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David Price
26a4e8f9 1 parent 0c9be1fb

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

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Showing 2 changed files with 653 additions and 2 deletions
...@@ -80,10 +80,10 @@ WHERE { ...@@ -80,10 +80,10 @@ WHERE {
80 80
81 81
82 <dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:ProductionVolumes" /> 82 <dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:ProductionVolumes" />
83 -<!-- <dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:ProductFlows" /> --> 83 +<dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:ProductFlows" />
84 /> 84 />
85 <dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:InjectionVolumes" /> 85 <dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:InjectionVolumes" />
86 -<!-- <dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:ProductFlowsInjection" /> --> 86 + <dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:ProductFlowsInjection" />
87 87
88 <dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:ImportVolumes" /> 88 <dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:ImportVolumes" />
89 <dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:ProductFlowsImport" /> 89 <dprswp:Table arg:report="{= ?report }" arg:template="dpr-tables:ProductFlowsImport" />
......
1 +<?xml version="1.0" encoding="UTF-8"?>
2 +<objects xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance"
3 + xmlns="http://www.epim.no/schemas/mprml/1" version="1.0(MPRML)">
4 + <documentInfo>
5 + <DocumentName namingSystem="EC">TRYM February 2012</DocumentName>
6 + <DocumentAlias namingSystem="EC">TRYM Copex Report</DocumentAlias>
7 + <DocumentDate>2012-03-04T00:00:00.0Z</DocumentDate>
8 + <documentClass namingSystem="EC">Dong E&amp;P Norge AS</documentClass>
9 + <documentClass namingSystem="EC">DPR 2.0</documentClass>
10 + <documentClass namingSystem="ERH">dpr2</documentClass>
11 + <FileCreationInformation>
12 +
13 + <FileCreationDate>2012-03-14T00:00:00.0Z</FileCreationDate>
14 +
15 + <SoftwareName>Energy Components</SoftwareName>
16 + <FileCreator>Dong E&amp;P Norge AS</FileCreator>
17 + <Comment>NA</Comment>
18 + </FileCreationInformation>
19 + <Owner>Dong E&amp;P Norge AS</Owner>
20 + </documentInfo>
21 + <context xsi:type="obj_report">
22 + <kind>DPR 2.0</kind>
23 +
24 + <title>TRYM</title>
25 + <date>2012-02-28</date>
26 + <dateEnd>2012-02-28</dateEnd>
27 + <month>2012-02</month>
28 + <year>2012</year>
29 + <reportVersion>1.2</reportVersion>
30 + <reportStatus>final</reportStatus>
31 + <installation kind="field" namingSystem="NPD" uidRef="18081500">TRYM</installation>
32 + <operator>
33 + <name>Dong E&amp;P Norge AS</name>
34 + <role>Operating company</role>
35 + </operator>
36 + </context>
37 + <object xsi:type="obj_productVolume">
38 + <name>TRYM</name>
39 + <installation kind="field" namingSystem="NPD" uidRef="18081500">TRYM</installation><facility>
40 + <name kind="flow meter" namingSystem="DONG" uidRef="NaN">MPD5</name>
41 + <facilityParent1 namingSystem="String" uidRef="x" kind="block valve">String</facilityParent1>
42 + <facilityParent2 namingSystem="String" uidRef="x" kind="block valve">String</facilityParent2>
43 + <facilityAlias namingSystem="String">String</facilityAlias>
44 + <facilityAlias namingSystem="String">String</facilityAlias>
45 + <contextFacility namingSystem="String" uidRef="x" kind="block valve">String</contextFacility>
46 + <contextFacility namingSystem="String" uidRef="x" kind="block valve">String</contextFacility>
47 +
48 +
49 +
50 + <flow>
51 + <kind>production</kind>
52 + <qualifier>metered - fiscal</qualifier>
53 + <version>2012-02-28T21:00:00.0Z</version>
54 + <versionSource>version src 726</versionSource>
