CN202177090U - Condensation type steam filling boiler of gas oil field - Google Patents
Condensation type steam filling boiler of gas oil field Download PDFInfo
- Publication number
- CN202177090U CN202177090U CN2011202401944U CN201120240194U CN202177090U CN 202177090 U CN202177090 U CN 202177090U CN 2011202401944 U CN2011202401944 U CN 2011202401944U CN 201120240194 U CN201120240194 U CN 201120240194U CN 202177090 U CN202177090 U CN 202177090U
- Authority
- CN
- China
- Prior art keywords
- condenser
- convection section
- steam generator
- radiant section
- section
- 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
Links
Images
Abstract
The utility model relates to a condensation type steam filling boiler of a gas oil field. The condensation type steam filling boiler reasonably recovers sensible heat and latent heat in smoke by reducing smoke exhaust temperature so as to reduce smoke exhaust heat loss and improve heat efficiency.
Description
Technical field
The utility model relates to boiler, further is meant the condensed type combustion gas uphole steam generator.
Background technology
Along with the continuous expansion of thickened oil recovery scale in the world wide, the exploitation via steam injection viscous crude more and more causes people's attention as a kind of maturation process, and along with the rise of energy prices, the power-saving technology of uphole steam generator is upgraded becomes trend of the times.Uphole steam generator commonly used now all adopts the direct current cooker form, mainly comprises combustion system, radiant section, changeover portion, convection section, water-water heat exchanger and chimney.Because uphole steam generator fuel mainly is residual oil, crude oil and natural gas, injection boiler all is designed to oil-gas two-way, for reducing the cold end corrosion of flue gas to pipe; The water that gets into convection section all is heated to more than 100 ℃ through water-water heat exchanger earlier, adds when burning residual oil, crude oil the seriously polluted and easy-clear not of heating surface pipe, causes exhaust gas temperature high (generally more than 200 ℃); When particularly being fuel with the natural gas again; Flue gas is when contaminated pipe conducts heat, and heat-transfer effect is poor, and the sensible heat of flue gas and latent heat are all wasted very serious; The injection boiler heat loss due to exhaust gas is big, and the thermal efficiency is low.
Summary of the invention
The technical problem that the utility model will solve is; Deficiency to prior art; Having proposed is the condensed type combustion gas uphole steam generator of fuel with the natural gas, through reducing the exhaust gas temperature of injection boiler, rationally reclaims sensible heat and latent heat in the flue gas; Reduce heat loss due to exhaust gas, improve the thermal efficiency of boiler.
The technical scheme that the utility model adopts does; A kind of condensed type combustion gas uphole steam generator; Comprise combustion system, be provided with the radiant section of exhaust gases passes, the convection section that is provided with exhaust gases passes, the flue gas condenser that is provided with exhaust gases passes and chimney; Radiant section one end links to each other with combustion system, it is characterized in that, said radiant section, convection section, flue gas condenser and chimney connect to form the exhaust gases passes of perforation successively; Be provided with the radiant section tube bank of ring-type in the said radiant section exhaust gases passes; Be provided with the convection section tube bank in the convection section exhaust gases passes; The condenser bundles of dress condensate liquid cooled flue gas in being provided with in the condenser exhaust gases passes; And in condenser, being provided with the condenser tank, circulation has water in said radiant section tube bank, convection section tube bank and the condenser tank, and condenser tank, convection section tube bank and radiant section tube bank series connection successively.
Below the utility model is further described.
Further, said radiant section is horizontal, and exhanst gas outlet and gas approach place radiant section main body right ends respectively.
Further, said convection section is horizontal, and exhanst gas outlet and gas approach place convection section main body right ends respectively.
Further, said radiant section tube bank is in series by light pipe.
Further, said light pipe diameter is 70mm-127mm.
Further, be provided with at least 5 row's convection section tube banks in the said convection section, and be in series for light pipe near 3 rows or 4 row's convection section tube banks of radiant section, all the other convection section tube banks are in series for finned tube.
Further, the diameter of said light pipe is 60mm-127mm.
Further, the diameter of said finned tube is 60mm-127mm.
The course of work and the principle of condensed type combustion gas uphole steam generator are; 20 ℃ of left and right sides low pressure demineralized waters get into the condenser water inlet pipe; The organ pipe bundle that is condensed is delivered to oxygen-eliminating device by the condenser outlet pipe after being heated to about 65 ℃; Deaerated water is added by plunger displacement pump and is pressed into water under high pressure and gets into the convection section water inlet pipe after the deoxygenation; By the water inlet pipe of convection section outlet pipe entering radiant section, exported by the radiant section steam (vapor) outlet through the qualified steam that the radiant section tube bank is heated under required pressure (high pressure, super-pressure or subcritical pressure boiler) and the mass dryness fraction by current after the convection section tube bank is heated to about 280 ℃ for current.High-temperature flue gas after natural gas burns through combustion system is mainly with the working medium heat exchange of radiation heat transfer mode in the radiant section tube bank; Flue gas is reduced to about 950 ℃ and is got into convection section; Flue gas is mainly with the working medium heat exchange in the convection section tube bank of heat convection mode; Flue gas is reduced to about 160 ℃ and is got into flue gas condenser, and flue gas is the heat convection working medium heat exchange in condenser bundles so that phase transformation to be arranged mainly, and flue-gas temperature is reduced to about 50 ℃ and to be got into chimney and enter atmosphere.
