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CN1451844A - Heat, electricity, CO2 and N2 united supply making method for oil field production - Google Patents

Heat, electricity, CO2 and N2 united supply making method for oil field production
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Publication number
CN1451844A
CN1451844ACN 03111639CN03111639ACN1451844ACN 1451844 ACN1451844 ACN 1451844ACN 03111639CN03111639CN 03111639CN 03111639 ACN03111639 ACN 03111639ACN 1451844 ACN1451844 ACN 1451844A
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CN
China
Prior art keywords
steam
hot water
feeding system
regulate
eliminator
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.)
Pending
Application number
CN 03111639
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Chinese (zh)
Inventor
张凤山
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.)
Liaohe Petroleum Exploration Bureau
Original Assignee
Liaohe Petroleum Exploration Bureau
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 Liaohe Petroleum Exploration BureaufiledCriticalLiaohe Petroleum Exploration Bureau
Priority to CN 03111639priorityCriticalpatent/CN1451844A/en
Publication of CN1451844ApublicationCriticalpatent/CN1451844A/en
Pendinglegal-statusCriticalCurrent

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Abstract

A system for providing heat, electric power, CO2 and N2 for oil field to recover petroleum is composed of separator, united supply system, enriching device, and regulation distiributor. The air separating technique is used to separate O2 and N2 from air. The critical or supercritical electric generator using the O2/CO2 and coal as fuel is used for providing electric energy, steam, hot water, CO2 and N2. It can increase the oil output and decrease cost.

Description

A kind of oilfield exploitation heat, electricity,CO 2, N 2The alliance manufacture method
Technical field:
The present invention relates to improve on a kind of field produces recovery ratio technology, particularly a kind of oilfield exploitation heat, electricity, CO2, N2The alliance manufacture method.
Technical background:
Thick oil steam drive, CO2Mixed phase drives, N2Non-phase-mixing driving is the effective ways of the raising recovery ratio of extensive use, and in order to increase substantially recovery ratio, the oil field needs a large amount of CO2, N2, steam and hot water, that use in the minority oil field at present is external import CO2And N2Car takes place, shipment or directly deliver to site operation, its cost is very high, has increased labour intensity, and the generation of steam (hot water) need be built a heat injection station specially, and contaminated environment has improved the oil extraction cost, and several gases can not be concentrated generation.
Technical scheme:
The object of the invention is to provide a kind of oilfield exploitation heat, electricity, CO2, N2The alliance manufacture method directly provides electricity, CO2, N2And steam (hot water), and pass through CO2, N2And fuel-economizing joint vapour, realization reduction cost of crude oil production are used in the optimum organization of steam (hot water).
The present invention seeks to realize like this, it by eliminator, co-feeding system, enricher, regulate and distribute device four parts and form, A, air is squeezed in the eliminator, utilize air separation technology with airborne O2And N2Separate the N that makes2Be transported to and regulate and distribute in the device; B, the O that makes2With portion C O2Flue gas is mixed in the co-feeding system, with critical or supercritical generating unit, takes O2/ CO2Produce the CO that the burning back produces with the fired coal combustion mode2Be transported to the enricher enrichment, simultaneously co-feeding system produce steam, hot water; CO in C, steam, hot water and the enricher that co-feeding system is produced2,,, the N that makes in the eliminator2Deliver to continually and regulate and distribute in the device; D, in regulating and distributing device, according to different reservoir development requirements, provide N2, CO2, N2+ CO2, N2+ steam (hot water), CO2+ steam (hot water), N2+ CO2+ steam (hot water), 7 kinds of different handling up or displacement mode of steam.
The present invention has been owing to adopted eliminator one end and co-feeding system, enricher, regulate and distribute device and be linked in sequence, eliminator, the co-feeding system other end respectively with regulate and distribute device and directly be connected, with critical or supercritical generating unit, take O2/ CO2Combustion system is produced, thereby provides institute's electricity consumption, steam, hot water, CO for oil field development2, N2And according to handling up or the difference of displacement mode, different mixed proportions is provided, replaces fuel oil and natural gas with fire coal, fuel-economizing and gas-economizing increases production again, improve the oil field ultimate recovery greatly, reduced the oil extraction cost, alleviated labour intensity, technical flow design is reasonable, simple to operate, be well suited for field popularization application.
Accompanying drawing is a process flow diagram of the present invention.
The present invention is further described below in conjunction with accompanying drawing.
As shown in the figure, the present invention by eliminator, co-feeding system, enricher, regulate and distribute device four parts and form, eliminator one end by transfer tube with co-feeding system, regulate and distribute device and be connected respectively, co-feeding system by transfer tube respectively with enricher, regulate and distribute device and be connected, enricher with regulate and distribute device and be connected, co-feeding system is provided with an outer power supply port, regulates and distributes to be connected to 7 groups on the device and to supply mouth outward; A, at first air is squeezed in the eliminator, airborne O2And N2Separate the 92%N that makes2Be transported to and regulate and distribute in the device; The 90%O that B, eliminator make2Portion C O with burning back generation from co-feeding system2Flue gas is mixed in the co-feeding system, with critical or supercritical generating unit, takes O2/ CO2Produce the CO that the burning back produces with the fired coal combustion mode2Content is transported to the enricher enrichment more than 95%, produce steam, hot water and electricity at co-feeding system simultaneously, and electricity is by outer power supply port output; CO in C, steam, hot water and the enricher that co-feeding system is produced2,,, the N that makes in the eliminator2Deliver to continually and regulate and distribute in the device; D, in regulating and distributing device, according to different reservoir development requirements, provide N2, CO2, N2+ CO2, N2+ steam (hot water), CO2+ steam (hot water), N2+ CO2+ steam (hot water), 7 kinds of different handling up or displacement mode of steam.

