Study on Homogeneous Reduction Technology in Gas Samples for Oil and Gas Loss
Abstract
:1. Introduction
2. Experimental Scheme and Design
2.1. Laboratory Equipment
2.2. Schematic Structure Design of Heating Box
2.3. Transfer Device Design
2.4. Constant-Temperature Gas Transmission Pipeline Design
3. Experimental Parameter Design
3.1. Heating Temperature of the Transmitter
3.2. Hot Air System Temperature
3.3. Heating Temperature of the Constant-Temperature Conveying Gas Pipe
3.4. The Experimental Scheme
3.5. Gas Chromatography–Mass Spectrometry Analysis Methods
3.6. Standard Gas Test Data Analysis
3.7. Field Gas Loss Measurement Data Analysis
4. Conclusions
Author Contributions
Funding
Data Availability Statement
Conflicts of Interest
Appendix A
References
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Serial Number | Component | Homogeneous Reduction Method | Direct Intake Method | ||
---|---|---|---|---|---|
Test results | Deviation | Test results | Deviation | ||
1 | N2 | 0.57258 | 6.95% | 0.59347 | 10.86% |
2 | CH4 | 0.19924 | 0.63% | 0.19819 | 0.10% |
3 | CH3CH3 | 0.05238 | −11.53% | 0.05103 | −13.79% |
4 | CH3CH2CH3 | 0.05265 | −11.06% | 0.05000 | −15.53% |
5 | CH3CHCH3 | 0.02742 | −7.35% | 0.02526 | −14.67% |
6 | CH3CH2CH2CH3 | 0.02943 | −0.92% | 0.02621 | −11.75% |
7 | CH3(CH2)2CH3 | 0.01420 | −6.55% | 0.01266 | −16.74% |
8 | CH3CH(CH3)CH2CH3 | 0.01516 | 3.11% | 0.01261 | −14.22% |
9 | CH3CH2CH2CH2CH3 | 0.01700 | −13.69% | 0.01377 | −30.13% |
10 | CH3C(CH3)2CH2CH3 | 0.00293 | −40.42% | 0.00247 | −49.78% |
11 | CH3CHCHCH3 | 0.00520 | 5.86% | 0.00440 | −10.33% |
12 | CH3CH2CH2CH(CH3)2 | - | - | - | - |
13 | CH3CH2CH(CH3)CH2CH3 | 0.00274 | −44.19% | 0.00235 | −52.12% |
14 | CH3CH2CH2CH2CH2CH3 | 0.00907 | −53.98% | 0.00757 | −61.55% |
Total | - | 1.0000 | 1.0000 | ||
Mean | - | −3.45% | −11.62% |
Serial Number | Component | Estuary District 4–2# | Yongyi Lian Primary Settling Tank | Yongyi Lian Secondary Settlement Tank | Yongyi Lian Export Tank | ||||||||
---|---|---|---|---|---|---|---|---|---|---|---|---|---|
Homogeneous Reduction Method | Direct Intake Method | Boost Performance | Homogeneous Reduction Method | Direct Intake Method | Boost Performance | Homogeneous Reduction Method | Direct Intake Method | Boost Performance | Homogeneous Reduction Method | Direct Intake Method | Boost Performance | ||
1 | N2 | 0.9473 | 0.9448 | 0.26% | 0.5487 | 0.7704 | −40.40% | 0.8449 | 0.9426 | −11.56% | 0.7836 | 0.9762 | −24.58% |
2 | CH4 | 0.0295 | 0.0317 | −7.46% | 0.2816 | 0.1669 | 40.73% | 0.0677 | 0.0140 | 79.32% | 0.1279 | 0.0015 | 98.83% |
3 | CO2 | 0.0009 | 0.0010 | −11.11% | 0.0027 | 0.0023 | 14.81% | 0.0016 | 0.0008 | 50.00% | 0.0021 | 0.0009 | 57.14% |
4 | CH3CH3 | 0.0105 | 0.0112 | −6.67% | 0.0181 | 0.0094 | 48.07% | 0.0070 | 0.0015 | 78.57% | 0.0084 | 0.0005 | 94.05% |
5 | CH3CH2CH3 | 0.0062 | 0.0065 | −4.84% | 0.0455 | 0.0177 | 61.10% | 0.0220 | 0.0069 | 68.64% | 0.0258 | 0.0025 | 90.31% |
6 | C(CH3)4 | 0.0013 | 0.0013 | 0.00% | 0.0137 | 0.0051 | 62.77% | 0.0070 | 0.0031 | 55.71% | 0.0083 | 0.0015 | 81.93% |