Known that by above the utility model is the condensed type combustion gas uphole steam generator, the beneficial effect that it is compared with prior art had is:
1, cancelled the changeover portion that traditional uphole steam generator is not arranged heating surface, radiation loss is reduced, improved the injection boiler thermal efficiency and reduced the manufactured materials consumption;
2, cancelled the water-water heat exchanger of traditional uphole steam generator, water resistance is reduced, the plunger displacement pump power consumption is reduced;
3, flue gas condenser rationally reclaims sensible heat and the latent heat in the flue gas, reduces heat loss due to exhaust gas, improves the thermal efficiency of boiler, and the injection boiler thermal efficiency is reached more than 100%, and energy-saving effect is remarkable, and has reduced the pollution to environment;
4, radiant section and convection section are the high pressure boiler circuit, and flue gas condenser is a low pressure water system, and the manufacturing cost of flue gas condenser is reduced.
Description of drawings
Fig. 1 is a kind of embodiment overall structure of the utility model sketch map;
Fig. 2 is a flue gas condenser structural representation (arrow is represented flue gas flow direction) among Fig. 1;
Fig. 3 is a convection section structural representation (arrow is represented flue gas flow direction) among Fig. 1;
Fig. 4 is a radiation segment structure sketch map among Fig. 1;
In the drawings:
1-combustion system, 2-radiant section, 3-convection section,
4-flue gas condenser, 5-chimney, 6-condenser water inlet pipe,
7-condenser bundles, 8-condenser outlet pipe, 9-convection section water inlet pipe,
The tube bank of 10-convection section, 11-convection section outlet pipe, the tube bank of 12-radiant section,
13-radiant section water inlet pipe, 14-radiant section steam (vapor) outlet.
The specific embodiment
Like Fig. 1-shown in Figure 4; A kind of condensed type combustion gas uphole steam generator; Comprise combustion system 1, be provided with the radiant section 2 of exhaust gases passes, the convection section 3 that is provided with exhaust gases passes, the flue gas condenser 4 that is provided with exhaust gases passes and chimney 5; Radiant section 2 one ends link to each other with combustion system 1, it is characterized in that, said radiant section 2, convection section 3, flue gas condenser 4 and chimney 5 connect to form the exhaust gases passes of perforation successively; Be provided with the radiant section tube bank 12 of ring-type in the said radiant section exhaust gases passes; Be provided with convection section tube bank 10 in the convection section exhaust gases passes; The condenser bundles 7 of dress condensate liquid cooled flue gas in being provided with in the condenser exhaust gases passes; And in condenser, being provided with condenser tank 15, circulation has water in said radiant section tube bank 12, convection section tube bank 10 and the condenser tank 15, and condenser tank 15, convection section tube bank 10 and radiant section tube bank 12 series connection successively.
Convection section is horizontal 3, and exhanst gas outlet and gas approach place convection section main body right ends respectively.
Radiant section tube bank 12 is in series by light pipe, and the light pipe diameter is 70mm-127mm.
Be provided with at least 5 row's convection section tube banks 10 in the convection section; And 3 rows or 4 row's convection section tube banks near radiant section are in series for light pipe; All the other convection section tube banks are in series for finned tube, and the diameter of light pipe is 60mm-127mm, and the diameter of finned tube is 60mm-127mm.
Claims (8)
1. condensed type combustion gas uphole steam generator; Comprise combustion system (1), be provided with the radiant section (2) of exhaust gases passes, the convection section (3) that is provided with exhaust gases passes, the flue gas condenser (4) that is provided with exhaust gases passes and chimney (5); Radiant section (2) one ends link to each other with combustion system (1); It is characterized in that said radiant section (2), convection section (3), flue gas condenser (4) and chimney (5) connect to form the exhaust gases passes of perforation successively; Be provided with the radiant section tube bank (12) of ring-type in the said radiant section exhaust gases passes; Be provided with convection section tube bank (10) in the convection section exhaust gases passes; The condenser bundles (7) of dress condensate liquid cooled flue gas in being provided with in the condenser exhaust gases passes; And in condenser, be provided with condenser tank (15); Circulation has water in said radiant section tube bank (12), convection section tube bank (10) and the condenser tank (15), and condenser tank (15), convection section tube bank (10) and radiant section tube bank (12) are connected successively.