Claims (2)

1, a kind of oilfield exploitation heat, electricity, CO2, N2The alliance manufacture method, it by eliminator, co-feeding system, enricher, regulate and distribute device four parts and form, it is characterized in that: A, air is squeezed in the eliminator, utilized air separation technology airborne O2And N2Separate the N that makes2Be transported to and regulate and distribute in the device; B, the O that makes2With portion C O2Flue gas is mixed in the co-feeding system, with critical or supercritical generating unit, takes O2/ CO2Produce the CO that the burning back produces with the fired coal combustion mode2Be transported to the enricher enrichment, simultaneously the steam that produces at co-feeding system, hot water; CO in C, steam, hot water and the enricher that co-feeding system is produced2,,, the N that makes in the eliminator2Deliver to continually and regulate and distribute in the device; D, in regulating and distributing device, according to different reservoir development requirements, provide N2, CO2, N2+ CO2, N2+ steam (hot water), CO2+ steam (hot water), N2+ CO2+ steam (hot water), 7 kinds of different handling up or displacement mode of steam.
CN 031116392003-05-092003-05-09Heat, electricity, CO2 and N2 united supply making method for oil field productionPendingCN1451844A (en)

Priority Applications (1)

Application NumberPriority DateFiling DateTitle
CN 03111639CN1451844A (en)2003-05-092003-05-09Heat, electricity, CO2 and N2 united supply making method for oil field production

Applications Claiming Priority (1)

Application NumberPriority DateFiling DateTitle
CN 03111639CN1451844A (en)2003-05-092003-05-09Heat, electricity, CO2 and N2 united supply making method for oil field production

Publications (1)

Publication NumberPublication Date
CN1451844Atrue CN1451844A (en)2003-10-29

Family

ID=29222749

Family Applications (1)

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CN 03111639PendingCN1451844A (en)2003-05-092003-05-09Heat, electricity, CO2 and N2 united supply making method for oil field production

Country Status (1)

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CN (1)CN1451844A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
CN101981272A (en)*2008-03-282011-02-23埃克森美孚上游研究公司Low emission power generation and hydrocarbon recovery systems and methods
CN1932237B (en)*2005-04-272012-10-24钻石Qc技术公司Method for exploiting heavy oil, gas or pitch
CN103775042A (en)*2013-06-182014-05-07中国石油天然气股份有限公司System and method for producing high-temperature high-pressure steam-flue gas based on oxygen-enriched boiler
CN106050205A (en)*2016-08-012016-10-26中嵘能源科技集团有限公司Gas power generation, tail gas steam and air combined supply joint oil production method and system
CN108343407A (en)*2018-02-092018-07-31邹积鹏Oil, the spontaneous carbon dioxide low temperature of well mix gas plugging releasing oil displacement technology
CN108397171A (en)*2018-02-022018-08-14中国石油大学(华东)A kind of nitrogen auxiliary carbon dioxide is handled up the method for the fine and close oil of exploitation
WO2018176691A1 (en)*2017-03-292018-10-04赫普热力发展有限公司Oil and gas field distributive multi-functional complementary energy resource micro-grid system
CN111577226A (en)*2020-06-052020-08-25中国石油天然气集团有限公司Production increasing method and special device for exploiting thick oil by gas-nitrogen mixed injection

Cited By (9)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
CN1932237B (en)*2005-04-272012-10-24钻石Qc技术公司Method for exploiting heavy oil, gas or pitch
CN101981272A (en)*2008-03-282011-02-23埃克森美孚上游研究公司Low emission power generation and hydrocarbon recovery systems and methods
CN101981272B (en)*2008-03-282014-06-11埃克森美孚上游研究公司Low emission power generation and hydrocarbon recovery systems and methods
CN103775042A (en)*2013-06-182014-05-07中国石油天然气股份有限公司System and method for producing high-temperature high-pressure steam-flue gas based on oxygen-enriched boiler
CN106050205A (en)*2016-08-012016-10-26中嵘能源科技集团有限公司Gas power generation, tail gas steam and air combined supply joint oil production method and system
WO2018176691A1 (en)*2017-03-292018-10-04赫普热力发展有限公司Oil and gas field distributive multi-functional complementary energy resource micro-grid system
CN108397171A (en)*2018-02-022018-08-14中国石油大学(华东)A kind of nitrogen auxiliary carbon dioxide is handled up the method for the fine and close oil of exploitation
CN108343407A (en)*2018-02-092018-07-31邹积鹏Oil, the spontaneous carbon dioxide low temperature of well mix gas plugging releasing oil displacement technology
CN111577226A (en)*2020-06-052020-08-25中国石油天然气集团有限公司Production increasing method and special device for exploiting thick oil by gas-nitrogen mixed injection

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