SU526370A1 - Device for determining the intensity coefficient of isobaric condensation of natural and associated gases - Google Patents
Device for determining the intensity coefficient of isobaric condensation of natural and associated gasesInfo
- Publication number
- SU526370A1 SU526370A1 SU2083738A SU2083738A SU526370A1 SU 526370 A1 SU526370 A1 SU 526370A1 SU 2083738 A SU2083738 A SU 2083738A SU 2083738 A SU2083738 A SU 2083738A SU 526370 A1 SU526370 A1 SU 526370A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- separator
- natural
- determining
- associated gases
- heat exchanger
- Prior art date
Links
Landscapes
- Sampling And Sample Adjustment (AREA)
Description
проводов 7 и 8 соединен со входом сепаратора 9. На выходе сепаратора 9 установлен газовый счетчпк 10, соединенный с сепаратором трубопроводом И.wires 7 and 8 are connected to the inlet of the separator 9. At the outlet of the separator 9, a gas counter 10 is installed, connected to the separator by pipeline I.
В днищах сепараторов смонтированы вентили 12 и 13. Вихрева трубка 14 соединена с теплообменником 1 трубопроводом 15. Теплообменник 1 и сепараторы 5 и 9 покрыты теплоизол ционным материалом 16.Valves 12 and 13 are mounted in the bottoms of the separators. The vortex tube 14 is connected to the heat exchanger 1 by pipeline 15. The heat exchanger 1 and the separators 5 and 9 are covered with heat insulating material 16.
Устройство работает следующим образом.The device works as follows.
Исследуемый газ по трубопроводу подаетс в теплообменпик 1. Проход по змеевику 2, он охлаждаетс до температуры, при которой происходит конденсаци т желых углеводородов, двухфазный поток проходит по трубопроводу б и попадает в сепаратор 5, в котором отдел етс жидка фаза. Одновременно замер етс температура сепарации Ti. Из сепаратора 5 газова фаза по трубопроводу 7 поступает обратно в теплообменник, где дополнительпо охлаждаетс в змеевике 3. При этом вновь происходит конденсаци т желых углеводородов и образование двухфазного потока, который по трубопроводу 8 подаетс в сепаратор 9. В сепараторе 9 происходит отделение жидкой фазы с одновременным замером температуры сепарации Га- Из сепаратора 9 газова фаза по трубопроводу 11 поступает на газовый счетчик 10. Отсепарированна жидкость после окончани работы сливаетс через вентили 12 и 13, при этом замер етс объем жидкости в сепараторе 9. Охлаждение газа в теплообменнике производитс с помощью вихревой трубки , газ на которую подаетс по отдельному трубопроводу.The test gas through the pipeline is fed to the heat exchanger 1. The passage through the coil 2, it is cooled to a temperature at which condensation of heavy hydrocarbons occurs, the two-phase flow passes through the pipeline b and enters the separator 5, in which the liquid phase separates. At the same time, the separation temperature Ti is measured. From the separator 5, the gas phase passes through the pipeline 7 back to the heat exchanger, where it is additionally cooled in the coil 3. This again condenses the heavy hydrocarbons and forms a two-phase flow, which is fed through the pipeline 8 to the separator 9. In the separator 9 simultaneously measuring the separation temperature Ga. From the separator 9, the gas phase through the pipeline 11 enters the gas meter 10. After the work is separated, the separated liquid is discharged through valves 12 and 13, while measuring The volume of liquid in the separator 9. The gas is cooled in the heat exchanger using a vortex tube, the gas to which is fed through a separate pipeline.
Конструкци теплообменника позвол ет создать разность температур между сспаратора ми 5 и 9 в 20-30°С и поддерживать ее посто нной независимо от расхода газа через вихревую трубку.The design of the heat exchanger allows you to create a temperature difference between the separators 5 and 9 at 20-30 ° C and keep it constant regardless of the gas flow through the vortex tube.
Изменение коэффициента изобарическойChange in isobaric coefficient
конденсации производитс по формуле (1) сcondensation is made according to the formula (1) with
0 учетом того, что + Vl, 1/} -1/, ; Q, 0 considering the fact that + Vl, 1 /} -1 /,; Q,
Qi Q, Qi Q,
где VI -жидкость, собранна в сепараторе 5;where VI is the liquid collected in the separator 5;
У|-жидкость, собранна в сепараторе9; 5Q - объем газа, прошедщего оба сепаратора .V | -liquid collected in separator 9; 5Q is the volume of gas passing through both separators.
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU2083738A SU526370A1 (en) | 1974-12-10 | 1974-12-10 | Device for determining the intensity coefficient of isobaric condensation of natural and associated gases |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU2083738A SU526370A1 (en) | 1974-12-10 | 1974-12-10 | Device for determining the intensity coefficient of isobaric condensation of natural and associated gases |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| SU526370A1 true SU526370A1 (en) | 1976-08-30 |
Family
ID=20603405
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SU2083738A SU526370A1 (en) | 1974-12-10 | 1974-12-10 | Device for determining the intensity coefficient of isobaric condensation of natural and associated gases |
Country Status (1)
| Country | Link |
|---|---|
| SU (1) | SU526370A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2475294C2 (en) * | 2007-07-05 | 2013-02-20 | Шелл Интернэшнл Рисерч Маатсхаппий Б.В. | Method of removing drops of contaminant from gas flow and rinsing chute |
-
1974
- 1974-12-10 SU SU2083738A patent/SU526370A1/en active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2475294C2 (en) * | 2007-07-05 | 2013-02-20 | Шелл Интернэшнл Рисерч Маатсхаппий Б.В. | Method of removing drops of contaminant from gas flow and rinsing chute |
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