55 + <gor uom="Euc">55.81</gor>
56 + <gorMTD uom="m3/m3">95.86</gorMTD>
57 + <waterConcMass uom="%">99.52</waterConcMass>
58 + <waterConcVol uom="ppm">27.17</waterConcVol>
59 + <atmosphere uom="Pa">41.37</atmosphere>
60 + <volumeValue>
61 + <volume status="comm failure" uom="m3">339.12</volume>
62 + <grossCalorificValue uom="J/m3">987.06</grossCalorificValue>
63 + <temp uom="K">66.34</temp>
64 + <pres uom="Pa">58.84</pres>
65 + </volumeValue>
66 + <volume status="bad calibration" uom="m3">95.52</volume>
67 + <volumeStd status="bad calibration" uom="m3">40.08</volumeStd>
68 + <flowRate status="bad calibration" uom="m3/s">82.26</flowRate>
69 + <temp uom="K">42.37</temp>
70 + <pres uom="Pa">49.16</pres>
71 + <absoluteMinPres uom="Pa">88.0</absoluteMinPres>
72 + <portDiff uid="f69e7840-12d9-11e2-9fb0-d067e534860e">
73 + <port uidRef="f69e7841-12d9-11e2-a6f4-d067e534860e">Port 1</port>
74 + <presDiff uom="Pa">87.58</presDiff>
75 + <tempDiff uom="K">57.77</tempDiff>
76 + <chokeSize uom="in/32">48.65</chokeSize>
77 + <chokeRelative uom="%">51.8</chokeRelative>
78 + </portDiff>
79 + <portDiff uid="f69e7842-12d9-11e2-8ef2-d067e534860e">
80 + <port uidRef="f69e7843-12d9-11e2-b996-d067e534860e">Port 2</port>
81 + <presDiff uom="Pa">62.4</presDiff>
82 + <tempDiff uom="K">47.76</tempDiff>
83 + <chokeSize uom="in/32">13.91</chokeSize>
84 + <chokeRelative uom="%">36.32</chokeRelative>
85 + </portDiff>
86 + <mass uom="kg">228.08</mass>
87 + <work uom="MJ">734.51</work>
88 + <efficiency uom="%">82.97</efficiency>
89 + <rvp uom="Pa">495.36</rvp>
90 + <tvp uom="bar">933.07</tvp>
91 + <bsw uom="%">39.55</bsw>
92 + <bswPrevious uom="m3/m3">10.83</bswPrevious>
93 + <densityValue>
94 + <density uom="kg/m3">223.18</density>
95 + <temp uom="K">38.89</temp>
96 + <pres uom="Pa">96.93</pres>
97 + </densityValue>
98 + <density uom="kg/m3">646.61</density>
99 + <densityFlowRate uom="Mg/a">203.95</densityFlowRate>
100 + <densityStd uom="kg/m3">683.08</densityStd>
101 + <concentration uom="ppm">35.23</concentration>
102 + <molecularWeight>91.21</molecularWeight>
103 + <weightPercent uom="%">69.45</weightPercent>
104 + <molePercent uom="%">75.76</molePercent>
105 + <moleAmt uom="kmol">84.87</moleAmt>
106 + <sg uom="Euc">53.08</sg>
107 + <hcDewpoint uom="K">537.34</hcDewpoint>
108 + <waterDewpoint uom="K">809.28</waterDewpoint>
109 + <wobbeIndex uom="J/m3">118.37</wobbeIndex>
110 + <grossCalorificValueStd uom="J/m3">491.47</grossCalorificValueStd>
111 + <rvpStabilizedCrude uom="Pa">270.17</rvpStabilizedCrude>
112 + <bswStabilizedCrude uom="Euc">73.17</bswStabilizedCrude>
113 + <densityStabilizedCrude uom="kg/m3">365.74</densityStabilizedCrude>
114 + <product>
115 + <kind>oil - gross</kind>
116 + <name namingSystem="TEST484">Test product name 791</name>
117 + <splitFactor>0.29</splitFactor>
118 + <gor uom="Euc">43.79</gor>
119 + <gorMTD uom="m3/m3">38.14</gorMTD>
120 + <waterConcMass uom="%">46.18</waterConcMass>
121 + <waterConcVol uom="ppm">39.2</waterConcVol>
122 + <atmosphere uom="Pa">79.21</atmosphere>
123 + <volumeValue>
124 + <volume status="comm failure" uom="m3">915.72</volume>
125 + <grossCalorificValue uom="J/m3">244.95</grossCalorificValue>
126 + <temp uom="K">68.94</temp>
127 + <pres uom="Pa">33.34</pres>
128 + </volumeValue>
129 + <volume status="bad calibration" uom="m3">23.78</volume>
130 + <volumeStd status="bad calibration" uom="m3">77.03</volumeStd>
131 + <flowRate status="bad calibration" uom="m3/s">46.36</flowRate>
132 + <temp uom="K">13.23</temp>
133 + <pres uom="Pa">34.92</pres>
134 + <absoluteMinPres uom="Pa">36.61</absoluteMinPres>
135 + <portDiff uid="f69e9f51-12d9-11e2-b954-d067e534860e">
136 + <port uidRef="f69e9f52-12d9-11e2-b96d-d067e534860e">Port 1</port>
