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David Price
23945e7a 1 parent 739a1f89

Added a one-flow test file

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1 +<?xml version="1.0" encoding="UTF-8"?>
2 +<objects xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance"
3 + xmlns="http://www.epim.no/schemas/mprml/1" version="1.0(MPRML)">
4 + <documentInfo>
5 + <DocumentName namingSystem="EC">TRYM February 2012</DocumentName>
6 + <DocumentAlias namingSystem="EC">TRYM Copex Report</DocumentAlias>
7 + <DocumentDate>2012-03-05T00:00:00.0Z</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>2012-03-15T00:00:00.0Z</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>2012-02-01</date>
26 + <dateEnd>2012-02-01</dateEnd>
27 + <month>2012-02</month>
28 + <year>2012</year>
29 + <reportVersion>1.1</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>
40 + <facility>
41 + <name kind="field" namingSystem="NPD" uidRef="18081500">TRYM</name>
42 + <facilityParent1 namingSystem="String" uidRef="x" kind="block valve">String</facilityParent1>
43 + <facilityParent2 namingSystem="String" uidRef="x" kind="block valve">String</facilityParent2>
44 + <facilityAlias namingSystem="String">String</facilityAlias>
45 + <facilityAlias namingSystem="String">String</facilityAlias>
46 + <contextFacility namingSystem="String" uidRef="x" kind="block valve">String</contextFacility>
47 + <contextFacility namingSystem="String" uidRef="x" kind="block valve">String</contextFacility>
48 +
49 +
50 + <downtimeReason uid="a5c6a140-8ae8-11e2-b65a-78acc03c3a5e">
51 + <who>MR Who</who>
52 + <role>Platform manager</role>
53 + <dTimStart>2012-02-01T02:00:00.0Z</dTimStart>
54 + <dTimEnd>2012-02-29T04:00:00.0Z</dTimEnd>
55 + <remark>If the position of the trace in (99c) were only relatively inaccessible to movement, a descriptively</remark>
56 + </downtimeReason>
57 + <downtimeReason uid="a5c6a141-8ae8-11e2-abf3-78acc03c3a5e">
58 + <who>Mr Who2</who>
59 + <role>Platform manager 2</role>
60 + <dTimStart>2012-02-01T06:00:00.0Z</dTimStart>
61 + <dTimEnd>2012-02-29T14:00:00.0Z</dTimEnd>
62 + <remark>Let us continue to suppose that the fundamental error of regarding functional notions as categorial </remark>
63 + </downtimeReason>
64 + <flow uid="TRY_SALEABLE_PRODUCTION">
65 + <name>Trym saleable volumes</name>
66 + <kind>production</kind>
67 + <qualifier>saleable</qualifier>
68 + <version>2012-02-01T02:00:00.0Z</version>
69 + <versionSource>version src 255</versionSource>
70 + <gor uom="Euc">48.25</gor>
71 + <gorMTD uom="m3/m3">33.03</gorMTD>
72 + <waterConcMass uom="%">89.99</waterConcMass>
73 + <waterConcVol uom="ppm">72.85</waterConcVol>
74 + <atmosphere uom="Pa">13.71</atmosphere>
75 + <volumeValue>
76 + <volume status="comm failure" uom="m3">134.26</volume>
77 + <grossCalorificValue uom="J/m3">862.8</grossCalorificValue>
78 + <temp uom="K">88.52</temp>
79 + <pres uom="Pa">46.23</pres>
80 + </volumeValue>
81 + <volume status="bad calibration" uom="m3">11.89</volume>
82 + <volumeStd status="bad calibration" uom="m3">15.4</volumeStd>
83 + <flowRate status="bad calibration" uom="m3/s">77.85</flowRate>
84 + <temp uom="K">22.68</temp>
85 + <pres uom="Pa">88.49</pres>
86 + <absoluteMinPres uom="Pa">67.96</absoluteMinPres>
