A kind of oilfield exploitation heat, electricity,CO 2, N 2The alliance manufacture methodTechnical 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.