CN202139205U - Device for recycling light oil in crude-oil single well - Google Patents

Device for recycling light oil in crude-oil single well Download PDF

Info

Publication number
CN202139205U
CN202139205U CN201120191437U CN201120191437U CN202139205U CN 202139205 U CN202139205 U CN 202139205U CN 201120191437 U CN201120191437 U CN 201120191437U CN 201120191437 U CN201120191437 U CN 201120191437U CN 202139205 U CN202139205 U CN 202139205U
Authority
CN
China
Prior art keywords
oil
gas
heat exchanger
liquid
phase separator
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201120191437U
Other languages
Chinese (zh)
Inventor
石永军
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
China University of Petroleum East China
Original Assignee
China University of Petroleum East China
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by China University of Petroleum East China filed Critical China University of Petroleum East China
Priority to CN201120191437U priority Critical patent/CN202139205U/en
Application granted granted Critical
Publication of CN202139205U publication Critical patent/CN202139205U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Separation By Low-Temperature Treatments (AREA)

Abstract

The utility model relates to a device for recycling light oil in a crude-oil single well, which comprises a primary heat exchanger, a secondary heat exchanger, a refrigerating machine, a gas-liquid two-phase separator, a filter, a flow meter, a thermometer, a safety valve, a liquid level meter, an oil gas inlet pipe, an oil gas pipe, an oil gas blow-down pipe, a light oil outlet and a pollution discharge port. Secondary heat exchange is performed on blow-down oil gas through the primary heat exchanger and the secondary heat exchanger, the back of the filter is provided with the flow meter, the thermometer is arranged between the secondary heat exchanger and the gas-liquid two-phase separator, and refrigerating output of the refrigerating machine is controlled through a temperature signal and a flow signal. The device is used for recycling the blow-down oil gas in a crude oil tank of a remote crude oil production well, and has the advantages of being high in recovery rate, convenient to install and transport and high in automation degree.

