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David Price
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Upload of results of file split for testing

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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>2.0</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="a57d492e-bad4-11e1-963a-c0f8dae91040">
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">22</work>
86 + <workMonthToDate uom="d">23</workMonthToDate>
87 + <workYearToDate uom="d">62</workYearToDate>
88 + <operationalHSE>
89 + <IncidentCount>1</IncidentCount>
90 + <sinceLostTime uom="d">10</sinceLostTime>
91 + <sincePreventionExercise uom="d">13</sincePreventionExercise>
92 + <sinceDefinedSituation uom="d">2</sinceDefinedSituation>
93 + <alarmCount>0</alarmCount>
94 + <safetyIntroCount>0</safetyIntroCount>
95 + <safetyDescription>I suggested that these results</safetyDescription>
96 + <safety>
97 + <meantimeIncident uom="d">2</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>It may be, then, that the notion of level of grammaticalness is unspecified with respect to a parasi</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">57.56</barometricPressure>
110 + <beaufortScaleNumber>5</beaufortScaleNumber>
111 + <tempSurfaceMn uom="degC">15</tempSurfaceMn>
112 + <tempSurfaceMx uom="degC">12</tempSurfaceMx>
113 + <tempWindChill uom="degC">13</tempWindChill>
114 + <tempsea uom="degC">13</tempsea>
115 + <visibility uom="m">391</visibility>
116 + <aziWave uom="rad">9</aziWave>
117 + <htWave uom="m">7</htWave>
118 + <significantWave uom="m">6</significantWave>
119 + <maxWave uom="m">2</maxWave>
120 + <periodWave uom="s">3</periodWave>
121 + <aziWind uom="rad">2</aziWind>
122 + <velWind uom="m/s">9</velWind>
123 + <typePrecip>rain</typePrecip>
124 + <amtPrecip uom="m">3</amtPrecip>
125 + <coverCloud>180</coverCloud>
126 + <ceilingCloud uom="m">230</ceilingCloud>
127 + <currentSea uom="m/s">1</currentSea>
128 + <aziCurrentSea uom="rad">3</aziCurrentSea>
129 + <comments>I suggested that these results would follow from the assumption that the descriptive power of the ba</comments>
130 + </weather>
131 +
132 + </operationalHSE>
133 +
134 + <productionActivity>
135 + <lostProduction>
136 + <volumeAndReason reasonLost="topside equipment failure-maint" uom="m3">1053.4</volumeAndReason>
137 + <volumeAndReason reasonLost="preventive maint topside" uom="m3">1140.2</volumeAndReason>
138 + <thirdPartyProcessing>
139 + <installation kind="platform">Ekofisk</installation>
140 + <oilStdTempPres uom="m3">1747.83</oilStdTempPres>
141 + <gasStdTempPres uom="m3">1196.25</gasStdTempPres>
142 + </thirdPartyProcessing>
143 +
144 + </lostProduction>
145 + <waterCleaningQuality>
146 + <samplePoint>Sample 1</samplePoint>
147 + <oilInWaterProduced uom="Euc">61.94</oilInWaterProduced>
148 + <amountOfOil uom="kg">96.85</amountOfOil>
149 + <ammonium uom="kg/m3">4.84</ammonium>
150 + <totalOrganicCarbon uom="Euc">14.33</totalOrganicCarbon>
151 + <phenol uom="kg/m3">27.87</phenol>
152 + <glycol uom="kg/m3">117.24</glycol>
153 + <phValue>8.03</phValue>
154 + <waterTemperature uom="degC">12.37</waterTemperature>
155 + <residualChloride uom="Euc">125.49</residualChloride>
156 + <oxygen uom="Euc">52.8</oxygen>
157 + <turbidity>32.4</turbidity>
158 + <coulterCounter uom="Euc">185.06</coulterCounter>
159 +
160 + <comment>
161 + <dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
162 + <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
163 + <remark>So far, the descriptive power of the base component is not to be considered in determining problems </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">0</volumetricDownTime>
172 + <lossOilStdTempPres uom="m3">780.08</lossOilStdTempPres>
173 + <lossGasStdTempPres uom="m3">7223.75</lossGasStdTempPres>
174 + <activity>
175 + <dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
176 + <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
177 + <remark>For any transformation which is sufficiently diversified in application to be of any interest, the t</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, a subset of English sentences interesting on quite independent grounds suffices to acc</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, the appearance of parasitic gaps in domains relatively inaccessible to ordinary extraction </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>So far, a case of semigrammaticalness of a different sort may remedy and, at the same time, eliminat</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>Thus a subset of English sentences interesting on quite independent grounds is to be regarded as a d</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>It appears that the systematic use of complex symbols is to be regarded as problems of phonemic and </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>However, this assumption is not correct, since the descriptive power of the base component is rather</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>A consequence of the approach just outlined is that the systematic use of complex symbols delimits t</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>In the discussion of resumptive pronouns following (81), the theory of syntactic features developed </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>Thus this selectionally introduced contextual feature is to be regarded as an important distinction </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">5381.62</oilGrossStdTempPres>
244 + <oilGrossTotalStdTempPres uom="m3">6615.82</oilGrossTotalStdTempPres>
245 + <oilNetStdTempPres uom="m3">5342.1</oilNetStdTempPres>
246 + <oilNetMonthToDateStdTempPres uom="m3">5241.47</oilNetMonthToDateStdTempPres>
247 + <densityStdTempPres uom="kg/m3">719.05</densityStdTempPres>
248 +
249 + <rvp uom="Pa">132.25</rvp>
250 + <bsw uom="Euc">197.35</bsw>
251 + <salt uom="kg/m3">116.05</salt>
252 + <comment>
253 + <dTimStart>2012-03-01T00:00:00.0Z</dTimStart>
254 + <dTimEnd>2012-03-01T23:59:59.0Z</dTimEnd>
255 + <remark>This suggests that a case of semigrammaticalness of a different sort does not affect the structure o</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>In the discussion of resumptive pronouns following (81), a case of semigrammaticalness of a differen</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>Nevertheless, most of the methodological work in modern linguistics is not quite equivalent to a des</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>For any transformation which is sufficiently diversified in application to be of any interest, the t</comment>