7 | CH3CH2CH2CH3 | 0.0020 | 0.0019 | 5.00% | 0.0363 | 0.0125 | 65.56% | 0.0195 | 0.0098 | 49.74% | 0.0196 | 0.0049 | 75.00% |
8 | CH3CH(CH3)CH2CH3 | 0.0008 | 0.0007 | 12.50% | 0.0195 | 0.0057 | 70.77% | 0.0106 | 0.0068 | 35.85% | 0.0101 | 0.0037 | 63.37% |
9 | CH3CH2CH2CH2CH3 | 0.0006 | 0.0005 | 16.67% | 0.0150 | 0.0044 | 70.67% | 0.0084 | 0.0057 | 32.14% | 0.0067 | 0.0031 | 53.73% |
10 | C5H10 | 0.0000 | 0.0000 | 0.0010 | 0.0003 | 70.00% | 0.0005 | 0.0004 | 20.00% | 0.0004 | 0.0002 | 50.00% | |
11 | C10H10 | 0.0000 | 0.0000 | 0.0000 | 0.0001 | 100.00% | 0.0000 | 0.0000 | - | 0.0000 | 0.0000 | - | |
12 | CH3CH(CH3)CH2CH3 | 0.0001 | 0.0001 | 0.00% | 0.0035 | 0.0009 | 74.29% | 0.0019 | 0.0016 | 15.79% | 0.0015 | 0.0008 | 46.67% |
13 | CH3CH2CH(CH3)CH3 | 0.0001 | 0.0000 | 100.00% | 0.0019 | 0.0005 | 73.68% | 0.0011 | 0.0009 | 18.18% | 0.0008 | 0.0005 | 37.50% |
14 | CH3CH2CH2CH2CH2CH3 | 0.0001 | 0.0001 | 0.00% | 0.0039 | 0.0012 | 69.23% | 0.0022 | 0.0020 | 9.09% | 0.0015 | 0.0010 | 33.33% |
15 | C5H9CH3 | 0.0001 | 0.0000 | 100.00% | 0.0020 | 0.0006 | 70.00% | 0.0011 | 0.0010 | 9.09% | 0.0007 | 0.0006 | 14.29% |
16 | C6H6 | 0.0000 | 0.0000 | - | 0.0002 | 0.0001 | 50.00% | 0.0001 | 0.0001 | 0.00% | 0.0001 | 0.0000 | 100.00% |
17 | C6H12 | 0.0000 | 0.0000 | - | 0.0010 | 0.0003 | 70.00% | 0.0006 | 0.0006 | 0.00% | 0.0004 | 0.0003 | 25.00% |
18 | CH3CH2CH2CH(CH3)CH2CH3 | 0.0001 | 0.0000 | 100.00% | 0.0023 | 0.0006 | 73.91% | 0.0015 | 0.0011 | 26.67% | 0.0009 | 0.0007 | 22.22% |
19 | CH3CH2CH2CH2CH2CH2CH3 | 0.0001 | 0.0000 | 100.00% | 0.0011 | 0.0003 | 72.73% | 0.0007 | 0.0004 | 42.86% | 0.0004 | 0.0003 | 25.00% |
20 | C6H11CH3 | 0.0000 | 0.0000 | - | 0.0010 | 0.0003 | 70.00% | 0.0007 | 0.0004 | 42.86% | 0.0004 | 0.0003 | 25.00% |
21 | C7H8 | 0.0000 | 0.0000 | - | 0.0003 | 0.0001 | 66.67% | 0.0002 | 0.0001 | 50.00% | 0.0001 | 0.0000 | 100.00% |
22 | CH3CH(CH3)CH2CH2CH2CH3 | 0.0000 | 0.0000 | - | 0.0004 | 0.0001 | 75.00% | 0.0003 | 0.0001 | 66.67% | 0.0002 | 0.0001 | 50.00% |
23 | CH3CH2CH2CH2CH2CH2CH2CH3 | 0.0000 | 0.0000 | - | 0.0002 | 0.0000 | 100.00% | 0.0002 | 0.0000 | 100.00% | 0.0001 | 0.0000 | 100.00% |
Total | - | 0.9997 | 0.9998 | 620.08% | 1.0000 | 1.0000 | 1229% | 1.0000 | 1.0000 | 876.3% | 1.0000 | 1.0000 | 1274.2% |
Mean | - | - | 0.0435 | 26.96% | 0.0435 | 0.0435 | 53.46% | 0.0435 | 0.0435 | 38.16% | 0.0435 | 0.0435 | 55.40% |
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Fan, L.; Yue, Y.; Song, H.; Zhang, X.; Hu, X.; Dai, Y. Study on Homogeneous Reduction Technology in Gas Samples for Oil and Gas Loss. Separations 2023, 10, 294. https://doi.org/10.3390/separations10050294
Fan L, Yue Y, Song H, Zhang X, Hu X, Dai Y. Study on Homogeneous Reduction Technology in Gas Samples for Oil and Gas Loss. Separations. 2023; 10(5):294. https://doi.org/10.3390/separations10050294
Chicago/Turabian StyleFan, Lu, Yu Yue, Honglin Song, Xiaohan Zhang, Xinyun Hu, and Yongshou Dai. 2023. "Study on Homogeneous Reduction Technology in Gas Samples for Oil and Gas Loss" Separations 10, no. 5: 294. https://doi.org/10.3390/separations10050294