137 + <presDiff uom="Pa">29.48</presDiff>
138 + <tempDiff uom="K">35.77</tempDiff>
139 + <chokeSize uom="in/32">65.85</chokeSize>
140 + <chokeRelative uom="%">65.02</chokeRelative>
141 + </portDiff>
142 + <portDiff uid="f69e9f53-12d9-11e2-b64e-d067e534860e">
143 + <port uidRef="f69e9f54-12d9-11e2-bbea-d067e534860e">Port 2</port>
144 + <presDiff uom="Pa">54.02</presDiff>
145 + <tempDiff uom="K">99.07</tempDiff>
146 + <chokeSize uom="in/32">64.92</chokeSize>
147 + <chokeRelative uom="%">60.85</chokeRelative>
148 + </portDiff>
149 + <mass uom="kg">195.62</mass>
150 + <work uom="MJ">728.23</work>
151 + <efficiency uom="%">23.73</efficiency>
152 + <rvp uom="Pa">150.85</rvp>
153 + <tvp uom="bar">772.75</tvp>
154 + <bsw uom="%">39.02</bsw>
155 + <bswPrevious uom="m3/m3">34.27</bswPrevious>
156 + <densityValue>
157 + <density uom="kg/m3">552.48</density>
158 + <temp uom="K">39.99</temp>
159 + <pres uom="Pa">26.03</pres>
160 + </densityValue>
161 + <density uom="kg/m3">378.88</density>
162 + <densityFlowRate uom="Mg/a">496.24</densityFlowRate>
163 + <densityStd uom="kg/m3">300.14</densityStd>
164 + <concentration uom="ppm">28.08</concentration>
165 + <molecularWeight>90.61</molecularWeight>
166 + <weightPercent uom="%">65.51</weightPercent>
167 + <molePercent uom="%">57.58</molePercent>
168 + <moleAmt uom="kmol">16.98</moleAmt>
169 + <sg uom="Euc">18.21</sg>
170 + <hcDewpoint uom="K">261.68</hcDewpoint>
171 + <waterDewpoint uom="K">664.2</waterDewpoint>
172 + <wobbeIndex uom="J/m3">635.05</wobbeIndex>
173 + <grossCalorificValueStd uom="J/m3">976.34</grossCalorificValueStd>
174 + <rvpStabilizedCrude uom="Pa">931.43</rvpStabilizedCrude>
175 + <bswStabilizedCrude uom="Euc">596.37</bswStabilizedCrude>
176 + <densityStabilizedCrude uom="kg/m3">678.95</densityStabilizedCrude>
177 + <componentContent uid="f69e9f55-12d9-11e2-bda3-d067e534860e">
178 + <kind>oil - net</kind>
179 + <referenceKind>vapor</referenceKind>
180 + <gor uom="Euc">64.75</gor>
181 + <gorMTD uom="m3/m3">70.72</gorMTD>
182 + <waterConcMass uom="%">31.95</waterConcMass>
183 + <waterConcVol uom="ppm">88.44</waterConcVol>
184 + <atmosphere uom="Pa">87.8</atmosphere>
185 + <volumeValue>
186 + <volume status="questionable" uom="m3">758.79</volume>
187 + <grossCalorificValue uom="J/m3">743.79</grossCalorificValue>
188 + <temp uom="K">28.91</temp>
189 + <pres uom="Pa">37.78</pres>
190 + </volumeValue>
191 + <volume status="bad calibration" uom="m3">27.49</volume>
192 + <volumeStd status="bad calibration" uom="m3">16.75</volumeStd>
193 + <flowRate status="bad calibration" uom="m3/s">44.69</flowRate>
194 + <temp uom="K">23.86</temp>
195 + <pres uom="Pa">42.98</pres>
196 + <absoluteMinPres uom="Pa">13.58</absoluteMinPres>
197 + <portDiff uid="f69ec661-12d9-11e2-a856-d067e534860e">
198 + <port uidRef="f69ec662-12d9-11e2-ba09-d067e534860e">Port 1</port>
199 + <presDiff uom="Pa">68.14</presDiff>
200 + <tempDiff uom="K">30.85</tempDiff>
201 + <chokeSize uom="in/32">19.01</chokeSize>
202 + <chokeRelative uom="%">35.48</chokeRelative>
203 + </portDiff>
204 + <portDiff uid="f69ec663-12d9-11e2-896f-d067e534860e">
205 + <port uidRef="f69ec664-12d9-11e2-9f42-d067e534860e">Port 2</port>
206 + <presDiff uom="Pa">38.84</presDiff>
207 + <tempDiff uom="K">51.72</tempDiff>
208 + <chokeSize uom="in/32">56.47</chokeSize>
209 + <chokeRelative uom="%">53.79</chokeRelative>
210 + </portDiff>
211 + <mass uom="kg">349.36</mass>
212 + <work uom="MJ">235.95</work>
213 + <efficiency uom="%">62.82</efficiency>
214 + <rvp uom="Pa">975.21</rvp>
215 + <tvp uom="bar">878.48</tvp>
216 + <bsw uom="%">26.81</bsw>
217 + <bswPrevious uom="m3/m3">35.68</bswPrevious>
218 + <densityValue>
219 + <density uom="kg/m3">74.09</density>
