 | - <thirdPartyProcessing> | ||
139 | - <installation kind="platform">Ekofisk</installation> | ||
140 | - <oilStdTempPres uom="m3">1246.33</oilStdTempPres> | ||
141 | - <gasStdTempPres uom="m3">1897.53</gasStdTempPres> | ||
142 | - </thirdPartyProcessing> | ||
143 | - | ||
144 | - </lostProduction> | ||
145 | - <waterCleaningQuality> | ||
146 | - <samplePoint>Sample 1</samplePoint> | ||
147 | - <oilInWaterProduced uom="Euc">195.36</oilInWaterProduced> | ||
148 | - <amountOfOil uom="kg">109.73</amountOfOil> | ||
149 | - <ammonium uom="kg/m3">4.31</ammonium> | ||
150 | - <totalOrganicCarbon uom="Euc">91.2</totalOrganicCarbon> | ||
151 | - <phenol uom="kg/m3">95.62</phenol> | ||
152 | - <glycol uom="kg/m3">49.54</glycol> | ||
153 | - <phValue>6.17</phValue> | ||
154 | - <waterTemperature uom="degC">10.87</waterTemperature> | ||
155 | - <residualChloride uom="Euc">168.63</residualChloride> | ||
156 | - <oxygen uom="Euc">37.37</oxygen> | ||
157 | - <turbidity>118.69</turbidity> | ||
158 | - <coulterCounter uom="Euc">51.55</coulterCounter> | ||
159 | - | ||
160 | - <comment> | ||
161 | - <dTimStart>2012-03-01T00:00:00.0Z</dTimStart> | ||
162 | - <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd> | ||
163 | - <remark>If the position of the trace in (99c) were only relatively inaccessible to movement, this selectiona</remark> | ||
164 | - </comment> | ||
165 | - </waterCleaningQuality> | ||
166 | - <shutdown> | ||
167 | - <installation kind="well">String</installation> | ||
168 | - <description>Preventive maintenance</description> | ||
169 | - <dTimStart>2012-03-01T00:00:00.0Z</dTimStart> | ||
170 | - <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd> | ||
171 | - <volumetricDownTime uom="h">22</volumetricDownTime> | ||
172 | - <lossOilStdTempPres uom="m3">973.87</lossOilStdTempPres> | ||
173 | - <lossGasStdTempPres uom="m3">7360.4</lossGasStdTempPres> | ||
174 | - <activity> | ||
175 | - <dTimStart>2012-03-01T00:00:00.0Z</dTimStart> | ||
176 | - <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd> | ||
177 | - <remark>It appears that the speaker-hearer's linguistic intuition cannot be arbitrary in the ultimate standa</remark> | ||
178 | - </activity> | ||
179 | - | ||
180 | - </shutdown> | ||
181 | - | ||
182 | - <alarm> | ||
183 | - <dTim>2012-03-01T00:00:00.0Z</dTim> | ||
184 | - <area>Area A</area> | ||
185 | - <type>Gas Alarm</type> | ||
186 | - <reason>Faulty alarm</reason> | ||
187 | - <comment>Nevertheless, the descriptive power of the base component raises serious doubts about a corpus of ut</comment> | ||
188 | - </alarm> | ||
189 | - | ||
190 | - <marineOperation> | ||
191 | - <dTimStart>2012-03-01T00:00:00.0Z</dTimStart> | ||
192 | - <dTimEnd>2012-03-01T02:00:00.0Z</dTimEnd> | ||
193 | - <generalComment>Clearly, a descriptively adequate grammar is not quite equivalent to a general convention regarding </generalComment> | ||
194 | - <supplyShip>Supply 1</supplyShip> | ||
195 | - <standbyVessel>Standby 1</standbyVessel> | ||
196 | - <supplyShipComment> | ||
197 | - | ||
198 | - <dTimStart>2012-03-01T01:00:00.0Z</dTimStart> | ||
199 | - <dTimEnd>2012-03-01T06:00:00.0Z</dTimEnd> | ||
200 | - <remark>From C1, it follows that the speaker-hearer's linguistic intuition delimits the requirement that bra</remark> | ||
201 | - </supplyShipComment> | ||
202 | - <supplyShipComment> | ||
203 | - | ||
204 | - <dTimStart>2012-03-01T06:00:00.0Z</dTimStart> | ||
205 | - <dTimEnd>2012-03-01T08:00:00.0Z</dTimEnd> | ||
206 | - <remark>If the position of the trace in (99c) were only relatively inaccessible to movement, most of the met</remark> | ||
207 | - </supplyShipComment> | ||
208 | - | ||
209 | - <standbyVesselComment> | ||
210 | - <dTimStart>2012-03-01T00:00:00.0Z</dTimStart> | ||
211 | - <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd> | ||
212 | - <remark>I suggested that these results would follow from the assumption that the theory of syntactic feature</remark> | ||
213 | - </standbyVesselComment> | ||
214 | - | ||
215 | - <basketMovement> | ||
216 | - <dTimStart>2012-03-01T00:00:00.0Z</dTimStart> | ||
217 | - <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd> | ||
218 | - <remark>With this clarification, this selectionally introduced contextual feature raises serious doubts abou</remark> | ||
219 | - </basketMovement> | ||
220 | - <basketMovement> | ||
221 | - <dTimStart>2012-03-01T02:00:00.0Z</dTimStart> | ||
222 | - <dTimEnd>2012-03-01T04:00:00.0Z</dTimEnd> | ||
223 | - <remark>Notice, incidentally, that relational information delimits the extended c-command discussed in conne</remark> | ||
224 | - </basketMovement> | ||
225 | - <activity> | ||
226 | - <dTimStart>2012-03-01T06:00:00.0Z</dTimStart> | ||
227 | - <dTimEnd>2012-03-01T08:00:00.0Z</dTimEnd> | ||
228 | - <remark>I suggested that these results would follow from the assumption that the notion of level of grammati</remark> | ||
229 | - </activity> | ||
230 | - <activity> | ||
231 | - <dTimStart>2012-03-01T09:00:00.0Z</dTimStart> | ||
232 | - <dTimEnd>2012-03-01T11:00:00.0Z</dTimEnd> | ||
233 | - <remark>However, this assumption is not correct, since the descriptive power of the base component is necess</remark> | ||
234 | - </activity> | ||
235 | - </marineOperation> | ||
236 | - | ||
237 | - <cargoShipOperation> | ||
238 | - <vesselName>Cargo 1</vesselName> | ||
239 | - <dTimStart>2012-03-01T00:00:00.0Z</dTimStart> | ||
240 | - <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd> | ||
241 | - <captain>Captain 1</captain> | ||
242 | - <cargo>Oil</cargo> | ||
243 | - <oilGrossStdTempPres uom="m3">6349.63</oilGrossStdTempPres> | ||
244 | - <oilGrossTotalStdTempPres uom="m3">6383.1</oilGrossTotalStdTempPres> | ||
245 | - <oilNetStdTempPres uom="m3">9682.53</oilNetStdTempPres> | ||
246 | - <oilNetMonthToDateStdTempPres uom="m3">6330.86</oilNetMonthToDateStdTempPres> | ||
247 | - <densityStdTempPres uom="kg/m3">720.98</densityStdTempPres> | ||
248 | - | ||
249 | - <rvp uom="Pa">167.33</rvp> | ||
250 | - <bsw uom="Euc">119.96</bsw> | ||
251 | - <salt uom="kg/m3">181.07</salt> | ||
252 | - <comment> | ||
253 | - <dTimStart>2012-03-01T00:00:00.0Z</dTimStart> | ||
254 | - <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd> | ||
255 | - <remark>We will bring evidence in favor of the following thesis: relational information suffices to account </remark> | ||
256 | - </comment> | ||
257 | - <comment> | ||
258 | - <dTimStart>2012-03-01T01:00:00.0Z</dTimStart> | ||
259 | - <dTimEnd>2012-03-01T02:00:00.0Z</dTimEnd> | ||
260 | - <remark>I suggested that these results would follow from the assumption that the speaker-hearer's linguistic</remark> | ||
261 | - </comment> | ||
262 | - </cargoShipOperation> | ||
263 | - <operationalComment> | ||
264 | - <type>production</type> | ||
265 | - <dTimStart>2012-03-01T00:00:00.0Z</dTimStart> | ||
266 | - <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd> | ||
267 | - <comment>To provide a constituent structure for T(Z,K), the speaker-hearer's linguistic intuition is rather d</comment> | ||
268 | - </operationalComment> | ||
269 | - <operationalComment> | ||
270 | - <type>production</type> | ||
271 | - <dTimStart>2012-03-01T06:00:00.0Z</dTimStart> | ||
272 | - <dTimEnd>2012-03-01T12:00:00.0Z</dTimEnd> | ||
273 | - <comment>From C1, it follows that the fundamental error of regarding functional notions as categorial appears</comment> | ||
274 | - </operationalComment> | ||
275 | - </productionActivity> | ||
276 | - </installationReport> | ||
277 | -</object><object xsi:type="obj_fluidSample"> | ||
278 | - <name>TYRIHANS-LIQUID-CHARACTERISTICS-1</name> | ||
279 | - <sampleType>separator oil</sampleType> | ||
280 | - <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility> | ||
281 | - <acquisitionDate>2012-02-12</acquisitionDate> | ||
282 | - <customData> | ||
283 | - <extensionNameValue> | ||
284 | - <name>ValidFrom</name> | ||
285 | - <value>2012-02-12T00:00:00.0Z</value> | ||
286 | - <dataType>dateTime</dataType> | ||
287 | - </extensionNameValue> | ||
288 | - <extensionNameValue> | ||
289 | - <name>ValidTo</name> | ||
290 | - <value>2012-02-21T00:00:00.0Z</value> | ||
291 | - <dataType>dateTime</dataType> | ||
292 | - </extensionNameValue> | ||
293 | - </customData> | ||
294 | - </object><object xsi:type="obj_fluidSample"> | ||
295 | - <name>TYRIHANS-GAS-CHARACTERISTICS-1</name> | ||
296 | - <sampleType>separator gas</sampleType> | ||
297 | - <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility> | ||
298 | - <acquisitionDate>2012-02-11</acquisitionDate> | ||
299 | - <customData> | ||
300 | - <extensionNameValue> | ||
301 | - <name>ValidFrom</name> | ||
302 | - <value>2012-02-11T00:00:00.0Z</value> | ||
303 | - <dataType>dateTime</dataType> | ||
304 | - </extensionNameValue> | ||
305 | - <extensionNameValue> | ||
306 | - <name>ValidTo</name> | ||
307 | - <value>2012-02-21T00:00:00.0Z</value> | ||
308 | - <dataType>dateTime</dataType> | ||
309 | - </extensionNameValue> | ||
310 | - </customData> | ||
311 | - </object><object xsi:type="obj_fluidSample"> | ||
312 | - <name>TYRIHANS-LIQUID-CHARACTERISTICS-2</name> | ||
313 | - <sampleType>separator oil</sampleType> | ||
314 | - <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility> | ||
315 | - <acquisitionDate>2012-02-11</acquisitionDate> | ||
316 | - <customData> | ||
317 | - <extensionNameValue> | ||
318 | - <name>ValidFrom</name> | ||
319 | - <value>2012-02-11T00:00:00.0Z</value> | ||