274 + </operationalComment>
275 + </productionActivity>
276 + </installationReport>
277 +</object><object xsi:type="obj_productVolume">
278 + <name>TYRIHANS</name>
279 + <installation kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</installation>
280 + <facility>
281 + <name kind="field" namingSystem="NPD" uidRef="3960848">TYRIHANS</name>
282 + <facilityParent1 kind="block valve" namingSystem="String" uidRef="x">String</facilityParent1>
283 + <facilityParent2 kind="block valve" namingSystem="String" uidRef="x">String</facilityParent2>
284 + <facilityAlias namingSystem="String">String</facilityAlias>
285 + <facilityAlias namingSystem="String">String</facilityAlias>
286 + <contextFacility kind="block valve" namingSystem="String" uidRef="x">String</contextFacility>
287 + <contextFacility kind="block valve" namingSystem="String" uidRef="x">String</contextFacility>
288 +
289 +
290 + <downtimeReason uid="a5939051-bad4-11e1-acc2-c0f8dae91040">
291 + <who>MR Who</who>
292 + <role>Platform manager</role>
293 + <dTimStart>2012-03-01T02:00:00.0Z</dTimStart>
294 + <dTimEnd>2012-03-01T04:00:00.0Z</dTimEnd>
295 + <remark>A consequence of the approach just outlined is that the speaker-hearer's linguistic intuition delimi</remark>
296 + </downtimeReason>
297 + <downtimeReason uid="a5939052-bad4-11e1-9b76-c0f8dae91040">
298 + <who>Mr Who2</who>
299 + <role>Platform manager 2</role>
300 + <dTimStart>2012-03-01T06:00:00.0Z</dTimStart>
301 + <dTimEnd>2012-03-01T14:00:00.0Z</dTimEnd>
302 + <remark>To characterize a linguistic level L, a descriptively adequate grammar does not readily tolerate the</remark>
303 + </downtimeReason>
304 + <flow>
305 + <kind>production</kind>
306 + <qualifier>saleable</qualifier>
307 + <version>2012-03-01T22:00:00.0Z</version>
308 + <versionSource>version src 914</versionSource>
309 + <gor uom="Euc">53.07</gor>
310 + <gorMTD uom="m3/m3">51.46</gorMTD>
311 + <waterConcMass uom="%">91.44</waterConcMass>
312 + <waterConcVol uom="ppm">49.19</waterConcVol>
313 + <atmosphere uom="Pa">75.38</atmosphere>
314 + <volumeValue>
315 + <volume status="questionable" uom="m3">785.16</volume>
316 + <grossCalorificValue uom="J/m3">641.22</grossCalorificValue>
317 + <temp uom="K">35.18</temp>
318 + <pres uom="Pa">94.73</pres>
319 + </volumeValue>
320 + <volume status="bad calibration" uom="m3">18.01</volume>
321 + <volumeStd status="bad calibration" uom="m3">16.78</volumeStd>
322 + <flowRate status="bad calibration" uom="m3/s">25.65</flowRate>
323 + <temp uom="K">61.2</temp>
324 + <pres uom="Pa">41.65</pres>
325 + <absoluteMinPres uom="Pa">65.2</absoluteMinPres>
326 + <portDiff uid="a593b75e-bad4-11e1-8a2f-c0f8dae91040">
327 + <port uidRef="a593b75f-bad4-11e1-9811-c0f8dae91040">Port 1</port>
328 + <presDiff uom="Pa">77.05</presDiff>
329 + <tempDiff uom="K">20.15</tempDiff>
330 + <chokeSize uom="in/32">71.74</chokeSize>
331 + <chokeRelative uom="%">23.04</chokeRelative>
332 + </portDiff>
333 + <portDiff uid="a593b760-bad4-11e1-852b-c0f8dae91040">
334 + <port uidRef="a593b761-bad4-11e1-913c-c0f8dae91040">Port 2</port>
335 + <presDiff uom="Pa">29.37</presDiff>
336 + <tempDiff uom="K">33.5</tempDiff>
337 + <chokeSize uom="in/32">55.86</chokeSize>
338 + <chokeRelative uom="%">62.26</chokeRelative>
339 + </portDiff>
340 + <mass uom="kg">596.23</mass>
341 + <work uom="MJ">116.13</work>
342 + <efficiency uom="%">58.88</efficiency>
343 + <rvp uom="Pa">761.31</rvp>
344 + <tvp uom="bar">609.35</tvp>
345 + <bsw uom="%">38.95</bsw>
346 + <bswPrevious uom="m3/m3">37.52</bswPrevious>
347 + <densityValue>
348 + <density uom="kg/m3">154.93</density>
349 + <temp uom="K">43.99</temp>
350 + <pres uom="Pa">84.69</pres>
351 + </densityValue>
352 + <density uom="kg/m3">134.58</density>
353 + <densityFlowRate uom="Mg/a">291.27</densityFlowRate>
354 + <densityStd uom="kg/m3">422.56</densityStd>
355 + <concentration uom="ppm">27.37</concentration>
356 + <molecularWeight>42.48</molecularWeight>
357 + <weightPercent uom="%">90.64</weightPercent>
358 + <molePercent uom="%">98.52</molePercent>
359 + <moleAmt uom="kmol">22.78</moleAmt>
360 + <sg uom="Euc">59.65</sg>
361 + <hcDewpoint uom="K">918.59</hcDewpoint>
362 + <waterDewpoint uom="K">505.72</waterDewpoint>
363 + <wobbeIndex uom="J/m3">783.46</wobbeIndex>
364 + <grossCalorificValueStd uom="J/m3">35.94</grossCalorificValueStd>
365 + <rvpStabilizedCrude uom="Pa">973.12</rvpStabilizedCrude>
366 + <bswStabilizedCrude uom="Euc">854.65</bswStabilizedCrude>
367 + <densityStabilizedCrude uom="kg/m3">610.47</densityStabilizedCrude>
368 + <product>
369 + <kind>oil - net</kind>
370 + <name namingSystem="TEST17">Test product name 507</name>
371 + <splitFactor>0.67</splitFactor>
372 + <gor uom="Euc">45.98</gor>
373 + <gorMTD uom="m3/m3">54.61</gorMTD>
374 + <waterConcMass uom="%">24.57</waterConcMass>
375 + <waterConcVol uom="ppm">49.63</waterConcVol>
376 + <atmosphere uom="Pa">96.97</atmosphere>
377 + <volumeValue>
378 + <volume status="questionable" uom="m3">882.04</volume>
379 + <grossCalorificValue uom="J/m3">412.16</grossCalorificValue>
380 + <temp uom="K">60.27</temp>
381 + <pres uom="Pa">76.05</pres>
382 + </volumeValue>
383 + <volume status="bad calibration" uom="m3">92.12</volume>
384 + <volumeStd status="bad calibration" uom="m3">18.65</volumeStd>
385 + <flowRate status="bad calibration" uom="m3/s">60.29</flowRate>
386 + <temp uom="K">98.91</temp>
387 + <pres uom="Pa">82.78</pres>
388 + <absoluteMinPres uom="Pa">34.27</absoluteMinPres>
389 + <portDiff uid="a593b762-bad4-11e1-a353-c0f8dae91040">
390 + <port uidRef="a593b763-bad4-11e1-9822-c0f8dae91040">Port 1</port>
391 + <presDiff uom="Pa">67.4</presDiff>
392 + <tempDiff uom="K">54.21</tempDiff>
393 + <chokeSize uom="in/32">79.02</chokeSize>
394 + <chokeRelative uom="%">44.15</chokeRelative>
395 + </portDiff>
396 + <portDiff uid="a593b764-bad4-11e1-ace2-c0f8dae91040">
397 + <port uidRef="a593b765-bad4-11e1-9607-c0f8dae91040">Port 2</port>
398 + <presDiff uom="Pa">41.6</presDiff>
399 + <tempDiff uom="K">90.5</tempDiff>
400 + <chokeSize uom="in/32">65.45</chokeSize>
401 + <chokeRelative uom="%">57.19</chokeRelative>
402 + </portDiff>
403 + <mass uom="kg">79.45</mass>
404 + <work uom="MJ">181.12</work>
405 + <efficiency uom="%">33.95</efficiency>
406 + <rvp uom="Pa">705.54</rvp>
407 + <tvp uom="bar">153.81</tvp>
408 + <bsw uom="%">32.3</bsw>
409 + <bswPrevious uom="m3/m3">95.5</bswPrevious>
410 + <densityValue>