220 + <temp uom="K">83.37</temp>
221 + <pres uom="Pa">15.41</pres>
222 + </densityValue>
223 + <density uom="kg/m3">414.68</density>
224 + <densityFlowRate uom="Mg/a">621.95</densityFlowRate>
225 + <densityStd uom="kg/m3">618.24</densityStd>
226 + <concentration uom="ppm">25.04</concentration>
227 + <molecularWeight>92.78</molecularWeight>
228 + <weightPercent uom="%">42.47</weightPercent>
229 + <molePercent uom="%">64.66</molePercent>
230 + <moleAmt uom="kmol">98.37</moleAmt>
231 + <sg uom="Euc">77.2</sg>
232 + <hcDewpoint uom="K">84.09</hcDewpoint>
233 + <waterDewpoint uom="K">576.56</waterDewpoint>
234 + <wobbeIndex uom="J/m3">568.53</wobbeIndex>
235 + <grossCalorificValueStd uom="J/m3">925.43</grossCalorificValueStd>
236 + <rvpStabilizedCrude uom="Pa">324.93</rvpStabilizedCrude>
237 + <bswStabilizedCrude uom="Euc">268.91</bswStabilizedCrude>
238 + <densityStabilizedCrude uom="kg/m3">703.27</densityStabilizedCrude>
239 + </componentContent>
240 + <period>
241 + <kind>day</kind>
242 + <dateStart>2012-02-28</dateStart>
243 + <dateEnd>2012-02-28</dateEnd>
244 + <gor uom="Euc">91.18</gor>
245 + <gorMTD uom="m3/m3">50.18</gorMTD>
246 + <waterConcMass uom="%">18.4</waterConcMass>
247 + <waterConcVol uom="ppm">99.56</waterConcVol>
248 + <atmosphere uom="Pa">82.72</atmosphere>
249 + <volumeValue>
250 +
251 + <volume uom="m3">1844.83</volume><temp uom="degC">15</temp>
252 + <pres uom="atm">1</pres>
253 + </volumeValue>
254 + <volume status="bad calibration" uom="m3">21.98</volume>
255 + <volumeStd status="bad calibration" uom="m3">83.58</volumeStd>
256 + <flowRate status="bad calibration" uom="m3/s">44.68</flowRate>
257 + <temp uom="K">62.0</temp>
258 + <pres uom="Pa">57.99</pres>
259 + <absoluteMinPres uom="Pa">98.21</absoluteMinPres>
260 +
261 + <mass uom="kg">900.4</mass>
262 + <work uom="J">510.98</work>
263 + <efficiency uom="%">56.43</efficiency>
264 + <rvp uom="Pa">942.18</rvp>
265 + <tvp uom="bar">171.81</tvp>
266 + <bsw uom="%">21.04</bsw>
267 + <bswPrevious uom="m3/m3">76.96</bswPrevious>
268 + <densityValue>
269 +
270 + <density uom="kg/m3">701.36</density>
271 + <temp uom="degC">15</temp>
272 + <pres uom="atm">1</pres>
273 + </densityValue>
274 + <density uom="kg/m3">329.8</density>
275 + <densityFlowRate uom="Mg/a">466.61</densityFlowRate>
276 + <densityStd uom="kg/m3">139.14</densityStd>
277 + <concentration uom="ppm">28.48</concentration>
278 + <molecularWeight>84.1</molecularWeight>
279 + <weightPercent uom="%">90.22</weightPercent>
280 + <molePercent uom="%">19.83</molePercent>
281 + <moleAmt uom="kmol">30.7</moleAmt>
282 + <sg uom="Euc">60.02</sg>
283 + <hcDewpoint uom="K">143.79</hcDewpoint>
284 + <waterDewpoint uom="K">551.42</waterDewpoint>
285 + <wobbeIndex uom="J/m3">327.48</wobbeIndex>
286 + <grossCalorificValueStd uom="J/m3">501.58</grossCalorificValueStd>
287 + <rvpStabilizedCrude uom="Pa">376.43</rvpStabilizedCrude>
288 + <bswStabilizedCrude uom="Euc">498.53</bswStabilizedCrude>
289 + <densityStabilizedCrude uom="kg/m3">528.55</densityStabilizedCrude>
290 + </period>
291 +
292 + </product><product>
293 + <kind>gas</kind>
294 + <name namingSystem="TEST89">Test product name 134</name>
295 + <splitFactor>0.35</splitFactor>
296 + <gor uom="Euc">81.81</gor>
297 + <gorMTD uom="m3/m3">30.8</gorMTD>
298 + <waterConcMass uom="%">23.14</waterConcMass>
299 + <waterConcVol uom="ppm">54.55</waterConcVol>
300 + <atmosphere uom="Pa">64.06</atmosphere>
301 + <volumeValue>
302 + <volume status="questionable" uom="m3">155.7</volume>
303 + <grossCalorificValue uom="J/m3">565.14</grossCalorificValue>
304 + <temp uom="K">41.76</temp>
305 + <pres uom="Pa">58.9</pres>
306 + </volumeValue>
307 + <volume status="bad calibration" uom="m3">88.77</volume>