320 | - <dataType>dateTime</dataType> | ||
321 | - </extensionNameValue> | ||
322 | - <extensionNameValue> | ||
323 | - <name>ValidTo</name> | ||
324 | - <value>2012-02-24T00:00:00.0Z</value> | ||
325 | - <dataType>dateTime</dataType> | ||
326 | - </extensionNameValue> | ||
327 | - </customData> | ||
328 | - </object><object xsi:type="obj_fluidSample"> | ||
329 | - <name>TYRIHANS-GAS-CHARACTERISTICS-2</name> | ||
330 | - <sampleType>separator gas</sampleType> | ||
331 | - <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility> | ||
332 | - <acquisitionDate>2012-02-15</acquisitionDate> | ||
333 | - <customData> | ||
334 | - <extensionNameValue> | ||
335 | - <name>ValidFrom</name> | ||
336 | - <value>2012-02-15T00:00:00.0Z</value> | ||
337 | - <dataType>dateTime</dataType> | ||
338 | - </extensionNameValue> | ||
339 | - <extensionNameValue> | ||
340 | - <name>ValidTo</name> | ||
341 | - <value>2012-02-28T00:00:00.0Z</value> | ||
342 | - <dataType>dateTime</dataType> | ||
343 | - </extensionNameValue> | ||
344 | - </customData> | ||
345 | - </object><object xsi:type="obj_fluidSample"> | ||
346 | - <name>TYRIHANS-LIQUID-CHARACTERISTICS-3</name> | ||
347 | - <sampleType>separator oil</sampleType> | ||
348 | - <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility> | ||
349 | - <acquisitionDate>2012-02-12</acquisitionDate> | ||
350 | - <customData> | ||
351 | - <extensionNameValue> | ||
352 | - <name>ValidFrom</name> | ||
353 | - <value>2012-02-12T00:00:00.0Z</value> | ||
354 | - <dataType>dateTime</dataType> | ||
355 | - </extensionNameValue> | ||
356 | - <extensionNameValue> | ||
357 | - <name>ValidTo</name> | ||
358 | - <value>2012-02-23T00:00:00.0Z</value> | ||
359 | - <dataType>dateTime</dataType> | ||
360 | - </extensionNameValue> | ||
361 | - </customData> | ||
362 | - </object><object xsi:type="obj_fluidSample"> | ||
363 | - <name>TYRIHANS-GAS-CHARACTERISTICS-3</name> | ||
364 | - <sampleType>separator gas</sampleType> | ||
365 | - <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility> | ||
366 | - <acquisitionDate>2012-02-12</acquisitionDate> | ||
367 | - <customData> | ||
368 | - <extensionNameValue> | ||
369 | - <name>ValidFrom</name> | ||
370 | - <value>2012-02-12T00:00:00.0Z</value> | ||
371 | - <dataType>dateTime</dataType> | ||
372 | - </extensionNameValue> | ||
373 | - <extensionNameValue> | ||
374 | - <name>ValidTo</name> | ||
375 | - <value>2012-02-22T00:00:00.0Z</value> | ||
376 | - <dataType>dateTime</dataType> | ||
377 | - </extensionNameValue> | ||
378 | - </customData> | ||
379 | - </object><object xsi:type="obj_fluidSample"> | ||
380 | - <name>TYRIHANS-LIQUID-CHARACTERISTICS-1</name> | ||
381 | - <sampleType>separator oil</sampleType> | ||
382 | - <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility> | ||
383 | - <acquisitionDate>2012-02-13</acquisitionDate> | ||
384 | - <customData> | ||
385 | - <extensionNameValue> | ||
386 | - <name>ValidFrom</name> | ||
387 | - <value>2012-02-13T00:00:00.0Z</value> | ||
388 | - <dataType>dateTime</dataType> | ||
389 | - </extensionNameValue> | ||
390 | - <extensionNameValue> | ||
391 | - <name>ValidTo</name> | ||
392 | - <value>2012-02-24T00:00:00.0Z</value> | ||
393 | - <dataType>dateTime</dataType> | ||
394 | - </extensionNameValue> | ||
395 | - </customData> | ||
396 | - </object><object xsi:type="obj_fluidSample"> | ||
397 | - <name>TYRIHANS-GAS-CHARACTERISTICS-1</name> | ||
398 | - <sampleType>separator gas</sampleType> | ||
399 | - <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility> | ||
400 | - <acquisitionDate>2012-02-14</acquisitionDate> | ||
401 | - <customData> | ||
402 | - <extensionNameValue> | ||
403 | - <name>ValidFrom</name> | ||
404 | - <value>2012-02-14T00:00:00.0Z</value> | ||
405 | - <dataType>dateTime</dataType> | ||
406 | - </extensionNameValue> | ||
407 | - <extensionNameValue> | ||
408 | - <name>ValidTo</name> | ||
409 | - <value>2012-02-26T00:00:00.0Z</value> | ||
410 | - <dataType>dateTime</dataType> | ||
411 | - </extensionNameValue> | ||
412 | - </customData> | ||
413 | - </object><object xsi:type="obj_fluidSample"> | ||
414 | - <name>TYRIHANS-LIQUID-CHARACTERISTICS-2</name> | ||
415 | - <sampleType>separator oil</sampleType> | ||
416 | - <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility> | ||
417 | - <acquisitionDate>2012-02-15</acquisitionDate> | ||
418 | - <customData> | ||
419 | - <extensionNameValue> | ||
420 | - <name>ValidFrom</name> | ||
421 | - <value>2012-02-15T00:00:00.0Z</value> | ||
422 | - <dataType>dateTime</dataType> | ||
423 | - </extensionNameValue> | ||
424 | - <extensionNameValue> | ||
425 | - <name>ValidTo</name> | ||
426 | - <value>2012-02-23T00:00:00.0Z</value> | ||
427 | - <dataType>dateTime</dataType> | ||
428 | - </extensionNameValue> | ||
429 | - </customData> | ||
430 | - </object><object xsi:type="obj_fluidSample"> | ||
431 | - <name>TYRIHANS-GAS-CHARACTERISTICS-2</name> | ||
432 | - <sampleType>separator gas</sampleType> | ||
433 | - <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility> | ||
434 | - <acquisitionDate>2012-02-13</acquisitionDate> | ||
435 | - <customData> | ||
436 | - <extensionNameValue> | ||
437 | - <name>ValidFrom</name> | ||
438 | - <value>2012-02-13T00:00:00.0Z</value> | ||
439 | - <dataType>dateTime</dataType> | ||
440 | - </extensionNameValue> | ||
441 | - <extensionNameValue> | ||
442 | - <name>ValidTo</name> | ||
443 | - <value>2012-02-27T00:00:00.0Z</value> | ||
444 | - <dataType>dateTime</dataType> | ||
445 | - </extensionNameValue> | ||
446 | - </customData> | ||
447 | - </object><object xsi:type="obj_fluidSample"> | ||
448 | - <name>TYRIHANS-LIQUID-CHARACTERISTICS-3</name> | ||
449 | - <sampleType>separator oil</sampleType> | ||
450 | - <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility> | ||
451 | - <acquisitionDate>2012-02-11</acquisitionDate> | ||
452 | - <customData> | ||
453 | - <extensionNameValue> | ||
454 | - <name>ValidFrom</name> | ||
455 | - <value>2012-02-11T00:00:00.0Z</value> | ||
456 | - <dataType>dateTime</dataType> | ||
457 | - </extensionNameValue> | ||
458 | - <extensionNameValue> | ||
459 | - <name>ValidTo</name> | ||
460 | - <value>2012-02-23T00:00:00.0Z</value> | ||
461 | - <dataType>dateTime</dataType> | ||
462 | - </extensionNameValue> | ||
463 | - </customData> | ||
464 | - </object><object xsi:type="obj_fluidSample"> | ||
465 | - <name>TYRIHANS-GAS-CHARACTERISTICS-3</name> | ||
466 | - <sampleType>separator gas</sampleType> | ||
467 | - <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility> | ||
468 | - <acquisitionDate>2012-02-13</acquisitionDate> | ||
469 | - <customData> | ||
470 | - <extensionNameValue> | ||
471 | - <name>ValidFrom</name> | ||
472 | - <value>2012-02-13T00:00:00.0Z</value> | ||
473 | - <dataType>dateTime</dataType> | ||
474 | - </extensionNameValue> | ||
475 | - <extensionNameValue> | ||
476 | - <name>ValidTo</name> | ||
477 | - <value>2012-02-21T00:00:00.0Z</value> | ||
478 | - <dataType>dateTime</dataType> | ||
479 | - </extensionNameValue> | ||
480 | - </customData> | ||
481 | - </object><object xsi:type="obj_fluidSample"> | ||
482 | - <name>TYRIHANS-LIQUID-CHARACTERISTICS-1</name> | ||
483 | - <sampleType>separator oil</sampleType> | ||
484 | - <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility> | ||
485 | - <acquisitionDate>2012-02-13</acquisitionDate> | ||
486 | - <customData> | ||
487 | - <extensionNameValue> | ||
488 | - <name>ValidFrom</name> | ||
489 | - <value>2012-02-13T00:00:00.0Z</value> | ||
490 | - <dataType>dateTime</dataType> | ||
491 | - </extensionNameValue> | ||
492 | - <extensionNameValue> | ||
493 | - <name>ValidTo</name> | ||
494 | - <value>2012-02-24T00:00:00.0Z</value> | ||
495 | - <dataType>dateTime</dataType> | ||
496 | - </extensionNameValue> | ||
497 | - </customData> | ||
498 | - </object><object xsi:type="obj_fluidSample"> | ||
499 | - <name>TYRIHANS-GAS-CHARACTERISTICS-1</name> | ||
500 | - <sampleType>separator gas</sampleType> | ||
501 | - <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility> | ||
502 | - <acquisitionDate>2012-02-13</acquisitionDate> | ||
503 | - <customData> | ||
504 | - <extensionNameValue> | ||
505 | - <name>ValidFrom</name> | ||
506 | - <value>2012-02-13T00:00:00.0Z</value> | ||
507 | - <dataType>dateTime</dataType> | ||
508 | - </extensionNameValue> | ||
509 | - <extensionNameValue> | ||
510 | - <name>ValidTo</name> | ||
511 | - <value>2012-02-27T00:00:00.0Z</value> | ||
512 | - <dataType>dateTime</dataType> | ||
513 | - </extensionNameValue> | ||
514 | - </customData> | ||
515 | - </object><object xsi:type="obj_fluidSample"> | ||
516 | - <name>TYRIHANS-LIQUID-CHARACTERISTICS-2</name> | ||
517 | - <sampleType>separator oil</sampleType> | ||
518 | - <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility> | ||
519 | - <acquisitionDate>2012-02-11</acquisitionDate> | ||
520 | - <customData> | ||
521 | - <extensionNameValue> | ||
522 | - <name>ValidFrom</name> | ||
523 | - <value>2012-02-11T00:00:00.0Z</value> | ||
524 | - <dataType>dateTime</dataType> | ||
525 | - </extensionNameValue> | ||
526 | - <extensionNameValue> | ||
527 | - <name>ValidTo</name> | ||
528 | - <value>2012-02-25T00:00:00.0Z</value> | ||
529 | - <dataType>dateTime</dataType> | ||
530 | - </extensionNameValue> | ||
531 | - </customData> | ||
532 | - </object><object xsi:type="obj_fluidSample"> | ||
533 | - <name>TYRIHANS-GAS-CHARACTERISTICS-2</name> | ||
534 | - <sampleType>separator gas</sampleType> | ||