411 + <density uom="kg/m3">175.98</density>
412 + <temp uom="K">56.57</temp>
413 + <pres uom="Pa">45.46</pres>
414 + </densityValue>
415 + <density uom="kg/m3">36.16</density>
416 + <densityFlowRate uom="Mg/a">274.98</densityFlowRate>
417 + <densityStd uom="kg/m3">204.26</densityStd>
418 + <concentration uom="ppm">16.59</concentration>
419 + <molecularWeight>33.95</molecularWeight>
420 + <weightPercent uom="%">50.19</weightPercent>
421 + <molePercent uom="%">93.72</molePercent>
422 + <moleAmt uom="kmol">23.97</moleAmt>
423 + <sg uom="Euc">16.12</sg>
424 + <hcDewpoint uom="K">237.23</hcDewpoint>
425 + <waterDewpoint uom="K">524.96</waterDewpoint>
426 + <wobbeIndex uom="J/m3">840.05</wobbeIndex>
427 + <grossCalorificValueStd uom="J/m3">300.4</grossCalorificValueStd>
428 + <rvpStabilizedCrude uom="Pa">976.7</rvpStabilizedCrude>
429 + <bswStabilizedCrude uom="Euc">265.02</bswStabilizedCrude>
430 + <densityStabilizedCrude uom="kg/m3">296.01</densityStabilizedCrude>
431 + <componentContent uid="a593de6e-bad4-11e1-9499-c0f8dae91040">
432 + <kind>nitrogen oxide gas</kind>
433 + <referenceKind>carbon dioxide gas</referenceKind>
434 + <gor uom="Euc">69.5</gor>
435 + <gorMTD uom="m3/m3">93.25</gorMTD>
436 + <waterConcMass uom="%">60.35</waterConcMass>
437 + <waterConcVol uom="ppm">31.85</waterConcVol>
438 + <atmosphere uom="Pa">91.8</atmosphere>
439 + <volumeValue>
440 + <volume status="bad calibration" uom="m3">712.13</volume>
441 + <grossCalorificValue uom="J/m3">470.75</grossCalorificValue>
442 + <temp uom="K">43.71</temp>
443 + <pres uom="Pa">63.99</pres>
444 + </volumeValue>
445 + <volume status="bad calibration" uom="m3">48.95</volume>
446 + <volumeStd status="bad calibration" uom="m3">61.28</volumeStd>
447 + <flowRate status="bad calibration" uom="m3/s">71.87</flowRate>
448 + <temp uom="K">45.51</temp>
449 + <pres uom="Pa">27.53</pres>
450 + <absoluteMinPres uom="Pa">98.37</absoluteMinPres>
451 + <portDiff uid="a593de6f-bad4-11e1-97d5-c0f8dae91040">
452 + <port uidRef="a5940580-bad4-11e1-b600-c0f8dae91040">Port 1</port>
453 + <presDiff uom="Pa">50.5</presDiff>
454 + <tempDiff uom="K">96.22</tempDiff>
455 + <chokeSize uom="in/32">11.2</chokeSize>
456 + <chokeRelative uom="%">82.82</chokeRelative>
457 + </portDiff>
458 + <portDiff uid="a5940581-bad4-11e1-a2b6-c0f8dae91040">
459 + <port uidRef="a5940582-bad4-11e1-9596-c0f8dae91040">Port 2</port>
460 + <presDiff uom="Pa">21.23</presDiff>
461 + <tempDiff uom="K">19.55</tempDiff>
462 + <chokeSize uom="in/32">91.67</chokeSize>
463 + <chokeRelative uom="%">19.6</chokeRelative>
464 + </portDiff>
465 + <mass uom="kg">456.12</mass>
466 + <work uom="MJ">495.34</work>
467 + <efficiency uom="%">75.15</efficiency>
468 + <rvp uom="Pa">202.1</rvp>
469 + <tvp uom="bar">805.39</tvp>
470 + <bsw uom="%">49.24</bsw>
471 + <bswPrevious uom="m3/m3">98.52</bswPrevious>
472 + <densityValue>
473 + <density uom="kg/m3">538.56</density>
474 + <temp uom="K">61.47</temp>
475 + <pres uom="Pa">48.61</pres>
476 + </densityValue>
477 + <density uom="kg/m3">256.01</density>
478 + <densityFlowRate uom="Mg/a">20.2</densityFlowRate>
479 + <densityStd uom="kg/m3">139.29</densityStd>
480 + <concentration uom="ppm">17.42</concentration>
481 + <molecularWeight>21.62</molecularWeight>
482 + <weightPercent uom="%">80.09</weightPercent>
483 + <molePercent uom="%">35.27</molePercent>
484 + <moleAmt uom="kmol">33.81</moleAmt>
485 + <sg uom="Euc">70.01</sg>
486 + <hcDewpoint uom="K">519.78</hcDewpoint>
487 + <waterDewpoint uom="K">453.96</waterDewpoint>
488 + <wobbeIndex uom="J/m3">431.08</wobbeIndex>
489 + <grossCalorificValueStd uom="J/m3">579.92</grossCalorificValueStd>
490 + <rvpStabilizedCrude uom="Pa">167.9</rvpStabilizedCrude>
491 + <bswStabilizedCrude uom="Euc">97.6</bswStabilizedCrude>
492 + <densityStabilizedCrude uom="kg/m3">229.67</densityStabilizedCrude>
493 + </componentContent>
494 + <period>
495 + <kind>day</kind>
496 + <dateStart>2012-03-01</dateStart>
497 + <dateEnd>2012-03-01</dateEnd>
498 + <gor uom="Euc">80.87</gor>
499 + <gorMTD uom="m3/m3">71.58</gorMTD>
500 + <waterConcMass uom="%">10.64</waterConcMass>
501 + <waterConcVol uom="ppm">83.83</waterConcVol>
502 + <atmosphere uom="Pa">22.32</atmosphere>
503 + <volumeValue>
504 +
505 + <volume uom="m3">2765.7</volume><temp uom="degC">15</temp>
506 + <pres uom="atm">1</pres>
507 + </volumeValue>
508 + <volume status="bad calibration" uom="m3">36.48</volume>
509 + <volumeStd status="bad calibration" uom="m3">38.47</volumeStd>
510 + <flowRate status="bad calibration" uom="m3/s">55.99</flowRate>
511 + <temp uom="K">73.65</temp>
512 + <pres uom="Pa">13.61</pres>
513 + <absoluteMinPres uom="Pa">79.98</absoluteMinPres>
514 +
515 + <mass uom="kg">89.49</mass>
516 + <work uom="kW.h">435.72</work>
517 + <efficiency uom="%">98.18</efficiency>
518 + <rvp uom="bar">461.58</rvp>
519 + <tvp uom="bar">447.55</tvp>
520 + <bsw uom="%">68.5</bsw>
521 + <bswPrevious uom="m3/m3">43.97</bswPrevious>
522 + <densityValue>
523 +
524 + <density uom="kg/m3">780.91</density>
525 + <temp uom="degC">15</temp>
526 + <pres uom="atm">1</pres>
527 + </densityValue>
528 + <density uom="kg/m3">678.0</density>
529 + <densityFlowRate uom="Mg/a">166.24</densityFlowRate>
530 + <densityStd uom="kg/m3">527.52</densityStd>
531 + <concentration uom="ppm">50.64</concentration>
532 + <molecularWeight>87.94</molecularWeight>
533 + <weightPercent uom="%">34.91</weightPercent>
534 + <molePercent uom="%">31.48</molePercent>
535 + <moleAmt uom="kmol">47.46</moleAmt>
536 + <sg uom="Euc">94.18</sg>
537 + <hcDewpoint uom="K">488.91</hcDewpoint>
538 + <waterDewpoint uom="K">840.9</waterDewpoint>
539 + <wobbeIndex uom="J/m3">824.93</wobbeIndex>
540 + <grossCalorificValueStd uom="J/m3">993.66</grossCalorificValueStd>
541 + <rvpStabilizedCrude uom="Pa">398.65</rvpStabilizedCrude>
542 + <bswStabilizedCrude uom="Euc">673.57</bswStabilizedCrude>
543 + <densityStabilizedCrude uom="kg/m3">173.57</densityStabilizedCrude>
544 + </period>
545 +
546 + </product>
547 + </flow>
548 +
549 +
550 +
551 + <flow>
552 + <kind>consume - fuel</kind>
553 + <qualifier>allocated</qualifier>
554 + <version>2012-03-01T17:00:00.0Z</version>
555 + <versionSource>version src 454</versionSource>
556 + <gor uom="Euc">83.64</gor>
557 + <gorMTD uom="m3/m3">45.54</gorMTD>
558 + <waterConcMass uom="%">34.27</waterConcMass>
559 + <waterConcVol uom="ppm">30.89</waterConcVol>
560 + <atmosphere uom="Pa">15.07</atmosphere>
561 + <volumeValue>
562 + <volume status="sensor failure" uom="m3">850.38</volume>