308 + <volumeStd status="bad calibration" uom="m3">48.18</volumeStd>
309 + <flowRate status="bad calibration" uom="m3/s">37.2</flowRate>
310 + <temp uom="K">64.54</temp>
311 + <pres uom="Pa">36.49</pres>
312 + <absoluteMinPres uom="Pa">76.62</absoluteMinPres>
313 + <portDiff uid="f69eed70-12d9-11e2-8d9d-d067e534860e">
314 + <port uidRef="f69eed71-12d9-11e2-9b3f-d067e534860e">Port 1</port>
315 + <presDiff uom="Pa">13.53</presDiff>
316 + <tempDiff uom="K">27.0</tempDiff>
317 + <chokeSize uom="in/32">30.02</chokeSize>
318 + <chokeRelative uom="%">70.1</chokeRelative>
319 + </portDiff>
320 + <portDiff uid="f69eed72-12d9-11e2-b723-d067e534860e">
321 + <port uidRef="f69eed73-12d9-11e2-bfbd-d067e534860e">Port 2</port>
322 + <presDiff uom="Pa">38.76</presDiff>
323 + <tempDiff uom="K">33.56</tempDiff>
324 + <chokeSize uom="in/32">39.89</chokeSize>
325 + <chokeRelative uom="%">33.36</chokeRelative>
326 + </portDiff>
327 + <mass uom="kg">424.13</mass>
328 + <work uom="MJ">471.08</work>
329 + <efficiency uom="%">93.23</efficiency>
330 + <rvp uom="Pa">343.49</rvp>
331 + <tvp uom="bar">629.63</tvp>
332 + <bsw uom="%">99.94</bsw>
333 + <bswPrevious uom="m3/m3">37.07</bswPrevious>
334 + <densityValue>
335 + <density uom="kg/m3">690.34</density>
336 + <temp uom="K">41.0</temp>
337 + <pres uom="Pa">51.18</pres>
338 + </densityValue>
339 + <density uom="kg/m3">38.48</density>
340 + <densityFlowRate uom="Mg/a">182.48</densityFlowRate>
341 + <densityStd uom="kg/m3">586.26</densityStd>
342 + <concentration uom="ppm">55.22</concentration>
343 + <molecularWeight>52.44</molecularWeight>
344 + <weightPercent uom="%">52.12</weightPercent>
345 + <molePercent uom="%">51.16</molePercent>
346 + <moleAmt uom="kmol">12.76</moleAmt>
347 + <sg uom="Euc">74.24</sg>
348 + <hcDewpoint uom="K">925.57</hcDewpoint>
349 + <waterDewpoint uom="K">453.77</waterDewpoint>
350 + <wobbeIndex uom="J/m3">555.38</wobbeIndex>
351 + <grossCalorificValueStd uom="J/m3">840.12</grossCalorificValueStd>
352 + <rvpStabilizedCrude uom="Pa">461.22</rvpStabilizedCrude>
353 + <bswStabilizedCrude uom="Euc">449.05</bswStabilizedCrude>
354 + <densityStabilizedCrude uom="kg/m3">159.86</densityStabilizedCrude>
355 + <componentContent uid="f69f1480-12d9-11e2-a165-d067e534860e">
356 + <kind>gas - rich</kind>
357 + <referenceKind>water</referenceKind>
358 + <gor uom="Euc">23.54</gor>
359 + <gorMTD uom="m3/m3">27.09</gorMTD>
360 + <waterConcMass uom="%">18.96</waterConcMass>
361 + <waterConcVol uom="ppm">24.05</waterConcVol>
362 + <atmosphere uom="Pa">79.31</atmosphere>
363 + <volumeValue>
364 + <volume status="sensor failure" uom="m3">842.51</volume>
365 + <grossCalorificValue uom="J/m3">932.26</grossCalorificValue>
366 + <temp uom="K">10.91</temp>
367 + <pres uom="Pa">77.87</pres>
368 + </volumeValue>
369 + <volume status="bad calibration" uom="m3">43.39</volume>
370 + <volumeStd status="bad calibration" uom="m3">95.9</volumeStd>
371 + <flowRate status="bad calibration" uom="m3/s">10.02</flowRate>
372 + <temp uom="K">18.52</temp>
373 + <pres uom="Pa">73.22</pres>
374 + <absoluteMinPres uom="Pa">11.99</absoluteMinPres>
375 + <portDiff uid="f69f1481-12d9-11e2-990a-d067e534860e">
376 + <port uidRef="f69f1482-12d9-11e2-8fc5-d067e534860e">Port 1</port>
377 + <presDiff uom="Pa">70.59</presDiff>
378 + <tempDiff uom="K">42.92</tempDiff>
379 + <chokeSize uom="in/32">36.46</chokeSize>
380 + <chokeRelative uom="%">94.03</chokeRelative>
381 + </portDiff>
382 + <portDiff uid="f69f1483-12d9-11e2-a8e7-d067e534860e">
383 + <port uidRef="f69f1484-12d9-11e2-8bf6-d067e534860e">Port 2</port>
384 + <presDiff uom="Pa">92.91</presDiff>
385 + <tempDiff uom="K">97.58</tempDiff>
386 + <chokeSize uom="in/32">27.32</chokeSize>
387 + <chokeRelative uom="%">82.78</chokeRelative>
388 + </portDiff>