535 | - <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility> | ||
536 | - <acquisitionDate>2012-02-15</acquisitionDate> | ||
537 | - <customData> | ||
538 | - <extensionNameValue> | ||
539 | - <name>ValidFrom</name> | ||
540 | - <value>2012-02-15T00:00:00.0Z</value> | ||
541 | - <dataType>dateTime</dataType> | ||
542 | - </extensionNameValue> | ||
543 | - <extensionNameValue> | ||
544 | - <name>ValidTo</name> | ||
545 | - <value>2012-02-26T00:00:00.0Z</value> | ||
546 | - <dataType>dateTime</dataType> | ||
547 | - </extensionNameValue> | ||
548 | - </customData> | ||
549 | - </object><object xsi:type="obj_fluidSample"> | ||
550 | - <name>TYRIHANS-LIQUID-CHARACTERISTICS-3</name> | ||
551 | - <sampleType>separator oil</sampleType> | ||
552 | - <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility> | ||
553 | - <acquisitionDate>2012-02-14</acquisitionDate> | ||
554 | - <customData> | ||
555 | - <extensionNameValue> | ||
556 | - <name>ValidFrom</name> | ||
557 | - <value>2012-02-14T00:00:00.0Z</value> | ||
558 | - <dataType>dateTime</dataType> | ||
559 | - </extensionNameValue> | ||
560 | - <extensionNameValue> | ||
561 | - <name>ValidTo</name> | ||
562 | - <value>2012-02-22T00:00:00.0Z</value> | ||
563 | - <dataType>dateTime</dataType> | ||
564 | - </extensionNameValue> | ||
565 | - </customData> | ||
566 | - </object><object xsi:type="obj_fluidSample"> | ||
567 | - <name>TYRIHANS-GAS-CHARACTERISTICS-3</name> | ||
568 | - <sampleType>separator gas</sampleType> | ||
569 | - <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility> | ||
570 | - <acquisitionDate>2012-02-12</acquisitionDate> | ||
571 | - <customData> | ||
572 | - <extensionNameValue> | ||
573 | - <name>ValidFrom</name> | ||
574 | - <value>2012-02-12T00:00:00.0Z</value> | ||
575 | - <dataType>dateTime</dataType> | ||
576 | - </extensionNameValue> | ||
577 | - <extensionNameValue> | ||
578 | - <name>ValidTo</name> | ||
579 | - <value>2012-02-24T00:00:00.0Z</value> | ||
580 | - <dataType>dateTime</dataType> | ||
581 | - </extensionNameValue> | ||
582 | - </customData> | ||
583 | - </object><object xsi:type="obj_productVolume"> | ||
584 | - <name>TYRIHANS</name> | ||
585 | - <installation kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</installation> | ||
586 | - <facility> | ||
587 | - <name kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</name> | ||
588 | - <facilityParent1 kind="block valve" namingSystem="String" uidRef="x">String</facilityParent1> | ||
589 | - <facilityParent2 kind="block valve" namingSystem="String" uidRef="x">String</facilityParent2> | ||
590 | - <facilityAlias namingSystem="String">String</facilityAlias> | ||
591 | - <facilityAlias namingSystem="String">String</facilityAlias> | ||
592 | - <contextFacility kind="block valve" namingSystem="String" uidRef="x">String</contextFacility> | ||
593 | - <contextFacility kind="block valve" namingSystem="String" uidRef="x">String</contextFacility> | ||
594 | - | ||
595 | - | ||
596 | - <downtimeReason uid="b15b5fde-f359-11e1-a318-d067e534860e"> | ||
597 | - <who>MR Who</who> | ||
598 | - <role>Platform manager</role> | ||
599 | - <dTimStart>2012-03-01T02:00:00.0Z</dTimStart> | ||
600 | - <dTimEnd>2012-03-01T04:00:00.0Z</dTimEnd> | ||
601 | - <remark>Let us continue to suppose that any associated supporting element is unspecified with respect to an </remark> | ||
602 | - </downtimeReason> | ||
603 | - <downtimeReason uid="b15b86ee-f359-11e1-a386-d067e534860e"> | ||
604 | - <who>Mr Who2</who> | ||
605 | - <role>Platform manager 2</role> | ||
606 | - <dTimStart>2012-03-01T06:00:00.0Z</dTimStart> | ||
607 | - <dTimEnd>2012-03-01T14:00:00.0Z</dTimEnd> | ||
608 | - <remark>It appears that the descriptive power of the base component does not readily tolerate an abstract un</remark> | ||
609 | - </downtimeReason> | ||
610 | - <flow> | ||
611 | - <kind>production</kind> | ||
612 | - <qualifier>saleable</qualifier> | ||
613 | - <version>2012-03-01T16:00:00.0Z</version> | ||
614 | - <versionSource>version src 71</versionSource> | ||
615 | - <gor uom="Euc">75.46</gor> | ||
616 | - <gorMTD uom="m3/m3">57.69</gorMTD> | ||
617 | - <waterConcMass uom="%">35.9</waterConcMass> | ||
618 | - <waterConcVol uom="ppm">86.59</waterConcVol> | ||
619 | - <atmosphere uom="Pa">28.71</atmosphere> | ||
620 | - <volumeValue> | ||
621 | - <volume status="bad calibration" uom="m3">834.26</volume> | ||
622 | - <grossCalorificValue uom="J/m3">613.16</grossCalorificValue> | ||
623 | - <temp uom="K">47.11</temp> | ||
624 | - <pres uom="Pa">12.89</pres> | ||
625 | - </volumeValue> | ||
626 | - <volume status="bad calibration" uom="m3">19.72</volume> | ||
627 | - <volumeStd status="bad calibration" uom="m3">89.01</volumeStd> | ||
628 | - <flowRate status="bad calibration" uom="m3/s">71.85</flowRate> | ||
629 | - <temp uom="K">98.42</temp> | ||
630 | - <pres uom="Pa">68.45</pres> | ||
631 | - <absoluteMinPres uom="Pa">29.8</absoluteMinPres> | ||
632 | - <portDiff uid="b15b86ef-f359-11e1-a5d7-d067e534860e"> | ||
633 | - <port uidRef="b15b86f0-f359-11e1-9bf6-d067e534860e">Port 1</port> | ||
634 | - <presDiff uom="Pa">91.4</presDiff> | ||
635 | - <tempDiff uom="K">70.32</tempDiff> | ||
636 | - <chokeSize uom="in/32">68.22</chokeSize> | ||
637 | - <chokeRelative uom="%">95.71</chokeRelative> | ||
638 | - </portDiff> | ||
639 | - <portDiff uid="b15b86f1-f359-11e1-8fc8-d067e534860e"> | ||
640 | - <port uidRef="b15b86f2-f359-11e1-8f01-d067e534860e">Port 2</port> | ||
641 | - <presDiff uom="Pa">97.94</presDiff> | ||
642 | - <tempDiff uom="K">98.68</tempDiff> | ||
643 | - <chokeSize uom="in/32">45.3</chokeSize> | ||
644 | - <chokeRelative uom="%">24.82</chokeRelative> | ||
645 | - </portDiff> | ||
646 | - <mass uom="kg">485.46</mass> | ||
647 | - <work uom="MJ">464.84</work> | ||
648 | - <efficiency uom="%">70.77</efficiency> | ||
649 | - <rvp uom="Pa">262.77</rvp> | ||
650 | - <tvp uom="bar">527.14</tvp> | ||
651 | - <bsw uom="%">80.9</bsw> | ||
652 | - <bswPrevious uom="m3/m3">18.13</bswPrevious> | ||
653 | - <densityValue> | ||
654 | - <density uom="kg/m3">34.68</density> | ||
655 | - <temp uom="K">48.15</temp> | ||
656 | - <pres uom="Pa">36.68</pres> | ||
657 | - </densityValue> | ||
658 | - <density uom="kg/m3">642.61</density> | ||
659 | - <densityFlowRate uom="Mg/a">495.01</densityFlowRate> | ||
660 | - <densityStd uom="kg/m3">303.76</densityStd> | ||
661 | - <concentration uom="ppm">49.74</concentration> | ||
662 | - <molecularWeight>42.55</molecularWeight> | ||
663 | - <weightPercent uom="%">67.96</weightPercent> | ||
664 | - <molePercent uom="%">41.57</molePercent> | ||
665 | - <moleAmt uom="kmol">98.22</moleAmt> | ||
666 | - <sg uom="Euc">87.09</sg> | ||
667 | - <hcDewpoint uom="K">229.53</hcDewpoint> | ||
668 | - <waterDewpoint uom="K">880.59</waterDewpoint> | ||
669 | - <wobbeIndex uom="J/m3">897.79</wobbeIndex> | ||
670 | - <grossCalorificValueStd uom="J/m3">27.92</grossCalorificValueStd> | ||
671 | - <rvpStabilizedCrude uom="Pa">574.9</rvpStabilizedCrude> | ||
672 | - <bswStabilizedCrude uom="Euc">541.59</bswStabilizedCrude> | ||
673 | - <densityStabilizedCrude uom="kg/m3">716.88</densityStabilizedCrude> | ||
674 | - <product> | ||
675 | - <kind>oil - net</kind> | ||
676 | - <name namingSystem="TEST954">Test product name 622</name> | ||
677 | - <splitFactor>0.65</splitFactor> | ||
678 | - <gor uom="Euc">98.73</gor> | ||
679 | - <gorMTD uom="m3/m3">84.85</gorMTD> | ||
680 | - <waterConcMass uom="%">73.24</waterConcMass> | ||
681 | - <waterConcVol uom="ppm">98.74</waterConcVol> | ||
682 | - <atmosphere uom="Pa">58.79</atmosphere> | ||
683 | - <volumeValue> | ||
684 | - <volume status="range limit" uom="m3">880.44</volume> | ||
685 | - <grossCalorificValue uom="J/m3">494.48</grossCalorificValue> | ||
686 | - <temp uom="K">75.73</temp> | ||
687 | - <pres uom="Pa">75.0</pres> | ||
688 | - </volumeValue> | ||
689 | - <volume status="bad calibration" uom="m3">44.97</volume> | ||
690 | - <volumeStd status="bad calibration" uom="m3">92.29</volumeStd> | ||
691 | - <flowRate status="bad calibration" uom="m3/s">62.29</flowRate> | ||
692 | - <temp uom="K">90.95</temp> | ||
693 | - <pres uom="Pa">27.05</pres> | ||
694 | - <absoluteMinPres uom="Pa">99.82</absoluteMinPres> | ||
695 | - <portDiff uid="b15bae00-f359-11e1-8073-d067e534860e"> | ||
696 | - <port uidRef="b15bae01-f359-11e1-8368-d067e534860e">Port 1</port> | ||
697 | - <presDiff uom="Pa">26.55</presDiff> | ||
698 | - <tempDiff uom="K">70.35</tempDiff> | ||
699 | - <chokeSize uom="in/32">47.5</chokeSize> | ||
700 | - <chokeRelative uom="%">68.21</chokeRelative> | ||
701 | - </portDiff> | ||
702 | - <portDiff uid="b15bae02-f359-11e1-96c3-d067e534860e"> | ||
703 | - <port uidRef="b15bae03-f359-11e1-a6c2-d067e534860e">Port 2</port> | ||
704 | - <presDiff uom="Pa">61.59</presDiff> | ||
705 | - <tempDiff uom="K">94.72</tempDiff> | ||
706 | - <chokeSize uom="in/32">75.58</chokeSize> | ||
707 | - <chokeRelative uom="%">44.09</chokeRelative> | ||
708 | - </portDiff> | ||
709 | - <mass uom="kg">388.85</mass> | ||
710 | - <work uom="MJ">154.17</work> | ||
711 | - <efficiency uom="%">70.62</efficiency> | ||
712 | - <rvp uom="Pa">684.1</rvp> | ||
713 | - <tvp uom="bar">419.71</tvp> | ||
714 | - <bsw uom="%">12.38</bsw> | ||
715 | - <bswPrevious uom="m3/m3">40.59</bswPrevious> | ||
716 | - <densityValue> | ||
717 | - <density uom="kg/m3">373.41</density> | ||
718 | - <temp uom="K">36.61</temp> | ||
719 | - <pres uom="Pa">80.1</pres> | ||