87 + <portDiff uid="a5c6a142-8ae8-11e2-a16c-78acc03c3a5e">
88 + <port uidRef="a5c6a143-8ae8-11e2-9fb7-78acc03c3a5e">Port 1</port>
89 + <presDiff uom="Pa">64.99</presDiff>
90 + <tempDiff uom="K">52.23</tempDiff>
91 + <chokeSize uom="in/32">78.15</chokeSize>
92 + <chokeRelative uom="%">18.46</chokeRelative>
93 + </portDiff>
94 + <portDiff uid="a5c6a144-8ae8-11e2-9abb-78acc03c3a5e">
95 + <port uidRef="a5c6a145-8ae8-11e2-9ed8-78acc03c3a5e">Port 2</port>
96 + <presDiff uom="Pa">79.65</presDiff>
97 + <tempDiff uom="K">31.38</tempDiff>
98 + <chokeSize uom="in/32">61.63</chokeSize>
99 + <chokeRelative uom="%">76.93</chokeRelative>
100 + </portDiff>
101 + <mass uom="kg">741.86</mass>
102 + <work uom="MJ">900.63</work>
103 + <efficiency uom="%">44.64</efficiency>
104 + <rvp uom="Pa">473.2</rvp>
105 + <tvp uom="bar">672.31</tvp>
106 + <bsw uom="%">56.58</bsw>
107 + <bswPrevious uom="m3/m3">34.61</bswPrevious>
108 + <densityValue>
109 + <density uom="kg/m3">37.41</density>
110 + <temp uom="K">53.03</temp>
111 + <pres uom="Pa">79.19</pres>
112 + </densityValue>
113 + <density uom="kg/m3">412.02</density>
114 + <densityFlowRate uom="Mg/a">328.63</densityFlowRate>
115 + <densityStd uom="kg/m3">667.03</densityStd>
116 + <concentration uom="ppm">62.47</concentration>
117 + <molecularWeight>40.34</molecularWeight>
118 + <weightPercent uom="%">38.31</weightPercent>
119 + <molePercent uom="%">53.15</molePercent>
120 + <moleAmt uom="kmol">80.5</moleAmt>
121 + <sg uom="Euc">78.32</sg>
122 + <hcDewpoint uom="K">539.52</hcDewpoint>
123 + <waterDewpoint uom="K">647.14</waterDewpoint>
124 + <wobbeIndex uom="J/m3">703.54</wobbeIndex>
125 + <grossCalorificValueStd uom="J/m3">999.35</grossCalorificValueStd>
126 + <rvpStabilizedCrude uom="Pa">218.7</rvpStabilizedCrude>
127 + <bswStabilizedCrude uom="Euc">473.17</bswStabilizedCrude>
128 + <densityStabilizedCrude uom="kg/m3">90.92</densityStabilizedCrude>
129 + <product>
130 + <kind>oil - net</kind>
131 + <name namingSystem="TEST411">Test product name 187</name>
132 + <splitFactor>0.11</splitFactor>
133 + <gor uom="Euc">82.69</gor>
134 + <gorMTD uom="m3/m3">63.83</gorMTD>
135 + <waterConcMass uom="%">18.93</waterConcMass>
136 + <waterConcVol uom="ppm">63.88</waterConcVol>
137 + <atmosphere uom="Pa">25.5</atmosphere>
138 + <volumeValue>
139 + <volume status="device failure" uom="m3">505.2</volume>
140 + <grossCalorificValue uom="J/m3">619.52</grossCalorificValue>
141 + <temp uom="K">92.1</temp>
142 + <pres uom="Pa">13.05</pres>
143 + </volumeValue>
144 + <volume status="bad calibration" uom="m3">86.05</volume>
145 + <volumeStd status="bad calibration" uom="m3">50.84</volumeStd>
146 + <flowRate status="bad calibration" uom="m3/s">81.66</flowRate>
147 + <temp uom="K">12.39</temp>
148 + <pres uom="Pa">23.36</pres>
149 + <absoluteMinPres uom="Pa">85.53</absoluteMinPres>
150 + <portDiff uid="a5c6a146-8ae8-11e2-a53c-78acc03c3a5e">
151 + <port uidRef="a5c6a147-8ae8-11e2-9d3d-78acc03c3a5e">Port 1</port>
152 + <presDiff uom="Pa">68.18</presDiff>
153 + <tempDiff uom="K">26.62</tempDiff>
154 + <chokeSize uom="in/32">54.61</chokeSize>
155 + <chokeRelative uom="%">53.42</chokeRelative>
156 + </portDiff>
157 + <portDiff uid="a5c6a148-8ae8-11e2-a4d1-78acc03c3a5e">
158 + <port uidRef="a5c6a149-8ae8-11e2-aab3-78acc03c3a5e">Port 2</port>