389 + <mass uom="kg">942.65</mass>
390 + <work uom="MJ">880.63</work>
391 + <efficiency uom="%">49.0</efficiency>
392 + <rvp uom="Pa">950.93</rvp>
393 + <tvp uom="bar">883.82</tvp>
394 + <bsw uom="%">34.92</bsw>
395 + <bswPrevious uom="m3/m3">33.45</bswPrevious>
396 + <densityValue>
397 + <density uom="kg/m3">14.99</density>
398 + <temp uom="K">16.89</temp>
399 + <pres uom="Pa">49.56</pres>
400 + </densityValue>
401 + <density uom="kg/m3">56.3</density>
402 + <densityFlowRate uom="Mg/a">187.6</densityFlowRate>
403 + <densityStd uom="kg/m3">223.77</densityStd>
404 + <concentration uom="ppm">99.99</concentration>
405 + <molecularWeight>94.47</molecularWeight>
406 + <weightPercent uom="%">37.43</weightPercent>
407 + <molePercent uom="%">88.11</molePercent>
408 + <moleAmt uom="kmol">20.01</moleAmt>
409 + <sg uom="Euc">71.85</sg>
410 + <hcDewpoint uom="K">33.41</hcDewpoint>
411 + <waterDewpoint uom="K">164.98</waterDewpoint>
412 + <wobbeIndex uom="J/m3">483.69</wobbeIndex>
413 + <grossCalorificValueStd uom="J/m3">532.71</grossCalorificValueStd>
414 + <rvpStabilizedCrude uom="Pa">908.47</rvpStabilizedCrude>
415 + <bswStabilizedCrude uom="Euc">376.38</bswStabilizedCrude>
416 + <densityStabilizedCrude uom="kg/m3">170.86</densityStabilizedCrude>
417 + </componentContent>
418 + <period>
419 + <kind>day</kind>
420 + <dateStart>2012-02-28</dateStart>
421 + <dateEnd>2012-02-28</dateEnd>
422 + <gor uom="Euc">83.69</gor>
423 + <gorMTD uom="m3/m3">53.5</gorMTD>
424 + <waterConcMass uom="%">58.37</waterConcMass>
425 + <waterConcVol uom="ppm">67.0</waterConcVol>
426 + <atmosphere uom="Pa">30.13</atmosphere>
427 + <volumeValue>
428 +
429 + <volume uom="m3">81.96</volume><temp uom="degC">15</temp>
430 + <pres uom="atm">1</pres>
431 + </volumeValue>
432 + <volume status="bad calibration" uom="m3">50.61</volume>
433 + <volumeStd status="bad calibration" uom="m3">96.63</volumeStd>
434 + <flowRate status="bad calibration" uom="m3/s">60.16</flowRate>
435 + <temp uom="K">45.55</temp>
436 + <pres uom="Pa">12.93</pres>
437 + <absoluteMinPres uom="Pa">51.49</absoluteMinPres>
438 +
439 + <mass uom="kg">316.62</mass>
440 + <work uom="kW.h">38.93</work>
441 + <efficiency uom="%">96.08</efficiency>
442 + <rvp uom="kpsi">287.31</rvp>
443 + <tvp uom="bar">591.38</tvp>
444 + <bsw uom="%">50.89</bsw>
445 + <bswPrevious uom="m3/m3">56.04</bswPrevious>
446 + <densityValue>
447 + <density uom="kg/m3">0.5</density>
448 +
449 + <temp uom="degC">15</temp>
450 + <pres uom="atm">1</pres>
451 + </densityValue>
452 + <density uom="kg/m3">539.46</density>
453 + <densityFlowRate uom="Mg/a">250.26</densityFlowRate>
454 + <densityStd uom="kg/m3">320.16</densityStd>
455 + <concentration uom="ppm">57.74</concentration>
456 + <molecularWeight>63.04</molecularWeight>
457 + <weightPercent uom="%">24.47</weightPercent>
458 + <molePercent uom="%">65.38</molePercent>
459 + <moleAmt uom="kmol">17.54</moleAmt>
460 + <sg uom="Euc">92.05</sg>
461 + <hcDewpoint uom="K">303.28</hcDewpoint>
462 + <waterDewpoint uom="K">964.34</waterDewpoint>
463 + <wobbeIndex uom="J/m3">956.94</wobbeIndex>
464 + <grossCalorificValueStd uom="J/m3">79.96</grossCalorificValueStd>
465 + <rvpStabilizedCrude uom="Pa">324.6</rvpStabilizedCrude>
466 + <bswStabilizedCrude uom="Euc">126.43</bswStabilizedCrude>
467 + <densityStabilizedCrude uom="kg/m3">557.09</densityStabilizedCrude>
468 + </period>
469 +
470 + </product><product>
471 + <kind>water</kind>
472 + <name namingSystem="TEST492">Test product name 655</name>
473 + <splitFactor>0.72</splitFactor>
474 + <gor uom="Euc">10.87</gor>
475 + <gorMTD uom="m3/m3">77.14</gorMTD>
476 + <waterConcMass uom="%">55.98</waterConcMass>
477 + <waterConcVol uom="ppm">54.46</waterConcVol>