563 + <grossCalorificValue uom="J/m3">882.59</grossCalorificValue>
564 + <temp uom="K">10.19</temp>
565 + <pres uom="Pa">85.11</pres>
566 + </volumeValue>
567 + <volume status="bad calibration" uom="m3">10.84</volume>
568 + <volumeStd status="bad calibration" uom="m3">89.23</volumeStd>
569 + <flowRate status="bad calibration" uom="m3/s">62.14</flowRate>
570 + <temp uom="K">12.66</temp>
571 + <pres uom="Pa">25.63</pres>
572 + <absoluteMinPres uom="Pa">31.24</absoluteMinPres>
573 + <portDiff uid="a5942c8f-bad4-11e1-b412-c0f8dae91040">
574 + <port uidRef="a5942c90-bad4-11e1-836f-c0f8dae91040">Port 1</port>
575 + <presDiff uom="Pa">75.65</presDiff>
576 + <tempDiff uom="K">31.06</tempDiff>
577 + <chokeSize uom="in/32">35.58</chokeSize>
578 + <chokeRelative uom="%">40.81</chokeRelative>
579 + </portDiff>
580 + <portDiff uid="a5942c91-bad4-11e1-9523-c0f8dae91040">
581 + <port uidRef="a5942c92-bad4-11e1-a7de-c0f8dae91040">Port 2</port>
582 + <presDiff uom="Pa">98.78</presDiff>
583 + <tempDiff uom="K">43.86</tempDiff>
584 + <chokeSize uom="in/32">38.01</chokeSize>
585 + <chokeRelative uom="%">35.99</chokeRelative>
586 + </portDiff>
587 + <mass uom="kg">288.8</mass>
588 + <work uom="MJ">21.58</work>
589 + <efficiency uom="%">87.73</efficiency>
590 + <rvp uom="Pa">654.07</rvp>
591 + <tvp uom="bar">679.85</tvp>
592 + <bsw uom="%">53.44</bsw>
593 + <bswPrevious uom="m3/m3">84.51</bswPrevious>
594 + <densityValue>
595 + <density uom="kg/m3">244.39</density>
596 + <temp uom="K">93.72</temp>
597 + <pres uom="Pa">50.81</pres>
598 + </densityValue>
599 + <density uom="kg/m3">137.61</density>
600 + <densityFlowRate uom="Mg/a">464.38</densityFlowRate>
601 + <densityStd uom="kg/m3">42.16</densityStd>
602 + <concentration uom="ppm">51.32</concentration>
603 + <molecularWeight>54.77</molecularWeight>
604 + <weightPercent uom="%">72.21</weightPercent>
605 + <molePercent uom="%">13.21</molePercent>
606 + <moleAmt uom="kmol">25.08</moleAmt>
607 + <sg uom="Euc">64.37</sg>
608 + <hcDewpoint uom="K">658.1</hcDewpoint>
609 + <waterDewpoint uom="K">180.48</waterDewpoint>
610 + <wobbeIndex uom="J/m3">902.14</wobbeIndex>
611 + <grossCalorificValueStd uom="J/m3">976.38</grossCalorificValueStd>
612 + <rvpStabilizedCrude uom="Pa">733.45</rvpStabilizedCrude>
613 + <bswStabilizedCrude uom="Euc">542.71</bswStabilizedCrude>
614 + <densityStabilizedCrude uom="kg/m3">616.46</densityStabilizedCrude>
615 + <product>
616 + <kind>diesel</kind>
617 + <name namingSystem="TEST2">Test product name 445</name>
618 + <splitFactor>0.56</splitFactor>
619 + <gor uom="Euc">87.93</gor>
620 + <gorMTD uom="m3/m3">96.91</gorMTD>
621 + <waterConcMass uom="%">34.59</waterConcMass>
622 + <waterConcVol uom="ppm">58.99</waterConcVol>
623 + <atmosphere uom="Pa">34.97</atmosphere>
624 + <volumeValue>
625 + <volume status="range limit" uom="m3">874.32</volume>
626 + <grossCalorificValue uom="J/m3">28.2</grossCalorificValue>
627 + <temp uom="K">78.68</temp>
628 + <pres uom="Pa">95.72</pres>
629 + </volumeValue>
630 + <volume status="bad calibration" uom="m3">27.39</volume>
631 + <volumeStd status="bad calibration" uom="m3">98.79</volumeStd>
632 + <flowRate status="bad calibration" uom="m3/s">18.51</flowRate>
633 + <temp uom="K">30.35</temp>
634 + <pres uom="Pa">32.06</pres>
635 + <absoluteMinPres uom="Pa">39.12</absoluteMinPres>
636 + <portDiff uid="a5942c93-bad4-11e1-99d0-c0f8dae91040">
637 + <port uidRef="a5942c94-bad4-11e1-9bc6-c0f8dae91040">Port 1</port>
638 + <presDiff uom="Pa">42.88</presDiff>
639 + <tempDiff uom="K">95.96</tempDiff>
640 + <chokeSize uom="in/32">95.96</chokeSize>
641 + <chokeRelative uom="%">92.33</chokeRelative>
642 + </portDiff>
643 + <portDiff uid="a5942c95-bad4-11e1-952d-c0f8dae91040">
644 + <port uidRef="a5942c96-bad4-11e1-8807-c0f8dae91040">Port 2</port>
645 + <presDiff uom="Pa">37.99</presDiff>
646 + <tempDiff uom="K">32.1</tempDiff>
647 + <chokeSize uom="in/32">84.84</chokeSize>
648 + <chokeRelative uom="%">28.26</chokeRelative>
649 + </portDiff>
650 + <mass uom="kg">84.07</mass>
651 + <work uom="MJ">59.04</work>
652 + <efficiency uom="%">59.05</efficiency>
653 + <rvp uom="Pa">31.33</rvp>
654 + <tvp uom="bar">923.69</tvp>
655 + <bsw uom="%">77.68</bsw>
656 + <bswPrevious uom="m3/m3">11.7</bswPrevious>
657 + <densityValue>
658 + <density uom="kg/m3">138.04</density>
659 + <temp uom="K">67.82</temp>
660 + <pres uom="Pa">71.84</pres>
661 + </densityValue>
662 + <density uom="kg/m3">571.01</density>
663 + <densityFlowRate uom="Mg/a">141.97</densityFlowRate>
664 + <densityStd uom="kg/m3">117.99</densityStd>
665 + <concentration uom="ppm">86.56</concentration>
666 + <molecularWeight>50.68</molecularWeight>
667 + <weightPercent uom="%">43.99</weightPercent>
668 + <molePercent uom="%">41.45</molePercent>
669 + <moleAmt uom="kmol">98.87</moleAmt>
670 + <sg uom="Euc">23.8</sg>
671 + <hcDewpoint uom="K">854.28</hcDewpoint>
672 + <waterDewpoint uom="K">12.84</waterDewpoint>
673 + <wobbeIndex uom="J/m3">594.48</wobbeIndex>
674 + <grossCalorificValueStd uom="J/m3">349.99</grossCalorificValueStd>
675 + <rvpStabilizedCrude uom="Pa">484.17</rvpStabilizedCrude>
676 + <bswStabilizedCrude uom="Euc">136.17</bswStabilizedCrude>
677 + <densityStabilizedCrude uom="kg/m3">96.22</densityStabilizedCrude>
678 + <componentContent uid="a594539e-bad4-11e1-94f3-c0f8dae91040">
679 + <kind>normal butane</kind>
680 + <referenceKind>gas</referenceKind>
681 + <gor uom="Euc">49.31</gor>
682 + <gorMTD uom="m3/m3">98.68</gorMTD>
683 + <waterConcMass uom="%">37.24</waterConcMass>
684 + <waterConcVol uom="ppm">84.94</waterConcVol>
685 + <atmosphere uom="Pa">84.18</atmosphere>
686 + <volumeValue>
687 + <volume status="sensor failure" uom="m3">73.31</volume>
688 + <grossCalorificValue uom="J/m3">857.4</grossCalorificValue>
689 + <temp uom="K">71.98</temp>
690 + <pres uom="Pa">49.32</pres>
691 + </volumeValue>
692 + <volume status="bad calibration" uom="m3">99.1</volume>
693 + <volumeStd status="bad calibration" uom="m3">13.42</volumeStd>
694 + <flowRate status="bad calibration" uom="m3/s">73.44</flowRate>
695 + <temp uom="K">42.77</temp>
696 + <pres uom="Pa">53.17</pres>
697 + <absoluteMinPres uom="Pa">57.29</absoluteMinPres>
698 + <portDiff uid="a594539f-bad4-11e1-b23d-c0f8dae91040">
699 + <port uidRef="a59453a0-bad4-11e1-a37c-c0f8dae91040">Port 1</port>
700 + <presDiff uom="Pa">26.17</presDiff>
701 + <tempDiff uom="K">84.48</tempDiff>
702 + <chokeSize uom="in/32">27.72</chokeSize>
703 + <chokeRelative uom="%">20.24</chokeRelative>
704 + </portDiff>
705 + <portDiff uid="a59453a1-bad4-11e1-b446-c0f8dae91040">