720 | - </densityValue> | ||
721 | - <density uom="kg/m3">419.96</density> | ||
722 | - <densityFlowRate uom="Mg/a">472.06</densityFlowRate> | ||
723 | - <densityStd uom="kg/m3">25.67</densityStd> | ||
724 | - <concentration uom="ppm">41.01</concentration> | ||
725 | - <molecularWeight>61.05</molecularWeight> | ||
726 | - <weightPercent uom="%">80.88</weightPercent> | ||
727 | - <molePercent uom="%">55.97</molePercent> | ||
728 | - <moleAmt uom="kmol">34.75</moleAmt> | ||
729 | - <sg uom="Euc">89.59</sg> | ||
730 | - <hcDewpoint uom="K">42.61</hcDewpoint> | ||
731 | - <waterDewpoint uom="K">861.58</waterDewpoint> | ||
732 | - <wobbeIndex uom="J/m3">994.75</wobbeIndex> | ||
733 | - <grossCalorificValueStd uom="J/m3">661.77</grossCalorificValueStd> | ||
734 | - <rvpStabilizedCrude uom="Pa">903.29</rvpStabilizedCrude> | ||
735 | - <bswStabilizedCrude uom="Euc">802.46</bswStabilizedCrude> | ||
736 | - <densityStabilizedCrude uom="kg/m3">732.34</densityStabilizedCrude> | ||
737 | - <componentContent uid="b15bae04-f359-11e1-928c-d067e534860e"> | ||
738 | - <kind>diesel</kind> | ||
739 | - <referenceKind>aqueous</referenceKind> | ||
740 | - <gor uom="Euc">57.74</gor> | ||
741 | - <gorMTD uom="m3/m3">76.27</gorMTD> | ||
742 | - <waterConcMass uom="%">30.42</waterConcMass> | ||
743 | - <waterConcVol uom="ppm">43.48</waterConcVol> | ||
744 | - <atmosphere uom="Pa">17.04</atmosphere> | ||
745 | - <volumeValue> | ||
746 | - <volume status="device failure" uom="m3">825.44</volume> | ||
747 | - <grossCalorificValue uom="J/m3">928.39</grossCalorificValue> | ||
748 | - <temp uom="K">72.1</temp> | ||
749 | - <pres uom="Pa">65.0</pres> | ||
750 | - </volumeValue> | ||
751 | - <volume status="bad calibration" uom="m3">13.92</volume> | ||
752 | - <volumeStd status="bad calibration" uom="m3">30.25</volumeStd> | ||
753 | - <flowRate status="bad calibration" uom="m3/s">40.77</flowRate> | ||
754 | - <temp uom="K">21.06</temp> | ||
755 | - <pres uom="Pa">27.33</pres> | ||
756 | - <absoluteMinPres uom="Pa">17.25</absoluteMinPres> | ||
757 | - <portDiff uid="b15bd50f-f359-11e1-9159-d067e534860e"> | ||
758 | - <port uidRef="b15bd510-f359-11e1-9333-d067e534860e">Port 1</port> | ||
759 | - <presDiff uom="Pa">19.8</presDiff> | ||
760 | - <tempDiff uom="K">24.95</tempDiff> | ||
761 | - <chokeSize uom="in/32">34.22</chokeSize> | ||
762 | - <chokeRelative uom="%">50.23</chokeRelative> | ||
763 | - </portDiff> | ||
764 | - <portDiff uid="b15bd511-f359-11e1-a2ee-d067e534860e"> | ||
765 | - <port uidRef="b15bd512-f359-11e1-b5a7-d067e534860e">Port 2</port> | ||
766 | - <presDiff uom="Pa">25.76</presDiff> | ||
767 | - <tempDiff uom="K">29.53</tempDiff> | ||
768 | - <chokeSize uom="in/32">76.31</chokeSize> | ||
769 | - <chokeRelative uom="%">36.08</chokeRelative> | ||
770 | - </portDiff> | ||
771 | - <mass uom="kg">749.09</mass> | ||
772 | - <work uom="MJ">343.14</work> | ||
773 | - <efficiency uom="%">36.97</efficiency> | ||
774 | - <rvp uom="Pa">677.75</rvp> | ||
775 | - <tvp uom="bar">316.01</tvp> | ||
776 | - <bsw uom="%">82.71</bsw> | ||
777 | - <bswPrevious uom="m3/m3">54.68</bswPrevious> | ||
778 | - <densityValue> | ||
779 | - <density uom="kg/m3">425.32</density> | ||
780 | - <temp uom="K">13.6</temp> | ||
781 | - <pres uom="Pa">45.04</pres> | ||
782 | - </densityValue> | ||
783 | - <density uom="kg/m3">233.23</density> | ||
784 | - <densityFlowRate uom="Mg/a">329.23</densityFlowRate> | ||
785 | - <densityStd uom="kg/m3">487.14</densityStd> | ||
786 | - <concentration uom="ppm">37.94</concentration> | ||
787 | - <molecularWeight>47.64</molecularWeight> | ||
788 | - <weightPercent uom="%">84.25</weightPercent> | ||
789 | - <molePercent uom="%">83.28</molePercent> | ||
790 | - <moleAmt uom="kmol">42.97</moleAmt> | ||
791 | - <sg uom="Euc">41.5</sg> | ||
792 | - <hcDewpoint uom="K">790.71</hcDewpoint> | ||
793 | - <waterDewpoint uom="K">877.18</waterDewpoint> | ||
794 | - <wobbeIndex uom="J/m3">691.74</wobbeIndex> | ||
795 | - <grossCalorificValueStd uom="J/m3">667.72</grossCalorificValueStd> | ||
796 | - <rvpStabilizedCrude uom="Pa">114.98</rvpStabilizedCrude> | ||
797 | - <bswStabilizedCrude uom="Euc">61.25</bswStabilizedCrude> | ||
798 | - <densityStabilizedCrude uom="kg/m3">367.63</densityStabilizedCrude> | ||
799 | - </componentContent> | ||
800 | - <period> | ||
801 | - <kind>day</kind> | ||
802 | - <dateStart>2012-03-01</dateStart> | ||
803 | - <dateEnd>2012-03-01</dateEnd> | ||
804 | - <gor uom="Euc">52.02</gor> | ||
805 | - <gorMTD uom="m3/m3">59.95</gorMTD> | ||
806 | - <waterConcMass uom="%">37.44</waterConcMass> | ||
807 | - <waterConcVol uom="ppm">78.68</waterConcVol> | ||
808 | - <atmosphere uom="Pa">82.5</atmosphere> | ||
809 | - <volumeValue> | ||
810 | - | ||
811 | - <volume uom="m3">2696.85</volume><temp uom="degC">15</temp> | ||
812 | - <pres uom="atm">1</pres> | ||
813 | - </volumeValue> | ||
814 | - <volume status="bad calibration" uom="m3">43.45</volume> | ||
815 | - <volumeStd status="bad calibration" uom="m3">41.94</volumeStd> | ||
816 | - <flowRate status="bad calibration" uom="m3/s">30.44</flowRate> | ||
817 | - <temp uom="K">17.45</temp> | ||
818 | - <pres uom="Pa">60.12</pres> | ||
819 | - <absoluteMinPres uom="Pa">29.16</absoluteMinPres> | ||
820 | - | ||
821 | - <mass uom="kg">259.85</mass> | ||
822 | - <work uom="J">80.56</work> | ||
823 | - <efficiency uom="%">73.47</efficiency> | ||
824 | - <rvp uom="bar">964.46</rvp> | ||
825 | - <tvp uom="bar">759.53</tvp> | ||
826 | - <bsw uom="%">35.01</bsw> | ||
827 | - <bswPrevious uom="m3/m3">19.09</bswPrevious> | ||
828 | - <densityValue> | ||
829 | - | ||
830 | - <density uom="kg/m3">778.74</density> | ||
831 | - <temp uom="degC">15</temp> | ||
832 | - <pres uom="atm">1</pres> | ||
833 | - </densityValue> | ||
834 | - <density uom="kg/m3">637.68</density> | ||
835 | - <densityFlowRate uom="Mg/a">113.92</densityFlowRate> | ||
836 | - <densityStd uom="kg/m3">455.32</densityStd> | ||
837 | - <concentration uom="ppm">78.91</concentration> | ||
838 | - <molecularWeight>19.7</molecularWeight> | ||
839 | - <weightPercent uom="%">79.84</weightPercent> | ||
840 | - <molePercent uom="%">72.58</molePercent> | ||
841 | - <moleAmt uom="kmol">83.36</moleAmt> | ||
842 | - <sg uom="Euc">51.11</sg> | ||
843 | - <hcDewpoint uom="K">664.37</hcDewpoint> | ||
844 | - <waterDewpoint uom="K">105.18</waterDewpoint> | ||
845 | - <wobbeIndex uom="J/m3">847.7</wobbeIndex> | ||
846 | - <grossCalorificValueStd uom="J/m3">427.91</grossCalorificValueStd> | ||
847 | - <rvpStabilizedCrude uom="Pa">273.24</rvpStabilizedCrude> | ||
848 | - <bswStabilizedCrude uom="Euc">744.11</bswStabilizedCrude> | ||
849 | - <densityStabilizedCrude uom="kg/m3">859.26</densityStabilizedCrude> | ||
850 | - </period> | ||
851 | - | ||
852 | - </product> | ||
853 | - </flow> | ||
854 | - | ||
855 | - | ||
856 | - | ||
857 | - <flow> | ||
858 | - <kind>consume - fuel</kind> | ||
859 | - <qualifier>allocated</qualifier> | ||
860 | - <version>2012-03-01T01:00:00.0Z</version> | ||
861 | - <versionSource>version src 623</versionSource> | ||
862 | - <gor uom="Euc">68.83</gor> | ||
863 | - <gorMTD uom="m3/m3">97.3</gorMTD> | ||
864 | - <waterConcMass uom="%">98.72</waterConcMass> | ||
865 | - <waterConcVol uom="ppm">91.68</waterConcVol> | ||
866 | - <atmosphere uom="Pa">27.77</atmosphere> | ||
867 | - <volumeValue> | ||
868 | - <volume status="device failure" uom="m3">80.69</volume> | ||
869 | - <grossCalorificValue uom="J/m3">582.24</grossCalorificValue> | ||
870 | - <temp uom="K">74.63</temp> | ||
871 | - <pres uom="Pa">29.01</pres> | ||
872 | - </volumeValue> | ||
873 | - <volume status="bad calibration" uom="m3">20.84</volume> | ||
874 | - <volumeStd status="bad calibration" uom="m3">45.1</volumeStd> | ||
875 | - <flowRate status="bad calibration" uom="m3/s">48.81</flowRate> | ||
876 | - <temp uom="K">20.51</temp> | ||
877 | - <pres uom="Pa">48.91</pres> | ||
878 | - <absoluteMinPres uom="Pa">94.27</absoluteMinPres> | ||
879 | - <portDiff uid="b15bfc1e-f359-11e1-b6e9-d067e534860e"> | ||
880 | - <port uidRef="b15bfc1f-f359-11e1-b41f-d067e534860e">Port 1</port> | ||
881 | - <presDiff uom="Pa">53.35</presDiff> | ||
882 | - <tempDiff uom="K">35.64</tempDiff> | ||
883 | - <chokeSize uom="in/32">95.67</chokeSize> | ||
884 | - <chokeRelative uom="%">88.74</chokeRelative> | ||
885 | - </portDiff> | ||
886 | - <portDiff uid="b15bfc20-f359-11e1-8833-d067e534860e"> | ||
887 | - <port uidRef="b15bfc21-f359-11e1-86ec-d067e534860e">Port 2</port> | ||
888 | - <presDiff uom="Pa">81.34</presDiff> | ||
889 | - <tempDiff uom="K">79.54</tempDiff> | ||
890 | - <chokeSize uom="in/32">85.86</chokeSize> | ||
891 | - <chokeRelative uom="%">32.62</chokeRelative> | ||
892 | - </portDiff> | ||
893 | - <mass uom="kg">524.18</mass> | ||
894 | - <work uom="MJ">122.33</work> | ||
895 | - <efficiency uom="%">91.84</efficiency> | ||
896 | - <rvp uom="Pa">789.55</rvp> | ||
897 | - <tvp uom="bar">602.6</tvp> | ||
898 | - <bsw uom="%">22.89</bsw> | ||
899 | - <bswPrevious uom="m3/m3">49.54</bswPrevious> | ||
900 | - <densityValue> | ||
901 | - <density uom="kg/m3">506.75</density> | ||
902 | - <temp uom="K">26.87</temp> | ||
903 | - <pres uom="Pa">32.79</pres> | ||
904 | - </densityValue> | ||
905 | - <density uom="kg/m3">344.63</density> | ||
906 | - <densityFlowRate uom="Mg/a">229.21</densityFlowRate> | ||
907 | - <densityStd uom="kg/m3">522.81</densityStd> | ||
908 | - <concentration uom="ppm">72.37</concentration> | ||
909 | - <molecularWeight>52.41</molecularWeight> | ||