478 + <atmosphere uom="Pa">37.76</atmosphere>
479 + <volumeValue>
480 + <volume status="bad calibration" uom="m3">992.46</volume>
481 + <grossCalorificValue uom="J/m3">263.11</grossCalorificValue>
482 + <temp uom="K">16.57</temp>
483 + <pres uom="Pa">52.71</pres>
484 + </volumeValue>
485 + <volume status="bad calibration" uom="m3">89.7</volume>
486 + <volumeStd status="bad calibration" uom="m3">66.59</volumeStd>
487 + <flowRate status="bad calibration" uom="m3/s">26.87</flowRate>
488 + <temp uom="K">20.42</temp>
489 + <pres uom="Pa">28.88</pres>
490 + <absoluteMinPres uom="Pa">63.17</absoluteMinPres>
491 + <portDiff uid="f69f3b8f-12d9-11e2-91f0-d067e534860e">
492 + <port uidRef="f69f3b90-12d9-11e2-b43f-d067e534860e">Port 1</port>
493 + <presDiff uom="Pa">90.36</presDiff>
494 + <tempDiff uom="K">64.66</tempDiff>
495 + <chokeSize uom="in/32">71.9</chokeSize>
496 + <chokeRelative uom="%">24.08</chokeRelative>
497 + </portDiff>
498 + <portDiff uid="f69f3b91-12d9-11e2-a8a0-d067e534860e">
499 + <port uidRef="f69f3b92-12d9-11e2-b517-d067e534860e">Port 2</port>
500 + <presDiff uom="Pa">91.32</presDiff>
501 + <tempDiff uom="K">73.49</tempDiff>
502 + <chokeSize uom="in/32">63.36</chokeSize>
503 + <chokeRelative uom="%">26.84</chokeRelative>
504 + </portDiff>
505 + <mass uom="kg">867.38</mass>
506 + <work uom="MJ">871.2</work>
507 + <efficiency uom="%">34.13</efficiency>
508 + <rvp uom="Pa">442.65</rvp>
509 + <tvp uom="bar">238.71</tvp>
510 + <bsw uom="%">12.41</bsw>
511 + <bswPrevious uom="m3/m3">74.68</bswPrevious>
512 + <densityValue>
513 + <density uom="kg/m3">539.95</density>
514 + <temp uom="K">71.73</temp>
515 + <pres uom="Pa">49.76</pres>
516 + </densityValue>
517 + <density uom="kg/m3">41.59</density>
518 + <densityFlowRate uom="Mg/a">153.51</densityFlowRate>
519 + <densityStd uom="kg/m3">598.39</densityStd>
520 + <concentration uom="ppm">21.95</concentration>
521 + <molecularWeight>12.52</molecularWeight>
522 + <weightPercent uom="%">10.43</weightPercent>
523 + <molePercent uom="%">95.49</molePercent>
524 + <moleAmt uom="kmol">56.42</moleAmt>
525 + <sg uom="Euc">74.0</sg>
526 + <hcDewpoint uom="K">801.24</hcDewpoint>
527 + <waterDewpoint uom="K">969.94</waterDewpoint>
528 + <wobbeIndex uom="J/m3">38.9</wobbeIndex>
529 + <grossCalorificValueStd uom="J/m3">981.48</grossCalorificValueStd>
530 + <rvpStabilizedCrude uom="Pa">515.47</rvpStabilizedCrude>
531 + <bswStabilizedCrude uom="Euc">697.51</bswStabilizedCrude>
532 + <densityStabilizedCrude uom="kg/m3">980.07</densityStabilizedCrude>
533 + <componentContent uid="f69f629e-12d9-11e2-b238-d067e534860e">
534 + <kind>helium gas</kind>
535 + <referenceKind>C6-</referenceKind>
536 + <gor uom="Euc">68.06</gor>
537 + <gorMTD uom="m3/m3">38.09</gorMTD>
538 + <waterConcMass uom="%">62.31</waterConcMass>
539 + <waterConcVol uom="ppm">50.92</waterConcVol>
540 + <atmosphere uom="Pa">31.94</atmosphere>
541 + <volumeValue>
542 + <volume status="questionable" uom="m3">297.12</volume>
543 + <grossCalorificValue uom="J/m3">213.93</grossCalorificValue>
544 + <temp uom="K">97.33</temp>
545 + <pres uom="Pa">94.81</pres>
546 + </volumeValue>
547 + <volume status="bad calibration" uom="m3">11.66</volume>
548 + <volumeStd status="bad calibration" uom="m3">68.73</volumeStd>
549 + <flowRate status="bad calibration" uom="m3/s">68.35</flowRate>
550 + <temp uom="K">33.24</temp>
551 + <pres uom="Pa">78.61</pres>
552 + <absoluteMinPres uom="Pa">31.57</absoluteMinPres>
553 + <portDiff uid="f69f629f-12d9-11e2-82b6-d067e534860e">
554 + <port uidRef="f69f62a0-12d9-11e2-babf-d067e534860e">Port 1</port>
555 + <presDiff uom="Pa">63.63</presDiff>
556 + <tempDiff uom="K">77.25</tempDiff>
557 + <chokeSize uom="in/32">54.35</chokeSize>
558 + <chokeRelative uom="%">51.92</chokeRelative>