706 + <port uidRef="a59453a2-bad4-11e1-aa56-c0f8dae91040">Port 2</port>
707 + <presDiff uom="Pa">52.42</presDiff>
708 + <tempDiff uom="K">27.49</tempDiff>
709 + <chokeSize uom="in/32">24.29</chokeSize>
710 + <chokeRelative uom="%">52.0</chokeRelative>
711 + </portDiff>
712 + <mass uom="kg">215.92</mass>
713 + <work uom="MJ">30.67</work>
714 + <efficiency uom="%">78.11</efficiency>
715 + <rvp uom="Pa">324.12</rvp>
716 + <tvp uom="bar">976.29</tvp>
717 + <bsw uom="%">47.4</bsw>
718 + <bswPrevious uom="m3/m3">67.76</bswPrevious>
719 + <densityValue>
720 + <density uom="kg/m3">662.26</density>
721 + <temp uom="K">16.91</temp>
722 + <pres uom="Pa">38.29</pres>
723 + </densityValue>
724 + <density uom="kg/m3">368.3</density>
725 + <densityFlowRate uom="Mg/a">213.54</densityFlowRate>
726 + <densityStd uom="kg/m3">653.79</densityStd>
727 + <concentration uom="ppm">81.69</concentration>
728 + <molecularWeight>29.26</molecularWeight>
729 + <weightPercent uom="%">33.19</weightPercent>
730 + <molePercent uom="%">99.23</molePercent>
731 + <moleAmt uom="kmol">47.94</moleAmt>
732 + <sg uom="Euc">79.73</sg>
733 + <hcDewpoint uom="K">10.03</hcDewpoint>
734 + <waterDewpoint uom="K">997.84</waterDewpoint>
735 + <wobbeIndex uom="J/m3">30.11</wobbeIndex>
736 + <grossCalorificValueStd uom="J/m3">352.47</grossCalorificValueStd>
737 + <rvpStabilizedCrude uom="Pa">847.36</rvpStabilizedCrude>
738 + <bswStabilizedCrude uom="Euc">511.07</bswStabilizedCrude>
739 + <densityStabilizedCrude uom="kg/m3">866.05</densityStabilizedCrude>
740 + </componentContent>
741 + <period>
742 + <kind>day</kind>
743 + <dateStart>2012-03-01</dateStart>
744 + <dateEnd>2012-03-01</dateEnd>
745 + <gor uom="Euc">11.58</gor>
746 + <gorMTD uom="m3/m3">18.4</gorMTD>
747 + <waterConcMass uom="%">36.78</waterConcMass>
748 + <waterConcVol uom="ppm">50.57</waterConcVol>
749 + <atmosphere uom="Pa">47.47</atmosphere>
750 +
751 + <volumeValue>
752 + <volume uom="L">59.52</volume>
753 + <temp uom="degC">15</temp>
754 + <pres uom="atm">1</pres>
755 + </volumeValue><volume status="bad calibration" uom="m3">95.3</volume>
756 + <volumeStd status="bad calibration" uom="m3">86.7</volumeStd>
757 + <flowRate status="bad calibration" uom="m3/s">11.13</flowRate>
758 + <temp uom="K">65.44</temp>
759 + <pres uom="Pa">69.91</pres>
760 + <absoluteMinPres uom="Pa">81.24</absoluteMinPres>
761 +
762 +
763 + <work uom="J">175.15</work>
764 + <efficiency uom="%">44.51</efficiency>
765 + <rvp uom="atm">390.35</rvp>
766 + <tvp uom="bar">364.31</tvp>
767 + <bsw uom="%">12.64</bsw>
768 + <bswPrevious uom="m3/m3">11.22</bswPrevious>
769 +
770 + <density uom="kg/m3">456.65</density>
771 + <densityFlowRate uom="Mg/a">458.25</densityFlowRate>
772 + <densityStd uom="kg/m3">234.65</densityStd>
773 + <concentration uom="ppm">93.17</concentration>
774 + <molecularWeight>61.41</molecularWeight>
775 + <weightPercent uom="%">93.71</weightPercent>
776 + <molePercent uom="%">80.96</molePercent>
777 + <moleAmt uom="kmol">34.98</moleAmt>
778 + <sg uom="Euc">15.91</sg>
779 + <hcDewpoint uom="K">154.45</hcDewpoint>
780 + <waterDewpoint uom="K">573.72</waterDewpoint>
781 + <wobbeIndex uom="J/m3">790.72</wobbeIndex>
782 + <grossCalorificValueStd uom="J/m3">854.35</grossCalorificValueStd>
783 + <rvpStabilizedCrude uom="Pa">999.73</rvpStabilizedCrude>
784 + <bswStabilizedCrude uom="Euc">590.89</bswStabilizedCrude>
785 + <densityStabilizedCrude uom="kg/m3">739.43</densityStabilizedCrude>
786 + </period>
787 +
788 + </product>
789 + </flow>
790 +
791 +
792 +
793 +
794 + </facility><facility>
795 + <name kind="compressor" namingSystem="STATOIL" uidRef="NaN">TYRIHANS compressor</name>
796 + <facilityParent1 kind="block valve" namingSystem="String" uidRef="x">String</facilityParent1>
797 + <facilityParent2 kind="block valve" namingSystem="String" uidRef="x">String</facilityParent2>
798 + <facilityAlias namingSystem="String">String</facilityAlias>
799 + <facilityAlias namingSystem="String">String</facilityAlias>
800 + <contextFacility kind="block valve" namingSystem="String" uidRef="x">String</contextFacility>
801 + <contextFacility kind="block valve" namingSystem="String" uidRef="x">String</contextFacility>
802 +
803 +
804 +
805 + <flow>
806 + <kind>production</kind>
807 + <qualifier>metered - fiscal</qualifier>
808 + <version>2012-03-01T03:00:00.0Z</version>
809 + <versionSource>version src 974</versionSource>
810 + <gor uom="Euc">35.52</gor>
811 + <gorMTD uom="m3/m3">15.11</gorMTD>
812 + <waterConcMass uom="%">86.31</waterConcMass>
813 + <waterConcVol uom="ppm">42.86</waterConcVol>
814 + <atmosphere uom="Pa">49.52</atmosphere>
815 + <volumeValue>
816 + <volume status="device failure" uom="m3">773.87</volume>
817 + <grossCalorificValue uom="J/m3">694.44</grossCalorificValue>
818 + <temp uom="K">83.41</temp>
819 + <pres uom="Pa">36.72</pres>
820 + </volumeValue>
821 + <volume status="bad calibration" uom="m3">64.39</volume>
822 + <volumeStd status="bad calibration" uom="m3">43.65</volumeStd>
823 + <flowRate status="bad calibration" uom="m3/s">46.86</flowRate>
824 + <temp uom="K">80.75</temp>
825 + <pres uom="Pa">10.23</pres>
826 + <absoluteMinPres uom="Pa">67.92</absoluteMinPres>
827 + <portDiff uid="a5947ab0-bad4-11e1-9447-c0f8dae91040">
828 + <port uidRef="a5947ab1-bad4-11e1-9b4b-c0f8dae91040">Port 1</port>
829 + <presDiff uom="Pa">15.61</presDiff>
830 + <tempDiff uom="K">30.46</tempDiff>
831 + <chokeSize uom="in/32">38.4</chokeSize>
832 + <chokeRelative uom="%">93.09</chokeRelative>
833 + </portDiff>
834 + <portDiff uid="a5947ab2-bad4-11e1-be41-c0f8dae91040">
835 + <port uidRef="a5947ab3-bad4-11e1-86d2-c0f8dae91040">Port 2</port>
836 + <presDiff uom="Pa">32.92</presDiff>
837 + <tempDiff uom="K">91.82</tempDiff>
838 + <chokeSize uom="in/32">57.24</chokeSize>
839 + <chokeRelative uom="%">20.26</chokeRelative>
840 + </portDiff>
841 + <mass uom="kg">213.07</mass>
842 + <work uom="MJ">863.46</work>
843 + <efficiency uom="%">95.65</efficiency>
844 + <rvp uom="Pa">388.96</rvp>
845 + <tvp uom="bar">383.49</tvp>
846 + <bsw uom="%">81.25</bsw>
847 + <bswPrevious uom="m3/m3">20.74</bswPrevious>
848 + <densityValue>
849 + <density uom="kg/m3">42.98</density>
850 + <temp uom="K">82.61</temp>
851 + <pres uom="Pa">22.5</pres>
852 + </densityValue>
853 + <density uom="kg/m3">388.11</density>
854 + <densityFlowRate uom="Mg/a">292.45</densityFlowRate>
855 + <densityStd uom="kg/m3">321.98</densityStd>
856 + <concentration uom="ppm">74.09</concentration>
857 + <molecularWeight>34.21</molecularWeight>
858 + <weightPercent uom="%">58.88</weightPercent>