910 | - <weightPercent uom="%">67.02</weightPercent> | ||
911 | - <molePercent uom="%">62.95</molePercent> | ||
912 | - <moleAmt uom="kmol">77.62</moleAmt> | ||
913 | - <sg uom="Euc">25.65</sg> | ||
914 | - <hcDewpoint uom="K">339.47</hcDewpoint> | ||
915 | - <waterDewpoint uom="K">383.0</waterDewpoint> | ||
916 | - <wobbeIndex uom="J/m3">324.3</wobbeIndex> | ||
917 | - <grossCalorificValueStd uom="J/m3">913.96</grossCalorificValueStd> | ||
918 | - <rvpStabilizedCrude uom="Pa">237.3</rvpStabilizedCrude> | ||
919 | - <bswStabilizedCrude uom="Euc">289.09</bswStabilizedCrude> | ||
920 | - <densityStabilizedCrude uom="kg/m3">209.51</densityStabilizedCrude> | ||
921 | - <product> | ||
922 | - <kind>diesel</kind> | ||
923 | - <name namingSystem="TEST949">Test product name 536</name> | ||
924 | - <splitFactor>0.11</splitFactor> | ||
925 | - <gor uom="Euc">95.69</gor> | ||
926 | - <gorMTD uom="m3/m3">32.66</gorMTD> | ||
927 | - <waterConcMass uom="%">58.1</waterConcMass> | ||
928 | - <waterConcVol uom="ppm">19.2</waterConcVol> | ||
929 | - <atmosphere uom="Pa">92.1</atmosphere> | ||
930 | - <volumeValue> | ||
931 | - <volume status="range limit" uom="m3">366.3</volume> | ||
932 | - <grossCalorificValue uom="J/m3">570.6</grossCalorificValue> | ||
933 | - <temp uom="K">41.33</temp> | ||
934 | - <pres uom="Pa">50.99</pres> | ||
935 | - </volumeValue> | ||
936 | - <volume status="bad calibration" uom="m3">12.59</volume> | ||
937 | - <volumeStd status="bad calibration" uom="m3">63.05</volumeStd> | ||
938 | - <flowRate status="bad calibration" uom="m3/s">98.13</flowRate> | ||
939 | - <temp uom="K">68.37</temp> | ||
940 | - <pres uom="Pa">23.28</pres> | ||
941 | - <absoluteMinPres uom="Pa">92.22</absoluteMinPres> | ||
942 | - <portDiff uid="b15bfc22-f359-11e1-af66-d067e534860e"> | ||
943 | - <port uidRef="b15bfc23-f359-11e1-b17d-d067e534860e">Port 1</port> | ||
944 | - <presDiff uom="Pa">33.31</presDiff> | ||
945 | - <tempDiff uom="K">84.21</tempDiff> | ||
946 | - <chokeSize uom="in/32">13.44</chokeSize> | ||
947 | - <chokeRelative uom="%">97.63</chokeRelative> | ||
948 | - </portDiff> | ||
949 | - <portDiff uid="b15c2330-f359-11e1-add9-d067e534860e"> | ||
950 | - <port uidRef="b15c2331-f359-11e1-ad46-d067e534860e">Port 2</port> | ||
951 | - <presDiff uom="Pa">75.85</presDiff> | ||
952 | - <tempDiff uom="K">89.75</tempDiff> | ||
953 | - <chokeSize uom="in/32">40.06</chokeSize> | ||
954 | - <chokeRelative uom="%">70.16</chokeRelative> | ||
955 | - </portDiff> | ||
956 | - <mass uom="kg">733.99</mass> | ||
957 | - <work uom="MJ">835.71</work> | ||
958 | - <efficiency uom="%">70.64</efficiency> | ||
959 | - <rvp uom="Pa">675.65</rvp> | ||
960 | - <tvp uom="bar">532.88</tvp> | ||
961 | - <bsw uom="%">38.79</bsw> | ||
962 | - <bswPrevious uom="m3/m3">32.91</bswPrevious> | ||
963 | - <densityValue> | ||
964 | - <density uom="kg/m3">35.09</density> | ||
965 | - <temp uom="K">56.34</temp> | ||
966 | - <pres uom="Pa">76.01</pres> | ||
967 | - </densityValue> | ||
968 | - <density uom="kg/m3">160.37</density> | ||
969 | - <densityFlowRate uom="Mg/a">420.95</densityFlowRate> | ||
970 | - <densityStd uom="kg/m3">548.86</densityStd> | ||
971 | - <concentration uom="ppm">25.46</concentration> | ||
972 | - <molecularWeight>76.55</molecularWeight> | ||
973 | - <weightPercent uom="%">32.03</weightPercent> | ||
974 | - <molePercent uom="%">90.69</molePercent> | ||
975 | - <moleAmt uom="kmol">82.36</moleAmt> | ||
976 | - <sg uom="Euc">22.8</sg> | ||
977 | - <hcDewpoint uom="K">986.14</hcDewpoint> | ||
978 | - <waterDewpoint uom="K">490.97</waterDewpoint> | ||
979 | - <wobbeIndex uom="J/m3">215.6</wobbeIndex> | ||
980 | - <grossCalorificValueStd uom="J/m3">939.64</grossCalorificValueStd> | ||
981 | - <rvpStabilizedCrude uom="Pa">62.37</rvpStabilizedCrude> | ||
982 | - <bswStabilizedCrude uom="Euc">580.57</bswStabilizedCrude> | ||
983 | - <densityStabilizedCrude uom="kg/m3">445.39</densityStabilizedCrude> | ||
984 | - <componentContent uid="b15c2332-f359-11e1-be17-d067e534860e"> | ||
985 | - <kind>C6-</kind> | ||
986 | - <referenceKind>propane</referenceKind> | ||
987 | - <gor uom="Euc">94.3</gor> | ||
988 | - <gorMTD uom="m3/m3">49.21</gorMTD> | ||
989 | - <waterConcMass uom="%">42.65</waterConcMass> | ||
990 | - <waterConcVol uom="ppm">95.55</waterConcVol> | ||
991 | - <atmosphere uom="Pa">98.22</atmosphere> | ||
992 | - <volumeValue> | ||
993 | - <volume status="range limit" uom="m3">872.16</volume> | ||
994 | - <grossCalorificValue uom="J/m3">292.66</grossCalorificValue> | ||
995 | - <temp uom="K">30.17</temp> | ||
996 | - <pres uom="Pa">87.79</pres> | ||
997 | - </volumeValue> | ||
998 | - <volume status="bad calibration" uom="m3">36.67</volume> | ||
999 | - <volumeStd status="bad calibration" uom="m3">83.65</volumeStd> | ||
1000 | - <flowRate status="bad calibration" uom="m3/s">47.6</flowRate> | ||
1001 | - <temp uom="K">59.59</temp> | ||
1002 | - <pres uom="Pa">74.77</pres> | ||
1003 | - <absoluteMinPres uom="Pa">50.9</absoluteMinPres> | ||
1004 | - <portDiff uid="b15c2333-f359-11e1-bf87-d067e534860e"> | ||
1005 | - <port uidRef="b15c2334-f359-11e1-b1b1-d067e534860e">Port 1</port> | ||
1006 | - <presDiff uom="Pa">10.46</presDiff> | ||
1007 | - <tempDiff uom="K">82.76</tempDiff> | ||
1008 | - <chokeSize uom="in/32">15.31</chokeSize> | ||
1009 | - <chokeRelative uom="%">45.42</chokeRelative> | ||
1010 | - </portDiff> | ||
1011 | - <portDiff uid="b15c2335-f359-11e1-8296-d067e534860e"> | ||
1012 | - <port uidRef="b15c2336-f359-11e1-af3c-d067e534860e">Port 2</port> | ||
1013 | - <presDiff uom="Pa">20.64</presDiff> | ||
1014 | - <tempDiff uom="K">24.55</tempDiff> | ||
1015 | - <chokeSize uom="in/32">90.41</chokeSize> | ||
1016 | - <chokeRelative uom="%">13.97</chokeRelative> | ||
1017 | - </portDiff> | ||
1018 | - <mass uom="kg">486.03</mass> | ||
1019 | - <work uom="MJ">667.54</work> | ||
1020 | - <efficiency uom="%">55.01</efficiency> | ||
1021 | - <rvp uom="Pa">539.8</rvp> | ||
1022 | - <tvp uom="bar">983.91</tvp> | ||
1023 | - <bsw uom="%">85.95</bsw> | ||
1024 | - <bswPrevious uom="m3/m3">69.42</bswPrevious> | ||
1025 | - <densityValue> | ||
1026 | - <density uom="kg/m3">83.37</density> | ||
1027 | - <temp uom="K">27.62</temp> | ||
1028 | - <pres uom="Pa">74.95</pres> | ||
1029 | - </densityValue> | ||
1030 | - <density uom="kg/m3">431.44</density> | ||
1031 | - <densityFlowRate uom="Mg/a">462.15</densityFlowRate> | ||
1032 | - <densityStd uom="kg/m3">75.11</densityStd> | ||
1033 | - <concentration uom="ppm">15.2</concentration> | ||
1034 | - <molecularWeight>83.02</molecularWeight> | ||
1035 | - <weightPercent uom="%">28.9</weightPercent> | ||
1036 | - <molePercent uom="%">40.99</molePercent> | ||
1037 | - <moleAmt uom="kmol">18.78</moleAmt> | ||
1038 | - <sg uom="Euc">69.2</sg> | ||
1039 | - <hcDewpoint uom="K">535.24</hcDewpoint> | ||
1040 | - <waterDewpoint uom="K">51.07</waterDewpoint> | ||
1041 | - <wobbeIndex uom="J/m3">514.25</wobbeIndex> | ||
1042 | - <grossCalorificValueStd uom="J/m3">378.36</grossCalorificValueStd> | ||
1043 | - <rvpStabilizedCrude uom="Pa">379.58</rvpStabilizedCrude> | ||
1044 | - <bswStabilizedCrude uom="Euc">832.23</bswStabilizedCrude> | ||
1045 | - <densityStabilizedCrude uom="kg/m3">895.99</densityStabilizedCrude> | ||
1046 | - </componentContent> | ||
1047 | - <period> | ||
1048 | - <kind>day</kind> | ||
1049 | - <dateStart>2012-03-01</dateStart> | ||
1050 | - <dateEnd>2012-03-01</dateEnd> | ||
1051 | - <gor uom="Euc">40.37</gor> | ||
1052 | - <gorMTD uom="m3/m3">63.45</gorMTD> | ||
1053 | - <waterConcMass uom="%">24.23</waterConcMass> | ||
1054 | - <waterConcVol uom="ppm">54.56</waterConcVol> | ||
1055 | - <atmosphere uom="Pa">23.37</atmosphere> | ||
1056 | - | ||
1057 | - <volumeValue> | ||
1058 | - <volume uom="L">249.11</volume> | ||
1059 | - <temp uom="degC">15</temp> | ||
1060 | - <pres uom="atm">1</pres> | ||
1061 | - </volumeValue><volume status="bad calibration" uom="m3">58.75</volume> | ||
1062 | - <volumeStd status="bad calibration" uom="m3">93.65</volumeStd> | ||
1063 | - <flowRate status="bad calibration" uom="m3/s">87.15</flowRate> | ||
1064 | - <temp uom="K">65.52</temp> | ||
1065 | - <pres uom="Pa">53.15</pres> | ||
1066 | - <absoluteMinPres uom="Pa">84.14</absoluteMinPres> | ||
1067 | - | ||
1068 | - | ||
1069 | - <work uom="MJ">234.84</work> | ||
1070 | - <efficiency uom="%">12.61</efficiency> | ||
1071 | - <rvp uom="atm">792.71</rvp> | ||
1072 | - <tvp uom="bar">845.1</tvp> | ||
1073 | - <bsw uom="%">70.53</bsw> | ||
1074 | - <bswPrevious uom="m3/m3">55.6</bswPrevious> | ||
1075 | - | ||
1076 | - <density uom="kg/m3">49.43</density> | ||
1077 | - <densityFlowRate uom="Mg/a">11.75</densityFlowRate> | ||
1078 | - <densityStd uom="kg/m3">442.26</densityStd> | ||
1079 | - <concentration uom="ppm">77.98</concentration> | ||
1080 | - <molecularWeight>51.9</molecularWeight> | ||
1081 | - <weightPercent uom="%">12.04</weightPercent> | ||
1082 | - <molePercent uom="%">89.37</molePercent> | ||
1083 | - <moleAmt uom="kmol">71.28</moleAmt> | ||
1084 | - <sg uom="Euc">76.78</sg> | ||
1085 | - <hcDewpoint uom="K">938.49</hcDewpoint> | ||
1086 | - <waterDewpoint uom="K">424.25</waterDewpoint> | ||
1087 | - <wobbeIndex uom="J/m3">409.88</wobbeIndex> | ||
1088 | - <grossCalorificValueStd uom="J/m3">543.05</grossCalorificValueStd> | ||
1089 | - <rvpStabilizedCrude uom="Pa">375.31</rvpStabilizedCrude> | ||
1090 | - <bswStabilizedCrude uom="Euc">619.48</bswStabilizedCrude> | ||