559 + </portDiff>
560 + <portDiff uid="f69f62a1-12d9-11e2-8e0f-d067e534860e">
561 + <port uidRef="f69f62a2-12d9-11e2-a28a-d067e534860e">Port 2</port>
562 + <presDiff uom="Pa">85.92</presDiff>
563 + <tempDiff uom="K">44.32</tempDiff>
564 + <chokeSize uom="in/32">98.99</chokeSize>
565 + <chokeRelative uom="%">16.74</chokeRelative>
566 + </portDiff>
567 + <mass uom="kg">301.51</mass>
568 + <work uom="MJ">557.83</work>
569 + <efficiency uom="%">50.41</efficiency>
570 + <rvp uom="Pa">199.92</rvp>
571 + <tvp uom="bar">729.42</tvp>
572 + <bsw uom="%">92.07</bsw>
573 + <bswPrevious uom="m3/m3">54.9</bswPrevious>
574 + <densityValue>
575 + <density uom="kg/m3">186.65</density>
576 + <temp uom="K">52.69</temp>
577 + <pres uom="Pa">92.63</pres>
578 + </densityValue>
579 + <density uom="kg/m3">253.61</density>
580 + <densityFlowRate uom="Mg/a">643.56</densityFlowRate>
581 + <densityStd uom="kg/m3">122.83</densityStd>
582 + <concentration uom="ppm">79.95</concentration>
583 + <molecularWeight>13.99</molecularWeight>
584 + <weightPercent uom="%">49.41</weightPercent>
585 + <molePercent uom="%">97.73</molePercent>
586 + <moleAmt uom="kmol">18.81</moleAmt>
587 + <sg uom="Euc">87.28</sg>
588 + <hcDewpoint uom="K">446.11</hcDewpoint>
589 + <waterDewpoint uom="K">265.29</waterDewpoint>
590 + <wobbeIndex uom="J/m3">35.13</wobbeIndex>
591 + <grossCalorificValueStd uom="J/m3">939.76</grossCalorificValueStd>
592 + <rvpStabilizedCrude uom="Pa">811.94</rvpStabilizedCrude>
593 + <bswStabilizedCrude uom="Euc">432.27</bswStabilizedCrude>
594 + <densityStabilizedCrude uom="kg/m3">200.32</densityStabilizedCrude>
595 + </componentContent>
596 + <period>
597 + <kind>day</kind>
598 + <dateStart>2012-02-28</dateStart>
599 + <dateEnd>2012-02-28</dateEnd>
600 + <gor uom="Euc">14.18</gor>
601 + <gorMTD uom="m3/m3">69.09</gorMTD>
602 + <waterConcMass uom="%">10.12</waterConcMass>
603 + <waterConcVol uom="ppm">33.84</waterConcVol>
604 + <atmosphere uom="Pa">97.44</atmosphere>
605 + <volumeValue>
606 +
607 + <volume uom="m3">93.62</volume><temp uom="degC">15</temp>
608 + <pres uom="atm">1</pres>
609 + </volumeValue>
610 + <volume status="bad calibration" uom="m3">43.01</volume>
611 + <volumeStd status="bad calibration" uom="m3">73.07</volumeStd>
612 + <flowRate status="bad calibration" uom="m3/s">93.19</flowRate>
613 + <temp uom="K">58.9</temp>
614 + <pres uom="Pa">60.81</pres>
615 + <absoluteMinPres uom="Pa">88.81</absoluteMinPres>
616 +
617 +
618 + <work uom="MJ">772.09</work>
619 + <efficiency uom="%">40.88</efficiency>
620 + <rvp uom="kpsi">504.32</rvp>
621 + <tvp uom="bar">481.8</tvp>
622 + <bsw uom="%">35.78</bsw>
623 + <bswPrevious uom="m3/m3">99.21</bswPrevious>
624 +
625 + <density uom="kg/m3">221.11</density>
626 + <densityFlowRate uom="Mg/a">128.23</densityFlowRate>
627 + <densityStd uom="kg/m3">54.54</densityStd>
628 + <concentration uom="ppm">24.08</concentration>
629 + <molecularWeight>43.89</molecularWeight>
630 + <weightPercent uom="%">54.36</weightPercent>
631 + <molePercent uom="%">90.16</molePercent>
632 + <moleAmt uom="kmol">32.38</moleAmt>
633 + <sg uom="Euc">64.29</sg>
634 + <hcDewpoint uom="K">27.64</hcDewpoint>
635 + <waterDewpoint uom="K">112.08</waterDewpoint>
636 + <wobbeIndex uom="J/m3">272.03</wobbeIndex>
637 + <grossCalorificValueStd uom="J/m3">823.1</grossCalorificValueStd>
638 + <rvpStabilizedCrude uom="Pa">101.55</rvpStabilizedCrude>
639 + <bswStabilizedCrude uom="Euc">168.24</bswStabilizedCrude>
640 + <densityStabilizedCrude uom="kg/m3">450.74</densityStabilizedCrude>
641 + </period>
642 +
643 + </product>
644 + </flow>
645 +
646 +
647 +
648 +
649 + </facility>
650 + </object>
651 +</objects>
...\ No newline at end of file ...\ No newline at end of file