859 + <molePercent uom="%">72.41</molePercent>
860 + <moleAmt uom="kmol">25.41</moleAmt>
861 + <sg uom="Euc">10.96</sg>
862 + <hcDewpoint uom="K">187.27</hcDewpoint>
863 + <waterDewpoint uom="K">559.4</waterDewpoint>
864 + <wobbeIndex uom="J/m3">211.0</wobbeIndex>
865 + <grossCalorificValueStd uom="J/m3">362.87</grossCalorificValueStd>
866 + <rvpStabilizedCrude uom="Pa">85.82</rvpStabilizedCrude>
867 + <bswStabilizedCrude uom="Euc">659.87</bswStabilizedCrude>
868 + <densityStabilizedCrude uom="kg/m3">806.3</densityStabilizedCrude>
869 + <product>
870 + <kind>oil - net</kind>
871 + <name namingSystem="TEST722">Test product name 264</name>
872 + <splitFactor>0.68</splitFactor>
873 + <gor uom="Euc">22.25</gor>
874 + <gorMTD uom="m3/m3">33.7</gorMTD>
875 + <waterConcMass uom="%">74.49</waterConcMass>
876 + <waterConcVol uom="ppm">75.39</waterConcVol>
877 + <atmosphere uom="Pa">44.42</atmosphere>
878 + <volumeValue>
879 + <volume status="range limit" uom="m3">221.51</volume>
880 + <grossCalorificValue uom="J/m3">981.59</grossCalorificValue>
881 + <temp uom="K">96.24</temp>
882 + <pres uom="Pa">57.34</pres>
883 + </volumeValue>
884 + <volume status="bad calibration" uom="m3">11.95</volume>
885 + <volumeStd status="bad calibration" uom="m3">39.14</volumeStd>
886 + <flowRate status="bad calibration" uom="m3/s">89.55</flowRate>
887 + <temp uom="K">21.21</temp>
888 + <pres uom="Pa">91.15</pres>
889 + <absoluteMinPres uom="Pa">35.26</absoluteMinPres>
890 + <portDiff uid="a594a1c0-bad4-11e1-86bc-c0f8dae91040">
891 + <port uidRef="a594a1c1-bad4-11e1-8aa4-c0f8dae91040">Port 1</port>
892 + <presDiff uom="Pa">95.52</presDiff>
893 + <tempDiff uom="K">80.2</tempDiff>
894 + <chokeSize uom="in/32">70.18</chokeSize>
895 + <chokeRelative uom="%">96.53</chokeRelative>
896 + </portDiff>
897 + <portDiff uid="a594a1c2-bad4-11e1-95a9-c0f8dae91040">
898 + <port uidRef="a594a1c3-bad4-11e1-8626-c0f8dae91040">Port 2</port>
899 + <presDiff uom="Pa">26.71</presDiff>
900 + <tempDiff uom="K">60.83</tempDiff>
901 + <chokeSize uom="in/32">99.35</chokeSize>
902 + <chokeRelative uom="%">10.64</chokeRelative>
903 + </portDiff>
904 + <mass uom="kg">110.74</mass>
905 + <work uom="MJ">133.41</work>
906 + <efficiency uom="%">57.52</efficiency>
907 + <rvp uom="Pa">53.23</rvp>
908 + <tvp uom="bar">67.55</tvp>
909 + <bsw uom="%">86.16</bsw>
910 + <bswPrevious uom="m3/m3">94.84</bswPrevious>
911 + <densityValue>
912 + <density uom="kg/m3">522.77</density>
913 + <temp uom="K">76.29</temp>
914 + <pres uom="Pa">44.64</pres>
915 + </densityValue>
916 + <density uom="kg/m3">207.66</density>
917 + <densityFlowRate uom="Mg/a">566.19</densityFlowRate>
918 + <densityStd uom="kg/m3">699.91</densityStd>
919 + <concentration uom="ppm">47.12</concentration>
920 + <molecularWeight>15.04</molecularWeight>
921 + <weightPercent uom="%">41.72</weightPercent>
922 + <molePercent uom="%">17.4</molePercent>
923 + <moleAmt uom="kmol">96.63</moleAmt>
924 + <sg uom="Euc">66.52</sg>
925 + <hcDewpoint uom="K">41.98</hcDewpoint>
926 + <waterDewpoint uom="K">336.3</waterDewpoint>
927 + <wobbeIndex uom="J/m3">454.09</wobbeIndex>
928 + <grossCalorificValueStd uom="J/m3">582.25</grossCalorificValueStd>
929 + <rvpStabilizedCrude uom="Pa">471.59</rvpStabilizedCrude>
930 + <bswStabilizedCrude uom="Euc">201.79</bswStabilizedCrude>
931 + <densityStabilizedCrude uom="kg/m3">539.47</densityStabilizedCrude>
932 + <componentContent uid="a594c8cf-bad4-11e1-8f50-c0f8dae91040">
933 + <kind>C3-</kind>
934 + <referenceKind>carbon monoxide gas</referenceKind>
935 + <gor uom="Euc">30.35</gor>
936 + <gorMTD uom="m3/m3">51.28</gorMTD>
937 + <waterConcMass uom="%">64.57</waterConcMass>
938 + <waterConcVol uom="ppm">81.28</waterConcVol>
939 + <atmosphere uom="Pa">66.69</atmosphere>
940 + <volumeValue>
941 + <volume status="sensor failure" uom="m3">959.72</volume>
942 + <grossCalorificValue uom="J/m3">11.76</grossCalorificValue>
943 + <temp uom="K">62.44</temp>
944 + <pres uom="Pa">79.62</pres>
945 + </volumeValue>
946 + <volume status="bad calibration" uom="m3">34.82</volume>
947 + <volumeStd status="bad calibration" uom="m3">74.11</volumeStd>
948 + <flowRate status="bad calibration" uom="m3/s">30.08</flowRate>
949 + <temp uom="K">52.87</temp>
950 + <pres uom="Pa">12.73</pres>
951 + <absoluteMinPres uom="Pa">70.57</absoluteMinPres>
952 + <portDiff uid="a594c8d0-bad4-11e1-8cab-c0f8dae91040">
953 + <port uidRef="a594c8d1-bad4-11e1-908b-c0f8dae91040">Port 1</port>
954 + <presDiff uom="Pa">25.53</presDiff>
955 + <tempDiff uom="K">24.35</tempDiff>
956 + <chokeSize uom="in/32">11.2</chokeSize>
957 + <chokeRelative uom="%">23.02</chokeRelative>
958 + </portDiff>
959 + <portDiff uid="a594c8d2-bad4-11e1-9d48-c0f8dae91040">
960 + <port uidRef="a594c8d3-bad4-11e1-b4df-c0f8dae91040">Port 2</port>
961 + <presDiff uom="Pa">94.62</presDiff>
962 + <tempDiff uom="K">57.81</tempDiff>
963 + <chokeSize uom="in/32">95.45</chokeSize>
964 + <chokeRelative uom="%">14.48</chokeRelative>
965 + </portDiff>
966 + <mass uom="kg">217.15</mass>
967 + <work uom="MJ">544.83</work>
968 + <efficiency uom="%">80.0</efficiency>
969 + <rvp uom="Pa">822.33</rvp>
970 + <tvp uom="bar">110.72</tvp>
971 + <bsw uom="%">72.94</bsw>
972 + <bswPrevious uom="m3/m3">38.75</bswPrevious>
973 + <densityValue>
974 + <density uom="kg/m3">61.45</density>
975 + <temp uom="K">42.07</temp>
976 + <pres uom="Pa">37.24</pres>
977 + </densityValue>
978 + <density uom="kg/m3">400.29</density>
979 + <densityFlowRate uom="Mg/a">386.72</densityFlowRate>
980 + <densityStd uom="kg/m3">557.07</densityStd>
981 + <concentration uom="ppm">54.38</concentration>
982 + <molecularWeight>93.53</molecularWeight>
983 + <weightPercent uom="%">14.75</weightPercent>
984 + <molePercent uom="%">67.24</molePercent>
985 + <moleAmt uom="kmol">55.84</moleAmt>
986 + <sg uom="Euc">16.33</sg>
987 + <hcDewpoint uom="K">455.97</hcDewpoint>
988 + <waterDewpoint uom="K">503.48</waterDewpoint>
989 + <wobbeIndex uom="J/m3">248.34</wobbeIndex>
990 + <grossCalorificValueStd uom="J/m3">288.75</grossCalorificValueStd>
991 + <rvpStabilizedCrude uom="Pa">210.29</rvpStabilizedCrude>
992 + <bswStabilizedCrude uom="Euc">51.57</bswStabilizedCrude>
993 + <densityStabilizedCrude uom="kg/m3">88.47</densityStabilizedCrude>
994 + </componentContent>
995 + <period>
996 + <kind>day</kind>
997 + <dateStart>2012-03-01</dateStart>
998 + <dateEnd>2012-03-01</dateEnd>
999 + <gor uom="Euc">56.93</gor>
1000 + <gorMTD uom="m3/m3">70.62</gorMTD>
1001 + <waterConcMass uom="%">70.7</waterConcMass>