1091 | - <densityStabilizedCrude uom="kg/m3">857.5</densityStabilizedCrude> | ||
1092 | - </period> | ||
1093 | - | ||
1094 | - </product> | ||
1095 | - </flow> | ||
1096 | - | ||
1097 | - | ||
1098 | - | ||
1099 | - | ||
1100 | - </facility><facility> | ||
1101 | - <name kind="compressor" namingSystem="STATOIL" uidRef="NaN">TYRIHANS compressor</name> | ||
1102 | - <facilityParent1 kind="block valve" namingSystem="String" uidRef="x">String</facilityParent1> | ||
1103 | - <facilityParent2 kind="block valve" namingSystem="String" uidRef="x">String</facilityParent2> | ||
1104 | - <facilityAlias namingSystem="String">String</facilityAlias> | ||
1105 | - <facilityAlias namingSystem="String">String</facilityAlias> | ||
1106 | - <contextFacility kind="block valve" namingSystem="String" uidRef="x">String</contextFacility> | ||
1107 | - <contextFacility kind="block valve" namingSystem="String" uidRef="x">String</contextFacility> | ||
1108 | - | ||
1109 | - | ||
1110 | - | ||
1111 | - <flow> | ||
1112 | - <kind>production</kind> | ||
1113 | - <qualifier>metered - fiscal</qualifier> | ||
1114 | - <version>2012-03-01T11:00:00.0Z</version> | ||
1115 | - <versionSource>version src 707</versionSource> | ||
1116 | - <gor uom="Euc">40.29</gor> | ||
1117 | - <gorMTD uom="m3/m3">58.4</gorMTD> | ||
1118 | - <waterConcMass uom="%">46.58</waterConcMass> | ||
1119 | - <waterConcVol uom="ppm">81.28</waterConcVol> | ||
1120 | - <atmosphere uom="Pa">60.96</atmosphere> | ||
1121 | - <volumeValue> | ||
1122 | - <volume status="device failure" uom="m3">846.9</volume> | ||
1123 | - <grossCalorificValue uom="J/m3">828.79</grossCalorificValue> | ||
1124 | - <temp uom="K">86.07</temp> | ||
1125 | - <pres uom="Pa">52.18</pres> | ||
1126 | - </volumeValue> | ||
1127 | - <volume status="bad calibration" uom="m3">42.06</volume> | ||
1128 | - <volumeStd status="bad calibration" uom="m3">54.54</volumeStd> | ||
1129 | - <flowRate status="bad calibration" uom="m3/s">10.81</flowRate> | ||
1130 | - <temp uom="K">24.9</temp> | ||
1131 | - <pres uom="Pa">56.33</pres> | ||
1132 | - <absoluteMinPres uom="Pa">75.4</absoluteMinPres> | ||
1133 | - <portDiff uid="b15c4a40-f359-11e1-b743-d067e534860e"> | ||
1134 | - <port uidRef="b15c4a41-f359-11e1-9645-d067e534860e">Port 1</port> | ||
1135 | - <presDiff uom="Pa">11.59</presDiff> | ||
1136 | - <tempDiff uom="K">87.23</tempDiff> | ||
1137 | - <chokeSize uom="in/32">22.03</chokeSize> | ||
1138 | - <chokeRelative uom="%">54.32</chokeRelative> | ||
1139 | - </portDiff> | ||
1140 | - <portDiff uid="b15c4a42-f359-11e1-b241-d067e534860e"> | ||
1141 | - <port uidRef="b15c714f-f359-11e1-b6b7-d067e534860e">Port 2</port> | ||
1142 | - <presDiff uom="Pa">88.87</presDiff> | ||
1143 | - <tempDiff uom="K">12.18</tempDiff> | ||
1144 | - <chokeSize uom="in/32">43.28</chokeSize> | ||
1145 | - <chokeRelative uom="%">33.13</chokeRelative> | ||
1146 | - </portDiff> | ||
1147 | - <mass uom="kg">809.05</mass> | ||
1148 | - <work uom="MJ">900.5</work> | ||
1149 | - <efficiency uom="%">65.19</efficiency> | ||
1150 | - <rvp uom="Pa">684.25</rvp> | ||
1151 | - <tvp uom="bar">160.2</tvp> | ||
1152 | - <bsw uom="%">14.44</bsw> | ||
1153 | - <bswPrevious uom="m3/m3">72.93</bswPrevious> | ||
1154 | - <densityValue> | ||
1155 | - <density uom="kg/m3">366.4</density> | ||
1156 | - <temp uom="K">42.15</temp> | ||
1157 | - <pres uom="Pa">48.97</pres> | ||
1158 | - </densityValue> | ||
1159 | - <density uom="kg/m3">110.37</density> | ||
1160 | - <densityFlowRate uom="Mg/a">245.46</densityFlowRate> | ||
1161 | - <densityStd uom="kg/m3">383.66</densityStd> | ||
1162 | - <concentration uom="ppm">59.27</concentration> | ||
1163 | - <molecularWeight>43.35</molecularWeight> | ||
1164 | - <weightPercent uom="%">74.89</weightPercent> | ||
1165 | - <molePercent uom="%">46.25</molePercent> | ||
1166 | - <moleAmt uom="kmol">74.51</moleAmt> | ||
1167 | - <sg uom="Euc">37.67</sg> | ||
1168 | - <hcDewpoint uom="K">553.35</hcDewpoint> | ||
1169 | - <waterDewpoint uom="K">747.77</waterDewpoint> | ||
1170 | - <wobbeIndex uom="J/m3">705.92</wobbeIndex> | ||
1171 | - <grossCalorificValueStd uom="J/m3">560.47</grossCalorificValueStd> | ||
1172 | - <rvpStabilizedCrude uom="Pa">143.03</rvpStabilizedCrude> | ||
1173 | - <bswStabilizedCrude uom="Euc">747.63</bswStabilizedCrude> | ||
1174 | - <densityStabilizedCrude uom="kg/m3">286.01</densityStabilizedCrude> | ||
1175 | - <product> | ||
1176 | - <kind>oil - net</kind> | ||
1177 | - <name namingSystem="TEST604">Test product name 986</name> | ||
1178 | - <splitFactor>0.68</splitFactor> | ||
1179 | - <gor uom="Euc">54.19</gor> | ||
1180 | - <gorMTD uom="m3/m3">82.24</gorMTD> | ||
1181 | - <waterConcMass uom="%">68.88</waterConcMass> | ||
1182 | - <waterConcVol uom="ppm">51.45</waterConcVol> | ||
1183 | - <atmosphere uom="Pa">13.95</atmosphere> | ||
1184 | - <volumeValue> | ||
1185 | - <volume status="sensor failure" uom="m3">593.81</volume> | ||
1186 | - <grossCalorificValue uom="J/m3">175.09</grossCalorificValue> | ||
1187 | - <temp uom="K">35.96</temp> | ||
1188 | - <pres uom="Pa">64.45</pres> | ||
1189 | - </volumeValue> | ||
1190 | - <volume status="bad calibration" uom="m3">37.51</volume> | ||
1191 | - <volumeStd status="bad calibration" uom="m3">15.96</volumeStd> | ||
1192 | - <flowRate status="bad calibration" uom="m3/s">13.5</flowRate> | ||
1193 | - <temp uom="K">87.42</temp> | ||
1194 | - <pres uom="Pa">68.02</pres> | ||
1195 | - <absoluteMinPres uom="Pa">84.66</absoluteMinPres> | ||
1196 | - <portDiff uid="b15c7150-f359-11e1-82e3-d067e534860e"> | ||
1197 | - <port uidRef="b15c7151-f359-11e1-bcb2-d067e534860e">Port 1</port> | ||
1198 | - <presDiff uom="Pa">29.49</presDiff> | ||
1199 | - <tempDiff uom="K">77.67</tempDiff> | ||
1200 | - <chokeSize uom="in/32">30.56</chokeSize> | ||
1201 | - <chokeRelative uom="%">37.53</chokeRelative> | ||
1202 | - </portDiff> | ||
1203 | - <portDiff uid="b15c7152-f359-11e1-a8b9-d067e534860e"> | ||
1204 | - <port uidRef="b15c7153-f359-11e1-81ac-d067e534860e">Port 2</port> | ||
1205 | - <presDiff uom="Pa">42.83</presDiff> | ||
1206 | - <tempDiff uom="K">54.87</tempDiff> | ||
1207 | - <chokeSize uom="in/32">85.52</chokeSize> | ||
1208 | - <chokeRelative uom="%">34.61</chokeRelative> | ||
1209 | - </portDiff> | ||
1210 | - <mass uom="kg">610.56</mass> | ||
1211 | - <work uom="MJ">128.67</work> | ||
1212 | - <efficiency uom="%">39.84</efficiency> | ||
1213 | - <rvp uom="Pa">424.75</rvp> | ||
1214 | - <tvp uom="bar">57.28</tvp> | ||
1215 | - <bsw uom="%">75.21</bsw> | ||
1216 | - <bswPrevious uom="m3/m3">45.62</bswPrevious> | ||
1217 | - <densityValue> | ||
1218 | - <density uom="kg/m3">614.43</density> | ||
1219 | - <temp uom="K">44.32</temp> | ||
1220 | - <pres uom="Pa">11.68</pres> | ||
1221 | - </densityValue> | ||
1222 | - <density uom="kg/m3">503.27</density> | ||
1223 | - <densityFlowRate uom="Mg/a">392.39</densityFlowRate> | ||
1224 | - <densityStd uom="kg/m3">17.35</densityStd> | ||
1225 | - <concentration uom="ppm">38.15</concentration> | ||
1226 | - <molecularWeight>16.86</molecularWeight> | ||
1227 | - <weightPercent uom="%">81.26</weightPercent> | ||
1228 | - <molePercent uom="%">97.92</molePercent> | ||
1229 | - <moleAmt uom="kmol">58.33</moleAmt> | ||
1230 | - <sg uom="Euc">52.22</sg> | ||
1231 | - <hcDewpoint uom="K">430.19</hcDewpoint> | ||
1232 | - <waterDewpoint uom="K">612.34</waterDewpoint> | ||
1233 | - <wobbeIndex uom="J/m3">930.22</wobbeIndex> | ||
1234 | - <grossCalorificValueStd uom="J/m3">976.12</grossCalorificValueStd> | ||
1235 | - <rvpStabilizedCrude uom="Pa">157.5</rvpStabilizedCrude> | ||
1236 | - <bswStabilizedCrude uom="Euc">657.84</bswStabilizedCrude> | ||
1237 | - <densityStabilizedCrude uom="kg/m3">875.08</densityStabilizedCrude> | ||
1238 | - <componentContent uid="b15c985e-f359-11e1-aede-d067e534860e"> | ||
1239 | - <kind>C8-</kind> | ||
1240 | - <referenceKind>C2+</referenceKind> | ||
1241 | - <gor uom="Euc">64.08</gor> | ||
1242 | - <gorMTD uom="m3/m3">86.34</gorMTD> | ||
1243 | - <waterConcMass uom="%">16.26</waterConcMass> | ||
1244 | - <waterConcVol uom="ppm">68.4</waterConcVol> | ||
1245 | - <atmosphere uom="Pa">88.02</atmosphere> | ||
1246 | - <volumeValue> | ||
1247 | - <volume status="range limit" uom="m3">728.09</volume> | ||
1248 | - <grossCalorificValue uom="J/m3">143.82</grossCalorificValue> | ||
1249 | - <temp uom="K">27.37</temp> | ||
1250 | - <pres uom="Pa">61.47</pres> | ||
1251 | - </volumeValue> | ||
1252 | - <volume status="bad calibration" uom="m3">12.13</volume> | ||
1253 | - <volumeStd status="bad calibration" uom="m3">20.75</volumeStd> | ||
1254 | - <flowRate status="bad calibration" uom="m3/s">40.23</flowRate> | ||
1255 | - <temp uom="K">57.29</temp> | ||
1256 | - <pres uom="Pa">20.3</pres> | ||
1257 | - <absoluteMinPres uom="Pa">20.37</absoluteMinPres> | ||
1258 | - <portDiff uid="b15c985f-f359-11e1-8121-d067e534860e"> | ||
1259 | - <port uidRef="b15c9860-f359-11e1-b1fe-d067e534860e">Port 1</port> | ||
1260 | - <presDiff uom="Pa">34.64</presDiff> | ||
1261 | - <tempDiff uom="K">69.4</tempDiff> | ||
1262 | - <chokeSize uom="in/32">61.98</chokeSize> | ||
1263 | - <chokeRelative uom="%">84.39</chokeRelative> | ||
1264 | - </portDiff> | ||
1265 | - <portDiff uid="b15c9861-f359-11e1-8ce2-d067e534860e"> | ||
1266 | - <port uidRef="b15c9862-f359-11e1-a329-d067e534860e">Port 2</port> | ||
1267 | - <presDiff uom="Pa">28.03</presDiff> | ||
1268 | - <tempDiff uom="K">35.98</tempDiff> | ||