159 + <presDiff uom="Pa">33.9</presDiff>
160 + <tempDiff uom="K">83.62</tempDiff>
161 + <chokeSize uom="in/32">50.9</chokeSize>
162 + <chokeRelative uom="%">90.59</chokeRelative>
163 + </portDiff>
164 + <mass uom="kg">413.44</mass>
165 + <work uom="MJ">634.56</work>
166 + <efficiency uom="%">76.94</efficiency>
167 + <rvp uom="Pa">659.3</rvp>
168 + <tvp uom="bar">800.3</tvp>
169 + <bsw uom="%">16.46</bsw>
170 + <bswPrevious uom="m3/m3">42.44</bswPrevious>
171 + <densityValue>
172 + <density uom="kg/m3">440.19</density>
173 + <temp uom="K">50.6</temp>
174 + <pres uom="Pa">45.21</pres>
175 + </densityValue>
176 + <density uom="kg/m3">100.46</density>
177 + <densityFlowRate uom="Mg/a">662.64</densityFlowRate>
178 + <densityStd uom="kg/m3">265.49</densityStd>
179 + <concentration uom="ppm">61.62</concentration>
180 + <molecularWeight>59.0</molecularWeight>
181 + <weightPercent uom="%">63.08</weightPercent>
182 + <molePercent uom="%">92.99</molePercent>
183 + <moleAmt uom="kmol">49.5</moleAmt>
184 + <sg uom="Euc">55.69</sg>
185 + <hcDewpoint uom="K">164.87</hcDewpoint>
186 + <waterDewpoint uom="K">865.69</waterDewpoint>
187 + <wobbeIndex uom="J/m3">378.96</wobbeIndex>
188 + <grossCalorificValueStd uom="J/m3">123.58</grossCalorificValueStd>
189 + <rvpStabilizedCrude uom="Pa">57.65</rvpStabilizedCrude>
190 + <bswStabilizedCrude uom="Euc">230.87</bswStabilizedCrude>
191 + <densityStabilizedCrude uom="kg/m3">87.87</densityStabilizedCrude>
192 + <componentContent uid="a5c6a14a-8ae8-11e2-b107-78acc03c3a5e">
193 + <kind>condensate</kind>
194 + <referenceKind>oil</referenceKind>
195 + <gor uom="Euc">60.51</gor>
196 + <gorMTD uom="m3/m3">18.36</gorMTD>
197 + <waterConcMass uom="%">40.9</waterConcMass>
198 + <waterConcVol uom="ppm">86.33</waterConcVol>
199 + <atmosphere uom="Pa">88.88</atmosphere>
200 + <volumeValue>
201 + <volume status="bad calibration" uom="m3">312.64</volume>
202 + <grossCalorificValue uom="J/m3">17.24</grossCalorificValue>
203 + <temp uom="K">71.58</temp>
204 + <pres uom="Pa">84.36</pres>
205 + </volumeValue>
206 + <volume status="bad calibration" uom="m3">60.48</volume>
207 + <volumeStd status="bad calibration" uom="m3">15.54</volumeStd>
208 + <flowRate status="bad calibration" uom="m3/s">52.91</flowRate>
209 + <temp uom="K">52.17</temp>
210 + <pres uom="Pa">62.3</pres>
211 + <absoluteMinPres uom="Pa">12.62</absoluteMinPres>
212 + <portDiff uid="a5c91240-8ae8-11e2-ae52-78acc03c3a5e">
213 + <port uidRef="a5c91241-8ae8-11e2-8794-78acc03c3a5e">Port 1</port>
214 + <presDiff uom="Pa">51.38</presDiff>
215 + <tempDiff uom="K">61.09</tempDiff>
216 + <chokeSize uom="in/32">42.97</chokeSize>
217 + <chokeRelative uom="%">52.18</chokeRelative>
218 + </portDiff>
219 + <portDiff uid="a5c91242-8ae8-11e2-9489-78acc03c3a5e">
220 + <port uidRef="a5c91243-8ae8-11e2-8437-78acc03c3a5e">Port 2</port>
221 + <presDiff uom="Pa">84.67</presDiff>
222 + <tempDiff uom="K">40.75</tempDiff>
223 + <chokeSize uom="in/32">76.06</chokeSize>
224 + <chokeRelative uom="%">88.08</chokeRelative>
225 + </portDiff>
226 + <mass uom="kg">467.73</mass>
227 + <work uom="MJ">840.23</work>
228 + <efficiency uom="%">33.86</efficiency>
229 + <rvp uom="Pa">991.18</rvp>
230 + <tvp uom="bar">755.73</tvp>
231 + <bsw uom="%">78.2</bsw>
232 + <bswPrevious uom="m3/m3">91.4</bswPrevious>