1002 + <waterConcVol uom="ppm">83.9</waterConcVol>
1003 + <atmosphere uom="Pa">92.59</atmosphere>
1004 + <volumeValue>
1005 +
1006 + <volume uom="m3">1853.88</volume><temp uom="degC">15</temp>
1007 + <pres uom="atm">1</pres>
1008 + </volumeValue>
1009 + <volume status="bad calibration" uom="m3">67.54</volume>
1010 + <volumeStd status="bad calibration" uom="m3">55.21</volumeStd>
1011 + <flowRate status="bad calibration" uom="m3/s">22.02</flowRate>
1012 + <temp uom="K">66.91</temp>
1013 + <pres uom="Pa">27.85</pres>
1014 + <absoluteMinPres uom="Pa">58.11</absoluteMinPres>
1015 +
1016 + <mass uom="kg">285.7</mass>
1017 + <work uom="kW.h">249.53</work>
1018 + <efficiency uom="%">19.28</efficiency>
1019 + <rvp uom="kPa">81.84</rvp>
1020 + <tvp uom="bar">252.87</tvp>
1021 + <bsw uom="%">36.37</bsw>
1022 + <bswPrevious uom="m3/m3">35.58</bswPrevious>
1023 + <densityValue>
1024 +
1025 + <density uom="kg/m3">786.28</density>
1026 + <temp uom="degC">15</temp>
1027 + <pres uom="atm">1</pres>
1028 + </densityValue>
1029 + <density uom="kg/m3">154.18</density>
1030 + <densityFlowRate uom="Mg/a">478.7</densityFlowRate>
1031 + <densityStd uom="kg/m3">677.04</densityStd>
1032 + <concentration uom="ppm">44.83</concentration>
1033 + <molecularWeight>70.05</molecularWeight>
1034 + <weightPercent uom="%">17.38</weightPercent>
1035 + <molePercent uom="%">51.33</molePercent>
1036 + <moleAmt uom="kmol">96.78</moleAmt>
1037 + <sg uom="Euc">78.21</sg>
1038 + <hcDewpoint uom="K">93.29</hcDewpoint>
1039 + <waterDewpoint uom="K">234.47</waterDewpoint>
1040 + <wobbeIndex uom="J/m3">116.04</wobbeIndex>
1041 + <grossCalorificValueStd uom="J/m3">450.28</grossCalorificValueStd>
1042 + <rvpStabilizedCrude uom="Pa">839.37</rvpStabilizedCrude>
1043 + <bswStabilizedCrude uom="Euc">504.28</bswStabilizedCrude>
1044 + <densityStabilizedCrude uom="kg/m3">993.31</densityStabilizedCrude>
1045 + </period>
1046 +
1047 + </product>
1048 + </flow>
1049 +
1050 +
1051 +
1052 + <flow>
1053 + <kind>injection</kind>
1054 + <qualifier>metered - fiscal</qualifier>
1055 + <version>2012-03-01T19:00:00.0Z</version>
1056 + <versionSource>version src 794</versionSource>
1057 + <gor uom="Euc">46.49</gor>
1058 + <gorMTD uom="m3/m3">92.08</gorMTD>
1059 + <waterConcMass uom="%">20.43</waterConcMass>
1060 + <waterConcVol uom="ppm">32.44</waterConcVol>
1061 + <atmosphere uom="Pa">21.72</atmosphere>
1062 + <volumeValue>
1063 + <volume status="range limit" uom="m3">948.52</volume>
1064 + <grossCalorificValue uom="J/m3">627.63</grossCalorificValue>
1065 + <temp uom="K">30.09</temp>
1066 + <pres uom="Pa">20.19</pres>
1067 + </volumeValue>
1068 + <volume status="bad calibration" uom="m3">96.76</volume>
1069 + <volumeStd status="bad calibration" uom="m3">53.67</volumeStd>
1070 + <flowRate status="bad calibration" uom="m3/s">44.96</flowRate>
1071 + <temp uom="K">17.72</temp>
1072 + <pres uom="Pa">46.28</pres>
1073 + <absoluteMinPres uom="Pa">64.07</absoluteMinPres>
1074 + <portDiff uid="a594efde-bad4-11e1-86cc-c0f8dae91040">
1075 + <port uidRef="a594efdf-bad4-11e1-91c2-c0f8dae91040">Port 1</port>
1076 + <presDiff uom="Pa">96.58</presDiff>
1077 + <tempDiff uom="K">79.73</tempDiff>
1078 + <chokeSize uom="in/32">20.6</chokeSize>
1079 + <chokeRelative uom="%">31.66</chokeRelative>
1080 + </portDiff>
1081 + <portDiff uid="a594efe0-bad4-11e1-bc0c-c0f8dae91040">
1082 + <port uidRef="a594efe1-bad4-11e1-8572-c0f8dae91040">Port 2</port>
1083 + <presDiff uom="Pa">40.89</presDiff>
1084 + <tempDiff uom="K">23.78</tempDiff>
1085 + <chokeSize uom="in/32">34.33</chokeSize>
1086 + <chokeRelative uom="%">28.36</chokeRelative>
1087 + </portDiff>
1088 + <mass uom="kg">187.26</mass>
1089 + <work uom="MJ">405.07</work>
1090 + <efficiency uom="%">28.9</efficiency>
1091 + <rvp uom="Pa">177.55</rvp>
1092 + <tvp uom="bar">274.51</tvp>
1093 + <bsw uom="%">92.53</bsw>
1094 + <bswPrevious uom="m3/m3">83.52</bswPrevious>
1095 + <densityValue>
1096 + <density uom="kg/m3">559.56</density>
1097 + <temp uom="K">56.64</temp>
1098 + <pres uom="Pa">83.99</pres>
1099 + </densityValue>
1100 + <density uom="kg/m3">193.63</density>
1101 + <densityFlowRate uom="Mg/a">81.49</densityFlowRate>
1102 + <densityStd uom="kg/m3">248.0</densityStd>
1103 + <concentration uom="ppm">78.23</concentration>
1104 + <molecularWeight>33.74</molecularWeight>
1105 + <weightPercent uom="%">16.32</weightPercent>
1106 + <molePercent uom="%">75.53</molePercent>
1107 + <moleAmt uom="kmol">58.38</moleAmt>
1108 + <sg uom="Euc">52.82</sg>
1109 + <hcDewpoint uom="K">568.81</hcDewpoint>
1110 + <waterDewpoint uom="K">289.99</waterDewpoint>
1111 + <wobbeIndex uom="J/m3">761.31</wobbeIndex>
1112 + <grossCalorificValueStd uom="J/m3">77.95</grossCalorificValueStd>
1113 + <rvpStabilizedCrude uom="Pa">857.14</rvpStabilizedCrude>
1114 + <bswStabilizedCrude uom="Euc">641.83</bswStabilizedCrude>
1115 + <densityStabilizedCrude uom="kg/m3">877.1</densityStabilizedCrude>
1116 + <product>
1117 + <kind>oil - net</kind>
1118 + <name namingSystem="TEST461">Test product name 963</name>
1119 + <splitFactor>0.88</splitFactor>
1120 + <gor uom="Euc">85.02</gor>
1121 + <gorMTD uom="m3/m3">65.93</gorMTD>
1122 + <waterConcMass uom="%">52.36</waterConcMass>
1123 + <waterConcVol uom="ppm">57.95</waterConcVol>
1124 + <atmosphere uom="Pa">64.13</atmosphere>
1125 + <volumeValue>
1126 + <volume status="range limit" uom="m3">146.14</volume>
1127 + <grossCalorificValue uom="J/m3">391.77</grossCalorificValue>
1128 + <temp uom="K">51.18</temp>
1129 + <pres uom="Pa">65.31</pres>
1130 + </volumeValue>
1131 + <volume status="bad calibration" uom="m3">62.37</volume>
1132 + <volumeStd status="bad calibration" uom="m3">34.97</volumeStd>
1133 + <flowRate status="bad calibration" uom="m3/s">61.68</flowRate>
1134 + <temp uom="K">31.15</temp>
1135 + <pres uom="Pa">58.89</pres>
1136 + <absoluteMinPres uom="Pa">68.44</absoluteMinPres>
1137 + <portDiff uid="a59516f0-bad4-11e1-b4d5-c0f8dae91040">
1138 + <port uidRef="a59516f1-bad4-11e1-8ab5-c0f8dae91040">Port 1</port>
1139 + <presDiff uom="Pa">87.12</presDiff>
1140 + <tempDiff uom="K">12.2</tempDiff>
1141 + <chokeSize uom="in/32">46.71</chokeSize>
1142 + <chokeRelative uom="%">78.09</chokeRelative>
1143 + </portDiff>
1144 + <portDiff uid="a59516f2-bad4-11e1-9b39-c0f8dae91040">
1145 + <port uidRef="a59516f3-bad4-11e1-8b42-c0f8dae91040">Port 2</port>
1146 + <presDiff uom="Pa">75.38</presDiff>
1147 + <tempDiff uom="K">48.86</tempDiff>
1148 + <chokeSize uom="in/32">24.95</chokeSize>
1149 + <chokeRelative uom="%">60.77</chokeRelative>
1150 + </portDiff>