Description

Crude oil individual well light oil recovery unit
Technical field
The utility model relates to a kind of crude oil individual well light oil recovery unit, belongs to Petro-Chemical Machinery, is a kind of device that from remote crude production oil well petroleum tank, reclaims lightweight oil.
Technical background
For remote crude production oil well, because there is not pipe network, the crude oil of producing all is to be stored in the multi-functional oil tank of individual well.Because in the crude oil multiple hydro carbons composition is arranged, and in crude production, often produce association lighter hydrocarbons gas, in addition, the multifunctional crude oil jar also will often heat, heating causes more lighter hydrocarbons gas to produce.In order to keep multi-functional tank pressure control within the specific limits, the frequent emptying of multifunctional crude oil storage tank often contains methane in dropping a hint; Lightweight oil; Components such as liquefied gas had both been polluted environment, had also been wasted the energy, and the light oil recovery unit to the crude production individual well is not arranged at present as yet.In order to improve production of hydrocarbons zone operating environment and save energy, the retrieving arrangement of lightweight oil improves associated gas comprehensive utilization ability in needing that exploitation is a kind of and dropping a hint to the individual well Multifunction tank.
The utility model content
The utility model technical problem to be solved provides a kind of crude oil individual well light oil recovery unit, and is low to solve remote crude production oil well organic efficiency, the problem that environmental pollution is serious.
The utility model solves the technical scheme that its technical problem adopted: crude oil individual well light oil recovery unit comprises strainer, under meter, first-class heat exchanger, secondary heat exchanger, SV, gas-liquid separator, liquidometer.Emptying oil gas from individual well multifunctional crude oil storage tank filters through strainer earlier, by under meter flow signal is passed to refrigerator, carries out precooling through first-class heat exchanger earlier, and then further cools off through secondary heat exchanger.Get into gas-liquid two-phase separator through the cooled gas of secondary heat exchanger, the gas temperature of secondary heat exchanger outlet is less than the condensing temperature under the normal pressure of lightweight oil, and behind the entering gas-liquid two-phase separator, lightweight oil is separated.Remain cooling gas in order to utilize in the gas-liquid two-phase separator behind the separation of lighter oil, residual gas gets into first-class heat exchanger and comes gas to carry out precooling to individual well multifunctional crude oil storage tank.Between secondary heat exchanger and gas-liquid two-phase separator, be provided with TM, through the refrigerating duty of temperature signal and flow signal control refrigeration system.
The beneficial effect of the utility model is to take the refrigerating duty intelligent control of secondary heat-exchanger rig and refrigeration system, good refrigeration effect, recovering of vaporized hydrocarbons rate height; Apparatus structure is simple, adopts whole skid, is convenient to install and transportation; The plant automation degree is high, and is safe and reliable.
Description of drawings
Accompanying drawing is a crude oil individual well light oil recovery unit structural representation;
1. individual well multifunctional crude oil storage tanks, 2. oil gas inlet tube, 3. strainer, 4. under meter among the figure; 5. oil gas pipe, 6. first-class heat exchanger, 7. secondary heat exchanger, 8. oil gas blow-down pipe; 9. refrigerator, 10. TM, 11. SV, 12. liquidometers; 13. the lightweight oil outlet, 14. blowdowns outlet, 15. gas-liquid two-phase separators.
Embodiment
Below in conjunction with accompanying drawing the utility model is further specified.Crude oil individual well light oil recovery unit is made up of first-class heat exchanger (6), secondary heat exchanger (7), refrigerator (9), gas-liquid two-phase separator (15), strainer (3), under meter (4), TM (10), SV (11), liquidometer (12), oil gas inlet tube (2), oil gas pipe (5), oil gas blow-down pipe (8), lightweight oil outlet (13), blowdown outlet (14) and gas-liquid two-phase separator (15), and is as shown in the figure.Emptying oil gas from individual well multifunctional crude oil storage tank (1) at first filters from oil gas inlet tube (2) entering strainer (3), and oil gas carries out precooling through first-class heat exchanger (6) earlier then, passes through further cooling of secondary heat exchanger (7) again.Get into gas-liquid two-phase separator (15) through the cooled gas of secondary heat exchanger (7); The gas temperature of secondary heat exchanger (7) outlet is less than the condensing temperature under the normal pressure of lightweight oil; After getting into gas-liquid two-phase separator (15); Lightweight oil is separated, and lightweight oil is outputed in the transport trolley by lightweight oil outlet (13) after reaching some amount, and the corresponding dirt that produces in the lightweight oil sepn process is discharged by blowdown outlet (14).Remain cooling gas in order to utilize in the gas-liquid two-phase separator (15) behind the separation of lighter oil, the residue cooling gas gets into first-class heat exchanger (6) and comes gas to carry out precooling to individual well multifunctional crude oil storage tank (1), is discharged by oil gas blow-down pipe (8) then.Gas-liquid two-phase separator (15) is provided with SV (11) and liquidometer (12), and SV (11) makes the interior pressure-controlling of gas-liquid two-phase separator (15) within the specific limits, the liquid level that liquidometer (12) is convenient to observe lightweight oil.Strainer (3) back is provided with under meter (4), between secondary heat exchanger (7) and gas-liquid two-phase separator (15), is provided with TM (10), through the refrigerating duty of temperature signal and flow signal control refrigerator (9).Under meter (4) is when needing repairing, and emptying oil gas can pass through oil gas pipe (5) and directly enter atmosphere.

Claims (3)