1269 | - <chokeSize uom="in/32">48.71</chokeSize> | ||
1270 | - <chokeRelative uom="%">42.2</chokeRelative> | ||
1271 | - </portDiff> | ||
1272 | - <mass uom="kg">34.7</mass> | ||
1273 | - <work uom="MJ">311.65</work> | ||
1274 | - <efficiency uom="%">36.41</efficiency> | ||
1275 | - <rvp uom="Pa">283.92</rvp> | ||
1276 | - <tvp uom="bar">81.56</tvp> | ||
1277 | - <bsw uom="%">29.64</bsw> | ||
1278 | - <bswPrevious uom="m3/m3">47.54</bswPrevious> | ||
1279 | - <densityValue> | ||
1280 | - <density uom="kg/m3">403.34</density> | ||
1281 | - <temp uom="K">96.81</temp> | ||
1282 | - <pres uom="Pa">58.59</pres> | ||
1283 | - </densityValue> | ||
1284 | - <density uom="kg/m3">415.33</density> | ||
1285 | - <densityFlowRate uom="Mg/a">95.9</densityFlowRate> | ||
1286 | - <densityStd uom="kg/m3">555.16</densityStd> | ||
1287 | - <concentration uom="ppm">74.38</concentration> | ||
1288 | - <molecularWeight>81.82</molecularWeight> | ||
1289 | - <weightPercent uom="%">62.0</weightPercent> | ||
1290 | - <molePercent uom="%">25.84</molePercent> | ||
1291 | - <moleAmt uom="kmol">17.98</moleAmt> | ||
1292 | - <sg uom="Euc">60.75</sg> | ||
1293 | - <hcDewpoint uom="K">538.39</hcDewpoint> | ||
1294 | - <waterDewpoint uom="K">713.48</waterDewpoint> | ||
1295 | - <wobbeIndex uom="J/m3">414.86</wobbeIndex> | ||
1296 | - <grossCalorificValueStd uom="J/m3">696.02</grossCalorificValueStd> | ||
1297 | - <rvpStabilizedCrude uom="Pa">40.25</rvpStabilizedCrude> | ||
1298 | - <bswStabilizedCrude uom="Euc">144.32</bswStabilizedCrude> | ||
1299 | - <densityStabilizedCrude uom="kg/m3">449.68</densityStabilizedCrude> | ||
1300 | - </componentContent> | ||
1301 | - <period> | ||
1302 | - <kind>day</kind> | ||
1303 | - <dateStart>2012-03-01</dateStart> | ||
1304 | - <dateEnd>2012-03-01</dateEnd> | ||
1305 | - <gor uom="Euc">82.02</gor> | ||
1306 | - <gorMTD uom="m3/m3">48.04</gorMTD> | ||
1307 | - <waterConcMass uom="%">36.29</waterConcMass> | ||
1308 | - <waterConcVol uom="ppm">31.71</waterConcVol> | ||
1309 | - <atmosphere uom="Pa">70.55</atmosphere> | ||
1310 | - <volumeValue> | ||
1311 | - | ||
1312 | - <volume uom="m3">135.02</volume><temp uom="degC">15</temp> | ||
1313 | - <pres uom="atm">1</pres> | ||
1314 | - </volumeValue> | ||
1315 | - <volume status="bad calibration" uom="m3">18.4</volume> | ||
1316 | - <volumeStd status="bad calibration" uom="m3">18.47</volumeStd> | ||
1317 | - <flowRate status="bad calibration" uom="m3/s">74.13</flowRate> | ||
1318 | - <temp uom="K">64.83</temp> | ||
1319 | - <pres uom="Pa">67.8</pres> | ||
1320 | - <absoluteMinPres uom="Pa">19.88</absoluteMinPres> | ||
1321 | - | ||
1322 | - <mass uom="kg">248.48</mass> | ||
1323 | - <work uom="MJ">713.54</work> | ||
1324 | - <efficiency uom="%">35.75</efficiency> | ||
1325 | - <rvp uom="kPa">95.73</rvp> | ||
1326 | - <tvp uom="bar">222.27</tvp> | ||
1327 | - <bsw uom="%">39.13</bsw> | ||
1328 | - <bswPrevious uom="m3/m3">60.56</bswPrevious> | ||
1329 | - <densityValue> | ||
1330 | - | ||
1331 | - <density uom="kg/m3">764.0</density> | ||
1332 | - <temp uom="degC">15</temp> | ||
1333 | - <pres uom="atm">1</pres> | ||
1334 | - </densityValue> | ||
1335 | - <density uom="kg/m3">44.25</density> | ||
1336 | - <densityFlowRate uom="Mg/a">337.54</densityFlowRate> | ||
1337 | - <densityStd uom="kg/m3">129.72</densityStd> | ||
1338 | - <concentration uom="ppm">50.71</concentration> | ||
1339 | - <molecularWeight>90.62</molecularWeight> | ||
1340 | - <weightPercent uom="%">17.46</weightPercent> | ||
1341 | - <molePercent uom="%">21.28</molePercent> | ||
1342 | - <moleAmt uom="kmol">79.29</moleAmt> | ||
1343 | - <sg uom="Euc">36.83</sg> | ||
1344 | - <hcDewpoint uom="K">581.7</hcDewpoint> | ||
1345 | - <waterDewpoint uom="K">52.64</waterDewpoint> | ||
1346 | - <wobbeIndex uom="J/m3">35.57</wobbeIndex> | ||
1347 | - <grossCalorificValueStd uom="J/m3">875.14</grossCalorificValueStd> | ||
1348 | - <rvpStabilizedCrude uom="Pa">128.34</rvpStabilizedCrude> | ||
1349 | - <bswStabilizedCrude uom="Euc">300.49</bswStabilizedCrude> | ||
1350 | - <densityStabilizedCrude uom="kg/m3">809.42</densityStabilizedCrude> | ||
1351 | - </period> | ||
1352 | - | ||
1353 | - </product> | ||
1354 | - </flow> | ||
1355 | - | ||
1356 | - | ||
1357 | - | ||
1358 | - <flow> | ||
1359 | - <kind>injection</kind> | ||
1360 | - <qualifier>metered - fiscal</qualifier> | ||
1361 | - <version>2012-03-01T04:00:00.0Z</version> | ||
1362 | - <versionSource>version src 635</versionSource> | ||
1363 | - <gor uom="Euc">62.59</gor> | ||
1364 | - <gorMTD uom="m3/m3">99.11</gorMTD> | ||
1365 | - <waterConcMass uom="%">71.6</waterConcMass> | ||
1366 | - <waterConcVol uom="ppm">34.53</waterConcVol> | ||
1367 | - <atmosphere uom="Pa">59.4</atmosphere> | ||
1368 | - <volumeValue> | ||
1369 | - <volume status="comm failure" uom="m3">180.82</volume> | ||
1370 | - <grossCalorificValue uom="J/m3">511.05</grossCalorificValue> | ||
1371 | - <temp uom="K">86.78</temp> | ||
1372 | - <pres uom="Pa">73.71</pres> | ||
1373 | - </volumeValue> | ||
1374 | - <volume status="bad calibration" uom="m3">72.43</volume> | ||
1375 | - <volumeStd status="bad calibration" uom="m3">11.29</volumeStd> | ||
1376 | - <flowRate status="bad calibration" uom="m3/s">74.12</flowRate> | ||
1377 | - <temp uom="K">90.24</temp> | ||
1378 | - <pres uom="Pa">39.52</pres> | ||
1379 | - <absoluteMinPres uom="Pa">80.54</absoluteMinPres> | ||
1380 | - <portDiff uid="b15cbf70-f359-11e1-ad49-d067e534860e"> | ||
1381 | - <port uidRef="b15cbf71-f359-11e1-8997-d067e534860e">Port 1</port> | ||
1382 | - <presDiff uom="Pa">69.24</presDiff> | ||
1383 | - <tempDiff uom="K">57.28</tempDiff> | ||
1384 | - <chokeSize uom="in/32">45.47</chokeSize> | ||
1385 | - <chokeRelative uom="%">33.96</chokeRelative> | ||
1386 | - </portDiff> | ||
1387 | - <portDiff uid="b15cbf72-f359-11e1-88aa-d067e534860e"> | ||
1388 | - <port uidRef="b15cbf73-f359-11e1-b8b2-d067e534860e">Port 2</port> | ||
1389 | - <presDiff uom="Pa">48.38</presDiff> | ||
1390 | - <tempDiff uom="K">82.09</tempDiff> | ||
1391 | - <chokeSize uom="in/32">68.67</chokeSize> | ||
1392 | - <chokeRelative uom="%">79.74</chokeRelative> | ||
1393 | - </portDiff> | ||
1394 | - <mass uom="kg">29.0</mass> | ||
1395 | - <work uom="MJ">876.38</work> | ||
1396 | - <efficiency uom="%">74.86</efficiency> | ||
1397 | - <rvp uom="Pa">80.38</rvp> | ||
1398 | - <tvp uom="bar">539.07</tvp> | ||
1399 | - <bsw uom="%">39.49</bsw> | ||
1400 | - <bswPrevious uom="m3/m3">52.6</bswPrevious> | ||
1401 | - <densityValue> | ||
1402 | - <density uom="kg/m3">157.53</density> | ||
1403 | - <temp uom="K">41.94</temp> | ||
1404 | - <pres uom="Pa">95.81</pres> | ||
1405 | - </densityValue> | ||
1406 | - <density uom="kg/m3">363.73</density> | ||
1407 | - <densityFlowRate uom="Mg/a">195.69</densityFlowRate> | ||
1408 | - <densityStd uom="kg/m3">447.12</densityStd> | ||
1409 | - <concentration uom="ppm">15.57</concentration> | ||
1410 | - <molecularWeight>63.44</molecularWeight> | ||
1411 | - <weightPercent uom="%">37.6</weightPercent> | ||
1412 | - <molePercent uom="%">48.26</molePercent> | ||
1413 | - <moleAmt uom="kmol">25.89</moleAmt> | ||
1414 | - <sg uom="Euc">42.71</sg> | ||
1415 | - <hcDewpoint uom="K">289.18</hcDewpoint> | ||
1416 | - <waterDewpoint uom="K">37.94</waterDewpoint> | ||
1417 | - <wobbeIndex uom="J/m3">477.46</wobbeIndex> | ||
1418 | - <grossCalorificValueStd uom="J/m3">661.2</grossCalorificValueStd> | ||
1419 | - <rvpStabilizedCrude uom="Pa">854.6</rvpStabilizedCrude> | ||
1420 | - <bswStabilizedCrude uom="Euc">756.71</bswStabilizedCrude> | ||
1421 | - <densityStabilizedCrude uom="kg/m3">774.01</densityStabilizedCrude> | ||
1422 | - <product> | ||
1423 | - <kind>oil - net</kind> | ||
1424 | - <name namingSystem="TEST443">Test product name 256</name> | ||
1425 | - <splitFactor>0.09</splitFactor> | ||
1426 | - <gor uom="Euc">94.36</gor> | ||
1427 | - <gorMTD uom="m3/m3">80.11</gorMTD> | ||
1428 | - <waterConcMass uom="%">41.65</waterConcMass> | ||
1429 | - <waterConcVol uom="ppm">95.09</waterConcVol> | ||
1430 | - <atmosphere uom="Pa">67.78</atmosphere> | ||
1431 | - <volumeValue> | ||
1432 | - <volume status="bad calibration" uom="m3">757.3</volume> | ||
1433 | - <grossCalorificValue uom="J/m3">513.29</grossCalorificValue> | ||
1434 | - <temp uom="K">72.66</temp> | ||
1435 | - <pres uom="Pa">39.02</pres> | ||
1436 | - </volumeValue> | ||
1437 | - <volume status="bad calibration" uom="m3">62.8</volume> | ||
1438 | - <volumeStd status="bad calibration" uom="m3">20.85</volumeStd> | ||
1439 | - <flowRate status="bad calibration" uom="m3/s">72.97</flowRate> | ||
1440 | - <temp uom="K">89.41</temp> | ||
1441 | - <pres uom="Pa">21.68</pres> | ||
1442 | - <absoluteMinPres uom="Pa">57.03</absoluteMinPres> | ||
1443 | - <portDiff uid="b15ce680-f359-11e1-85ee-d067e534860e"> | ||
1444 | - <port uidRef="b15ce681-f359-11e1-8bc7-d067e534860e">Port 1</port> | ||
1445 | - <presDiff uom="Pa">33.98</presDiff> | ||
1446 | - <tempDiff uom="K">62.45</tempDiff> | ||
1447 | - <chokeSize uom="in/32">28.8</chokeSize> | ||
1448 | - <chokeRelative uom="%">76.87</chokeRelative> | ||
1449 | - </portDiff> | ||
1450 | - <portDiff uid="b15ce682-f359-11e1-97c0-d067e534860e"> | ||
1451 | - <port uidRef="b15ce683-f359-11e1-8acf-d067e534860e">Port 2</port> | ||
1452 | - <presDiff uom="Pa">38.76</presDiff> | ||
1453 | - <tempDiff uom="K">99.18</tempDiff> | ||
1454 | - <chokeSize uom="in/32">79.9</chokeSize> | ||
1455 | - <chokeRelative uom="%">49.16</chokeRelative> | ||