2. according to the said condensed type combustion gas uphole steam generator of claim 1, it is characterized in that said radiant section (2) is horizontal, exhanst gas outlet and gas approach place radiant section main body right ends respectively.
3. according to the said condensed type combustion gas uphole steam generator of claim 1, it is characterized in that said convection section is horizontal (3), exhanst gas outlet and gas approach place convection section main body right ends respectively.
4. according to the said condensed type combustion gas uphole steam generator of claim 1, it is characterized in that said radiant section tube bank (12) is in series by light pipe.
5. according to the said condensed type combustion gas uphole steam generator of claim 4, it is characterized in that said light pipe diameter is 70mm-127mm.
6. according to the said condensed type combustion gas uphole steam generator of claim 1; It is characterized in that; Be provided with at least 5 row's convection section tube banks (10) in the said convection section, and be in series for light pipe near 3 rows or 4 row's convection section tube banks of radiant section, all the other convection section tube banks are in series for finned tube.
7. according to the said condensed type combustion gas uphole steam generator of claim 6, it is characterized in that the diameter of said light pipe is 60mm-127mm.
8. according to the said condensed type combustion gas uphole steam generator of claim 6, it is characterized in that the diameter of said finned tube is 60mm-127mm.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011202401944U CN202177090U (en) | 2011-07-08 | 2011-07-08 | Condensation type steam filling boiler of gas oil field |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011202401944U CN202177090U (en) | 2011-07-08 | 2011-07-08 | Condensation type steam filling boiler of gas oil field |
Publications (1)
Publication Number | Publication Date |
---|---|
CN202177090U true CN202177090U (en) | 2012-03-28 |
Family
ID=45866966
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2011202401944U Expired - Fee Related CN202177090U (en) | 2011-07-08 | 2011-07-08 | Condensation type steam filling boiler of gas oil field |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN202177090U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109654520A (en) * | 2018-12-27 | 2019-04-19 | 中国石油化工股份有限公司胜利油田分公司注汽技术服务中心 | A kind of novel injection boiler back-end ductwork system |
-
2011
- 2011-07-08 CN CN2011202401944U patent/CN202177090U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109654520A (en) * | 2018-12-27 | 2019-04-19 | 中国石油化工股份有限公司胜利油田分公司注汽技术服务中心 | A kind of novel injection boiler back-end ductwork system |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103244214A (en) | Smoke condensation heat recovery combined heat and power supply system based on organic Rankine cycle | |
CN102454980A (en) | Method for recycling flue gas waste heat of thermal power plant boiler | |
CN205717146U (en) | A kind of ultrahigh pressure coal gas boiler | |
CN206073441U (en) | Forced circulation fuel-firing gas-firing pipe hot water boiler | |
CN103471084B (en) | Low-pressure hot-water smoke cooling system and method for avoiding low-temperature corrosion of air pre-heater | |
CN202791972U (en) | Boiler tail flue gas waste heat utilization system | |
CN203771380U (en) | Condensation waste heat recovery steam boiler | |
CN210714643U (en) | Multi-energy complementary thickened oil exploitation energy-saving system | |
CN201779684U (en) | High-grade recycling system for exhaust heat of power station boiler | |
CN101929670A (en) | Oilfield steam injection boiler | |
CN201926121U (en) | Horizontal type condensing normal pressure hot water boiler | |
CN202177090U (en) | Condensation type steam filling boiler of gas oil field | |
CN204880066U (en) | Large -scale module high -efficient condensing gas steam boiler that gets ready | |
CN202791953U (en) | Water pipe type condensation superheating steam generator | |
CN103363663B (en) | Heavy die block assembling high-efficiency condensing type gas-fired water heating boiler | |
CN202158578U (en) | Composite water circulation heat exchanger with function of exchanging heat and heating air for three times | |
CN201844388U (en) | Flue-gas waste heat recovery device | |
CN104373310B (en) | Solar energy and fuel complementary power generation system | |
CN204534516U (en) | A kind of Novel supercritical carbon dioxide coal-burning boiler | |
CN107345656A (en) | A kind of steam raising plant using residual heat from boiler fume | |
CN211290559U (en) | Flue gas waste heat recovery device | |
CN209213910U (en) | A kind of light coal complementary system realizing solar energy cascade and utilizing | |
CN201028494Y (en) | Environment-friendly energy-saving boiler group | |
CN206755129U (en) | A kind of steam raising plant using residual heat from boiler fume | |
CN202792536U (en) | Water pipe type condensation hot water boiler |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120328 Termination date: 20190708 |
|
CF01 | Termination of patent right due to non-payment of annual fee |