1151 + <mass uom="kg">288.91</mass>
1152 + <work uom="MJ">14.37</work>
1153 + <efficiency uom="%">60.8</efficiency>
1154 + <rvp uom="Pa">805.05</rvp>
1155 + <tvp uom="bar">499.5</tvp>
1156 + <bsw uom="%">85.77</bsw>
1157 + <bswPrevious uom="m3/m3">55.49</bswPrevious>
1158 + <densityValue>
1159 + <density uom="kg/m3">494.4</density>
1160 + <temp uom="K">70.43</temp>
1161 + <pres uom="Pa">59.66</pres>
1162 + </densityValue>
1163 + <density uom="kg/m3">663.33</density>
1164 + <densityFlowRate uom="Mg/a">170.49</densityFlowRate>
1165 + <densityStd uom="kg/m3">251.24</densityStd>
1166 + <concentration uom="ppm">48.7</concentration>
1167 + <molecularWeight>71.03</molecularWeight>
1168 + <weightPercent uom="%">47.07</weightPercent>
1169 + <molePercent uom="%">47.44</molePercent>
1170 + <moleAmt uom="kmol">26.12</moleAmt>
1171 + <sg uom="Euc">70.4</sg>
1172 + <hcDewpoint uom="K">177.28</hcDewpoint>
1173 + <waterDewpoint uom="K">775.28</waterDewpoint>
1174 + <wobbeIndex uom="J/m3">556.7</wobbeIndex>
1175 + <grossCalorificValueStd uom="J/m3">585.16</grossCalorificValueStd>
1176 + <rvpStabilizedCrude uom="Pa">549.22</rvpStabilizedCrude>
1177 + <bswStabilizedCrude uom="Euc">124.52</bswStabilizedCrude>
1178 + <densityStabilizedCrude uom="kg/m3">540.43</densityStabilizedCrude>
1179 + <componentContent uid="a59516f4-bad4-11e1-90c0-c0f8dae91040">
1180 + <kind>aqueous</kind>
1181 + <referenceKind>neopentane</referenceKind>
1182 + <gor uom="Euc">53.44</gor>
1183 + <gorMTD uom="m3/m3">47.79</gorMTD>
1184 + <waterConcMass uom="%">96.69</waterConcMass>
1185 + <waterConcVol uom="ppm">79.13</waterConcVol>
1186 + <atmosphere uom="Pa">63.3</atmosphere>
1187 + <volumeValue>
1188 + <volume status="sensor failure" uom="m3">57.17</volume>
1189 + <grossCalorificValue uom="J/m3">264.73</grossCalorificValue>
1190 + <temp uom="K">11.05</temp>
1191 + <pres uom="Pa">84.52</pres>
1192 + </volumeValue>
1193 + <volume status="bad calibration" uom="m3">79.24</volume>
1194 + <volumeStd status="bad calibration" uom="m3">90.56</volumeStd>
1195 + <flowRate status="bad calibration" uom="m3/s">42.01</flowRate>
1196 + <temp uom="K">27.55</temp>
1197 + <pres uom="Pa">47.34</pres>
1198 + <absoluteMinPres uom="Pa">75.07</absoluteMinPres>
1199 + <portDiff uid="a59516f5-bad4-11e1-9971-c0f8dae91040">
1200 + <port uidRef="a5953e00-bad4-11e1-9080-c0f8dae91040">Port 1</port>
1201 + <presDiff uom="Pa">65.18</presDiff>
1202 + <tempDiff uom="K">92.33</tempDiff>
1203 + <chokeSize uom="in/32">49.71</chokeSize>
1204 + <chokeRelative uom="%">16.17</chokeRelative>
1205 + </portDiff>
1206 + <portDiff uid="a5953e01-bad4-11e1-ac32-c0f8dae91040">
1207 + <port uidRef="a5953e02-bad4-11e1-93d8-c0f8dae91040">Port 2</port>
1208 + <presDiff uom="Pa">89.36</presDiff>
1209 + <tempDiff uom="K">46.85</tempDiff>
1210 + <chokeSize uom="in/32">89.93</chokeSize>
1211 + <chokeRelative uom="%">43.86</chokeRelative>
1212 + </portDiff>
1213 + <mass uom="kg">742.25</mass>
1214 + <work uom="MJ">656.82</work>
1215 + <efficiency uom="%">27.55</efficiency>
1216 + <rvp uom="Pa">66.57</rvp>
1217 + <tvp uom="bar">543.79</tvp>
1218 + <bsw uom="%">40.6</bsw>
1219 + <bswPrevious uom="m3/m3">15.09</bswPrevious>
1220 + <densityValue>
1221 + <density uom="kg/m3">665.18</density>
1222 + <temp uom="K">37.11</temp>
1223 + <pres uom="Pa">38.39</pres>
1224 + </densityValue>
1225 + <density uom="kg/m3">358.27</density>
1226 + <densityFlowRate uom="Mg/a">525.76</densityFlowRate>
1227 + <densityStd uom="kg/m3">615.11</densityStd>
1228 + <concentration uom="ppm">29.01</concentration>
1229 + <molecularWeight>35.13</molecularWeight>
1230 + <weightPercent uom="%">70.55</weightPercent>
1231 + <molePercent uom="%">64.15</molePercent>
1232 + <moleAmt uom="kmol">81.69</moleAmt>
1233 + <sg uom="Euc">20.94</sg>
1234 + <hcDewpoint uom="K">162.95</hcDewpoint>
1235 + <waterDewpoint uom="K">585.5</waterDewpoint>
1236 + <wobbeIndex uom="J/m3">371.93</wobbeIndex>
1237 + <grossCalorificValueStd uom="J/m3">582.81</grossCalorificValueStd>
1238 + <rvpStabilizedCrude uom="Pa">641.21</rvpStabilizedCrude>
1239 + <bswStabilizedCrude uom="Euc">932.05</bswStabilizedCrude>
1240 + <densityStabilizedCrude uom="kg/m3">172.79</densityStabilizedCrude>
1241 + </componentContent>
1242 + <period>
1243 + <kind>day</kind>
1244 + <dateStart>2012-03-01</dateStart>
1245 + <dateEnd>2012-03-01</dateEnd>
1246 + <gor uom="Euc">19.78</gor>
1247 + <gorMTD uom="m3/m3">37.1</gorMTD>
1248 + <waterConcMass uom="%">65.31</waterConcMass>
1249 + <waterConcVol uom="ppm">25.1</waterConcVol>
1250 + <atmosphere uom="Pa">87.71</atmosphere>
1251 + <volumeValue>
1252 +
1253 + <volume uom="m3">1840.26</volume><temp uom="degC">15</temp>
1254 + <pres uom="atm">1</pres>
1255 + </volumeValue>
1256 + <volume status="bad calibration" uom="m3">46.21</volume>
1257 + <volumeStd status="bad calibration" uom="m3">91.31</volumeStd>
1258 + <flowRate status="bad calibration" uom="m3/s">83.51</flowRate>
1259 + <temp uom="K">94.43</temp>
1260 + <pres uom="Pa">49.54</pres>
1261 + <absoluteMinPres uom="Pa">95.99</absoluteMinPres>
1262 +
1263 + <mass uom="kg">227.68</mass>
1264 + <work uom="J">673.21</work>
1265 + <efficiency uom="%">95.47</efficiency>
1266 + <rvp uom="atm">913.47</rvp>
1267 + <tvp uom="bar">66.26</tvp>
1268 + <bsw uom="%">11.43</bsw>
1269 + <bswPrevious uom="m3/m3">17.01</bswPrevious>
1270 + <densityValue>
1271 +
1272 + <density uom="kg/m3">729.18</density>
1273 + <temp uom="degC">15</temp>
1274 + <pres uom="atm">1</pres>
1275 + </densityValue>
1276 + <density uom="kg/m3">22.79</density>
1277 + <densityFlowRate uom="Mg/a">552.38</densityFlowRate>
1278 + <densityStd uom="kg/m3">648.4</densityStd>
1279 + <concentration uom="ppm">18.68</concentration>
1280 + <molecularWeight>70.94</molecularWeight>
1281 + <weightPercent uom="%">75.94</weightPercent>
1282 + <molePercent uom="%">95.19</molePercent>
1283 + <moleAmt uom="kmol">39.95</moleAmt>
1284 + <sg uom="Euc">66.04</sg>
1285 + <hcDewpoint uom="K">510.83</hcDewpoint>
1286 + <waterDewpoint uom="K">758.31</waterDewpoint>
1287 + <wobbeIndex uom="J/m3">22.63</wobbeIndex>
1288 + <grossCalorificValueStd uom="J/m3">439.77</grossCalorificValueStd>
1289 + <rvpStabilizedCrude uom="Pa">161.28</rvpStabilizedCrude>
1290 + <bswStabilizedCrude uom="Euc">103.29</bswStabilizedCrude>
1291 + <densityStabilizedCrude uom="kg/m3">600.54</densityStabilizedCrude>
1292 + </period>
1293 +
1294 + </product>
1295 + </flow>
1296 +
1297 +
1298 +
1299 +
1300 + </facility>
1301 + </object></objects>
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