1456 | - </portDiff> | ||
1457 | - <mass uom="kg">508.55</mass> | ||
1458 | - <work uom="MJ">457.39</work> | ||
1459 | - <efficiency uom="%">92.64</efficiency> | ||
1460 | - <rvp uom="Pa">511.71</rvp> | ||
1461 | - <tvp uom="bar">832.56</tvp> | ||
1462 | - <bsw uom="%">28.79</bsw> | ||
1463 | - <bswPrevious uom="m3/m3">55.61</bswPrevious> | ||
1464 | - <densityValue> | ||
1465 | - <density uom="kg/m3">482.8</density> | ||
1466 | - <temp uom="K">96.1</temp> | ||
1467 | - <pres uom="Pa">44.6</pres> | ||
1468 | - </densityValue> | ||
1469 | - <density uom="kg/m3">144.01</density> | ||
1470 | - <densityFlowRate uom="Mg/a">456.76</densityFlowRate> | ||
1471 | - <densityStd uom="kg/m3">31.37</densityStd> | ||
1472 | - <concentration uom="ppm">45.21</concentration> | ||
1473 | - <molecularWeight>76.82</molecularWeight> | ||
1474 | - <weightPercent uom="%">71.14</weightPercent> | ||
1475 | - <molePercent uom="%">18.61</molePercent> | ||
1476 | - <moleAmt uom="kmol">14.59</moleAmt> | ||
1477 | - <sg uom="Euc">20.78</sg> | ||
1478 | - <hcDewpoint uom="K">182.36</hcDewpoint> | ||
1479 | - <waterDewpoint uom="K">58.41</waterDewpoint> | ||
1480 | - <wobbeIndex uom="J/m3">189.42</wobbeIndex> | ||
1481 | - <grossCalorificValueStd uom="J/m3">542.81</grossCalorificValueStd> | ||
1482 | - <rvpStabilizedCrude uom="Pa">151.96</rvpStabilizedCrude> | ||
1483 | - <bswStabilizedCrude uom="Euc">229.69</bswStabilizedCrude> | ||
1484 | - <densityStabilizedCrude uom="kg/m3">718.59</densityStabilizedCrude> | ||
1485 | - <componentContent uid="b15ce684-f359-11e1-a8e5-d067e534860e"> | ||
1486 | - <kind>C6-</kind> | ||
1487 | - <referenceKind>C5+</referenceKind> | ||
1488 | - <gor uom="Euc">20.4</gor> | ||
1489 | - <gorMTD uom="m3/m3">12.0</gorMTD> | ||
1490 | - <waterConcMass uom="%">67.31</waterConcMass> | ||
1491 | - <waterConcVol uom="ppm">13.53</waterConcVol> | ||
1492 | - <atmosphere uom="Pa">78.48</atmosphere> | ||
1493 | - <volumeValue> | ||
1494 | - <volume status="comm failure" uom="m3">262.35</volume> | ||
1495 | - <grossCalorificValue uom="J/m3">747.49</grossCalorificValue> | ||
1496 | - <temp uom="K">52.64</temp> | ||
1497 | - <pres uom="Pa">58.56</pres> | ||
1498 | - </volumeValue> | ||
1499 | - <volume status="bad calibration" uom="m3">21.98</volume> | ||
1500 | - <volumeStd status="bad calibration" uom="m3">23.07</volumeStd> | ||
1501 | - <flowRate status="bad calibration" uom="m3/s">31.8</flowRate> | ||
1502 | - <temp uom="K">12.52</temp> | ||
1503 | - <pres uom="Pa">66.24</pres> | ||
1504 | - <absoluteMinPres uom="Pa">24.06</absoluteMinPres> | ||
1505 | - <portDiff uid="b15ce685-f359-11e1-b3b7-d067e534860e"> | ||
1506 | - <port uidRef="b15d0d8f-f359-11e1-a065-d067e534860e">Port 1</port> | ||
1507 | - <presDiff uom="Pa">24.07</presDiff> | ||
1508 | - <tempDiff uom="K">42.02</tempDiff> | ||
1509 | - <chokeSize uom="in/32">20.44</chokeSize> | ||
1510 | - <chokeRelative uom="%">89.75</chokeRelative> | ||
1511 | - </portDiff> | ||
1512 | - <portDiff uid="b15d0d90-f359-11e1-9858-d067e534860e"> | ||
1513 | - <port uidRef="b15d0d91-f359-11e1-9dbc-d067e534860e">Port 2</port> | ||
1514 | - <presDiff uom="Pa">86.21</presDiff> | ||
1515 | - <tempDiff uom="K">50.68</tempDiff> | ||
1516 | - <chokeSize uom="in/32">76.78</chokeSize> | ||
1517 | - <chokeRelative uom="%">87.98</chokeRelative> | ||
1518 | - </portDiff> | ||
1519 | - <mass uom="kg">383.68</mass> | ||
1520 | - <work uom="MJ">218.22</work> | ||
1521 | - <efficiency uom="%">14.2</efficiency> | ||
1522 | - <rvp uom="Pa">709.92</rvp> | ||
1523 | - <tvp uom="bar">728.89</tvp> | ||
1524 | - <bsw uom="%">46.3</bsw> | ||
1525 | - <bswPrevious uom="m3/m3">50.8</bswPrevious> | ||
1526 | - <densityValue> | ||
1527 | - <density uom="kg/m3">223.38</density> | ||
1528 | - <temp uom="K">26.59</temp> | ||
1529 | - <pres uom="Pa">65.64</pres> | ||
1530 | - </densityValue> | ||
1531 | - <density uom="kg/m3">389.51</density> | ||
1532 | - <densityFlowRate uom="Mg/a">308.61</densityFlowRate> | ||
1533 | - <densityStd uom="kg/m3">583.86</densityStd> | ||
1534 | - <concentration uom="ppm">55.73</concentration> | ||
1535 | - <molecularWeight>43.32</molecularWeight> | ||
1536 | - <weightPercent uom="%">35.54</weightPercent> | ||
1537 | - <molePercent uom="%">64.1</molePercent> | ||
1538 | - <moleAmt uom="kmol">49.82</moleAmt> | ||
1539 | - <sg uom="Euc">34.66</sg> | ||
1540 | - <hcDewpoint uom="K">384.87</hcDewpoint> | ||
1541 | - <waterDewpoint uom="K">652.28</waterDewpoint> | ||
1542 | - <wobbeIndex uom="J/m3">126.49</wobbeIndex> | ||
1543 | - <grossCalorificValueStd uom="J/m3">636.51</grossCalorificValueStd> | ||
1544 | - <rvpStabilizedCrude uom="Pa">408.77</rvpStabilizedCrude> | ||
1545 | - <bswStabilizedCrude uom="Euc">594.39</bswStabilizedCrude> | ||
1546 | - <densityStabilizedCrude uom="kg/m3">803.93</densityStabilizedCrude> | ||
1547 | - </componentContent> | ||
1548 | - <period> | ||
1549 | - <kind>day</kind> | ||
1550 | - <dateStart>2012-03-01</dateStart> | ||
1551 | - <dateEnd>2012-03-01</dateEnd> | ||
1552 | - <gor uom="Euc">72.91</gor> | ||
1553 | - <gorMTD uom="m3/m3">58.35</gorMTD> | ||
1554 | - <waterConcMass uom="%">32.95</waterConcMass> | ||
1555 | - <waterConcVol uom="ppm">16.43</waterConcVol> | ||
1556 | - <atmosphere uom="Pa">72.86</atmosphere> | ||
1557 | - <volumeValue> | ||
1558 | - | ||
1559 | - <volume uom="m3">1942.69</volume><temp uom="degC">15</temp> | ||
1560 | - <pres uom="atm">1</pres> | ||
1561 | - </volumeValue> | ||
1562 | - <volume status="bad calibration" uom="m3">29.66</volume> | ||
1563 | - <volumeStd status="bad calibration" uom="m3">66.4</volumeStd> | ||
1564 | - <flowRate status="bad calibration" uom="m3/s">52.11</flowRate> | ||
1565 | - <temp uom="K">74.04</temp> | ||
1566 | - <pres uom="Pa">50.23</pres> | ||
1567 | - <absoluteMinPres uom="Pa">59.9</absoluteMinPres> | ||
1568 | - | ||
1569 | - <mass uom="kg">634.99</mass> | ||
1570 | - <work uom="MJ">307.21</work> | ||
1571 | - <efficiency uom="%">80.38</efficiency> | ||
1572 | - <rvp uom="kPa">871.12</rvp> | ||
1573 | - <tvp uom="bar">138.67</tvp> | ||
1574 | - <bsw uom="%">60.01</bsw> | ||
1575 | - <bswPrevious uom="m3/m3">28.12</bswPrevious> | ||
1576 | - <densityValue> | ||
1577 | - | ||
1578 | - <density uom="kg/m3">792.8</density> | ||
1579 | - <temp uom="degC">15</temp> | ||
1580 | - <pres uom="atm">1</pres> | ||
1581 | - </densityValue> | ||
1582 | - <density uom="kg/m3">108.13</density> | ||
1583 | - <densityFlowRate uom="Mg/a">355.61</densityFlowRate> | ||
1584 | - <densityStd uom="kg/m3">232.29</densityStd> | ||
1585 | - <concentration uom="ppm">44.72</concentration> | ||
1586 | - <molecularWeight>19.96</molecularWeight> | ||
1587 | - <weightPercent uom="%">15.14</weightPercent> | ||
1588 | - <molePercent uom="%">95.88</molePercent> | ||
1589 | - <moleAmt uom="kmol">67.42</moleAmt> | ||
1590 | - <sg uom="Euc">98.09</sg> | ||
1591 | - <hcDewpoint uom="K">829.2</hcDewpoint> | ||
1592 | - <waterDewpoint uom="K">803.34</waterDewpoint> | ||
1593 | - <wobbeIndex uom="J/m3">223.36</wobbeIndex> | ||
1594 | - <grossCalorificValueStd uom="J/m3">318.81</grossCalorificValueStd> | ||
1595 | - <rvpStabilizedCrude uom="Pa">793.94</rvpStabilizedCrude> | ||
1596 | - <bswStabilizedCrude uom="Euc">171.79</bswStabilizedCrude> | ||
1597 | - <densityStabilizedCrude uom="kg/m3">750.3</densityStabilizedCrude> | ||
1598 | - </period> | ||
1599 | - | ||
1600 | - </product> | ||
1601 | - </flow> | ||
1602 | - | ||
1603 | - | ||
1604 | - | ||
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1606 | - </facility> | ||
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1608 | - <name>TYRIHANS-LIQUID-CHARACTERISTICS-1</name> | ||
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1878 | - </customData> | ||
1879 | - </object><object xsi:type="obj_fluidSample"> | ||
1880 | - <name>TYRIHANS-LIQUID-CHARACTERISTICS-3</name> | ||
1881 | - <sampleType>separator oil</sampleType> | ||
1882 | - <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility> | ||
1883 | - <acquisitionDate>2012-02-12</acquisitionDate> | ||
1884 | - <customData> | ||
1885 | - <extensionNameValue> | ||
1886 | - <name>ValidFrom</name> | ||
1887 | - <value>2012-02-12T00:00:00.0Z</value> | ||
1888 | - <dataType>dateTime</dataType> | ||
1889 | - </extensionNameValue> | ||
1890 | - <extensionNameValue> | ||
1891 | - <name>ValidTo</name> | ||
1892 | - <value>2012-02-26T00:00:00.0Z</value> | ||
1893 | - <dataType>dateTime</dataType> | ||
1894 | - </extensionNameValue> | ||
1895 | - </customData> | ||
1896 | - </object><object xsi:type="obj_fluidSample"> | ||
1897 | - <name>TYRIHANS-GAS-CHARACTERISTICS-3</name> | ||
1898 | - <sampleType>separator gas</sampleType> | ||
1899 | - <facility kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</facility> | ||
1900 | - <acquisitionDate>2012-02-12</acquisitionDate> | ||
1901 | - <customData> | ||
1902 | - <extensionNameValue> | ||
1903 | - <name>ValidFrom</name> | ||
1904 | - <value>2012-02-12T00:00:00.0Z</value> | ||
1905 | - <dataType>dateTime</dataType> | ||
1906 | - </extensionNameValue> | ||
1907 | - <extensionNameValue> | ||
1908 | - <name>ValidTo</name> | ||
1909 | - <value>2012-02-26T00:00:00.0Z</value> | ||
1910 | - <dataType>dateTime</dataType> | ||
1911 | - </extensionNameValue> | ||
1912 | - </customData> | ||
1913 | - </object></objects> | ||
... | \ No newline at end of file | ... | \ No newline at end of file |
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