1. crude oil individual well light oil recovery unit; It is characterized in that it comprises first-class heat exchanger (6), secondary heat exchanger (7), refrigerator (9), gas-liquid two-phase separator (15), strainer (3), under meter (4), TM (10), SV (11), liquidometer (12), oil gas inlet tube (2), oil gas pipe (5), oil gas blow-down pipe (8), lightweight oil outlet (13), blowdown outlet (14) and gas-liquid two-phase separator (15); Emptying oil gas carries out the secondary heat exchange through first-class heat exchanger (6) and secondary heat exchanger (7); Strainer (3) back is provided with under meter (4); Between secondary heat exchanger (7) and gas-liquid two-phase separator (15), be provided with TM (10), through the refrigerating duty of temperature signal and flow signal control refrigerator (9).
2. crude oil individual well light oil recovery unit according to claim 1 is characterized in that remaining behind the separation of lighter oil in the gas-liquid two-phase separator (15) cooling gas entering first-class heat exchanger (6) and comes gas to carry out precooling to individual well multifunctional crude oil storage tank (1).
3. crude oil individual well light oil recovery unit according to claim 1 is characterized in that gas-liquid two-phase separator (15) is provided with SV (11) and liquidometer (12).
CN201120191437U 2011-05-26 2011-05-26 Device for recycling light oil in crude-oil single well Expired - Fee Related CN202139205U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201120191437U CN202139205U (en) 2011-05-26 2011-05-26 Device for recycling light oil in crude-oil single well

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201120191437U CN202139205U (en) 2011-05-26 2011-05-26 Device for recycling light oil in crude-oil single well

Publications (1)

Publication Number Publication Date
CN202139205U true CN202139205U (en) 2012-02-08

Family

ID=45550277

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201120191437U Expired - Fee Related CN202139205U (en) 2011-05-26 2011-05-26 Device for recycling light oil in crude-oil single well

Country Status (1)

Country Link
CN (1) CN202139205U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109847398A (en) * 2019-03-21 2019-06-07 成都华气厚普机电设备股份有限公司 A kind of liquid nitrogen spraying device for recovering oil and gas and method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109847398A (en) * 2019-03-21 2019-06-07 成都华气厚普机电设备股份有限公司 A kind of liquid nitrogen spraying device for recovering oil and gas and method
CN109847398B (en) * 2019-03-21 2023-08-29 厚普清洁能源(集团)股份有限公司 Liquid nitrogen spraying oil gas recovery device and method

Similar Documents

Publication Publication Date Title
CN101456556B (en) Carbon dioxide industrial-scale separation and purification system and method in mixture gas by hydrate method
CN201280427Y (en) Oil gas reclaiming apparatus
CN103160353B (en) Miniature skid-mounted natural gas recovery system
CN103539155B (en) Recovery ammonia in synthesis ammonia system waste gas is utilized to utilize the method for device
CN201104074Y (en) Skid mounted biogas purifying and liquefying device
CN207243827U (en) Below C8 alkane production condensation adsorption recovery apparatus
CN101703841B (en) Device for collecting and recovering oil gas by condensation and absorption
CN101586037A (en) Method for realizing selective reprocessing of catalytic cracking reprocessed oil slurry
CN103775029A (en) Waste heat recovery liquid nitrogen evaporating system
CN201260899Y (en) Oil vapour recovering equipment
CN107158878A (en) A kind of condensation method petroleum vapor recovery ice chest and its recovery method
CN202139205U (en) Device for recycling light oil in crude-oil single well
CN204717343U (en) A kind of refrigeration plant for reclaiming boil-off gas cold energy
CN203990235U (en) A kind of condensed oil-gas embrane method device for recovering oil and gas
CN209702668U (en) A kind of gas recovery system for oil
CN102039082B (en) Method and device for vaporizing hydrogen chloride in tail gas in polycrystalline silicon production
CN201330707Y (en) Refrigerator oil cooling system for screw compressor
CN206488547U (en) A kind of utilization LNG cold energy reclaims the VOCs gas devices of oil tank discharge
CN203216177U (en) Tube ice maker
CN103353207B (en) Device for purifying methane liquid from purified landfill gas
CN203048901U (en) Low-cost and low-energy natural gas recovering and processing device
CN206281263U (en) A kind of useless air-conditioning refrigerant reclaiming clean device
CN203612972U (en) Device for recycling ammonia from waste gas in ammonia synthetizing system
CN210030602U (en) Skid-mounted natural gas deoiling and dehydrating integrated device
CN110330018B (en) Device for preparing dry ice and separating ethylene by using LNG cold energy and working method

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20120208

Termination date: 20130526