233 + <densityValue>
234 + <density uom="kg/m3">241.87</density>
235 + <temp uom="K">33.79</temp>
236 + <pres uom="Pa">32.72</pres>
237 + </densityValue>
238 + <density uom="kg/m3">576.9</density>
239 + <densityFlowRate uom="Mg/a">105.41</densityFlowRate>
240 + <densityStd uom="kg/m3">55.76</densityStd>
241 + <concentration uom="ppm">20.34</concentration>
242 + <molecularWeight>16.71</molecularWeight>
243 + <weightPercent uom="%">57.89</weightPercent>
244 + <molePercent uom="%">38.67</molePercent>
245 + <moleAmt uom="kmol">67.02</moleAmt>
246 + <sg uom="Euc">21.22</sg>
247 + <hcDewpoint uom="K">715.1</hcDewpoint>
248 + <waterDewpoint uom="K">100.26</waterDewpoint>
249 + <wobbeIndex uom="J/m3">289.8</wobbeIndex>
250 + <grossCalorificValueStd uom="J/m3">363.38</grossCalorificValueStd>
251 + <rvpStabilizedCrude uom="Pa">407.89</rvpStabilizedCrude>
252 + <bswStabilizedCrude uom="Euc">704.82</bswStabilizedCrude>
253 + <densityStabilizedCrude uom="kg/m3">257.23</densityStabilizedCrude>
254 + </componentContent>
255 + <period>
256 + <kind>month</kind>
257 + <dateStart>2012-02-01</dateStart>
258 + <dateEnd>2012-02-29</dateEnd>
259 + <gor uom="Euc">55.03</gor>
260 + <gorMTD uom="m3/m3">71.04</gorMTD>
261 + <waterConcMass uom="%">67.41</waterConcMass>
262 + <waterConcVol uom="ppm">31.52</waterConcVol>
263 + <atmosphere uom="Pa">81.95</atmosphere>
264 + <volumeValue>
265 +
266 + <volume uom="m3">615.87</volume><temp uom="degC">15</temp>
267 + <pres uom="atm">1</pres>
268 + </volumeValue>
269 + <volume status="bad calibration" uom="m3">31.27</volume>
270 + <volumeStd status="bad calibration" uom="m3">43.03</volumeStd>
271 + <flowRate status="bad calibration" uom="m3/s">57.45</flowRate>
272 + <temp uom="K">41.0</temp>
273 + <pres uom="Pa">48.88</pres>
274 + <absoluteMinPres uom="Pa">55.29</absoluteMinPres>
275 +
276 + <mass uom="kg">224.73</mass>
277 + <work uom="kW.h">491.2</work>
278 + <efficiency uom="%">15.12</efficiency>
279 + <rvp uom="kPa">900.96</rvp>
280 + <tvp uom="bar">827.62</tvp>
281 + <bsw uom="%">58.3</bsw>
282 + <bswPrevious uom="m3/m3">51.07</bswPrevious>
283 + <densityValue>
284 +
285 + <density uom="kg/m3">786.94</density>
286 + <temp uom="degC">15</temp>
287 + <pres uom="atm">1</pres>
288 + </densityValue>
289 + <density uom="kg/m3">334.31</density>
290 + <densityFlowRate uom="Mg/a">290.09</densityFlowRate>
291 + <densityStd uom="kg/m3">412.8</densityStd>
292 + <concentration uom="ppm">53.22</concentration>
293 + <molecularWeight>50.39</molecularWeight>
294 + <weightPercent uom="%">12.68</weightPercent>
295 + <molePercent uom="%">97.96</molePercent>
296 + <moleAmt uom="kmol">68.2</moleAmt>
297 + <sg uom="Euc">18.88</sg>
298 + <hcDewpoint uom="K">339.08</hcDewpoint>
299 + <waterDewpoint uom="K">722.12</waterDewpoint>
300 + <wobbeIndex uom="J/m3">108.08</wobbeIndex>
301 + <grossCalorificValueStd uom="J/m3">230.02</grossCalorificValueStd>
302 + <rvpStabilizedCrude uom="Pa">322.68</rvpStabilizedCrude>
303 + <bswStabilizedCrude uom="Euc">84.89</bswStabilizedCrude>
304 + <densityStabilizedCrude uom="kg/m3">124.95</densityStabilizedCrude>
305 + </period>
306 +
307 + </product>
308 + </flow>
309 + </facility>
310 + </object>
311 +</objects>
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