CN202328136U - Oil-field steam injection boiler taking pulverized coal as fuel - Google Patents
Oil-field steam injection boiler taking pulverized coal as fuel Download PDFInfo
- Publication number
- CN202328136U CN202328136U CN2011205013033U CN201120501303U CN202328136U CN 202328136 U CN202328136 U CN 202328136U CN 2011205013033 U CN2011205013033 U CN 2011205013033U CN 201120501303 U CN201120501303 U CN 201120501303U CN 202328136 U CN202328136 U CN 202328136U
- Authority
- CN
- China
- Prior art keywords
- communicated
- coal
- input port
- oil
- fuel
- 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
Landscapes
- Combustion Of Fluid Fuel (AREA)
Abstract
The utility model relates to an oil-field steam injection boiler, in particular to an oil-field steam injection boiler taking pulverized coal as fuel, and is used for solving the problems that the traditional fuel coal oil-field steam injection boiler has low efficiency and large discharge amount of atmospheric pollutants. The oil-field steam injection boiler taking the pulverized coal as the fuel comprises a pulverized coal combustion system, a boiler body and a smoke treatment device, wherein the pulverized coal combustion system comprises a middle pulverized coal bin, a pulverized coal feeding machine, a mixer, a pulverized coal combustor, a primary fan, a secondary fan and a petroleum liquid gas storage tank; the boiler body comprises a J-shaped hearth, a furnace top and a convection flue; and the smoke treatment device comprises a cloth-bag type dust remover, a draught fan, a desulfurizer and a chimney. According to the oil-field steam injection boiler taking the pulverized coal as the fuel, disclosed by the utility model, based on a brand new structure, clean combustion of coal is realized, saturated steam is produced under critical pressure, and the problems that the traditional fuel coal oil-field steam injection boiler has low efficiency and large discharge amount of atmospheric pollutants are solved; and the oil-field steam injection boiler taking the pulverized coal as the fuel, disclosed by the utility model, is suitable for a crude oil thermal recovery process of an oil field.
Description
Technical field
The utility model relates to uphole steam generator, specifically be a kind of be the uphole steam generator of fuel with the coal dust.
Background technology
Oil thermal recovery is exploited after being meant the underground sticky crude oil that is difficult to exploit being heated.In the oil thermal recovery process, be used for being called thermal recovery boiler, also be uphole steam generator to the steam generating equipment of oilbearing stratum injection Steam Heating crude oil.Uphole steam generator is a kind of high parameter low capacity direct-flow steam boiler, and its operating pressure is up to 18Mpa, but capacity is generally little.Early stage uphole steam generator fuel generally uses the petroleum by-product in oil, gas or oil field; Like waste oil waste gas etc.; Then along with oil price is constantly soaring, even the oil field also hopes to adopt cheap coal fuel to replace expensive fuel oil; To reduce the thickened oil recovery cost, so oil field gas injection boiler of fuel coal has just been arranged.Existing oil field gas injection boiler of fuel coal generally is to be the grate firing boiler (chain grate boiler) of fuel with the raw coal; Directly the shortcoming of burning raw coal mainly contains two: the one, and efficient is low, using energy source insufficient (It is generally accepted that the average operating efficiency of chain grate boiler has only about 65%); The 2nd, boiler Air Pollutant Emission amount is bigger, is unfavorable for environmental protection.Coal dust firing is one of high performance clean burning mode of the coal of generally acknowledging, and its efficiency of combustion can reach more than 95%~99% usually, is that other combustion system institute is unapproachable.Pulverized coal combustion is the combustion technology of a maturation originally; On large-sized station boiler, use quite general; And long-term history arranged; Just because the limitation of economic development and science and technology, receive cost height, uncontrollable atmosphere pollution initial ejection concentration and pollute the restriction of aspects such as the thing discharging is serious, make this clean burning technology on the low capacity boiler, not obtain good application for a long time.Also be rooted in the hearts of the people day by day along with energy-conserving and environment-protective become fundamental state policy, research and development and the application of this efficient energy-saving clean burning technology of coal dust firing on the low capacity boiler obtains paying attention in recent years.Uphole steam generator belongs to the special boiler of high parameter, low capacity, on uphole steam generator, uses pulverized coal combustion, can realize low energy consumption, low emission.Based on this, being necessary to invent a kind of is the uphole steam generator of fuel with the coal dust, to solve the existing problem that oil field gas injection boiler of fuel coal efficient is low and the Air Pollutant Emission amount is big.
Summary of the invention
The utility model is in order to solve the existing problem that oil field gas injection boiler of fuel coal efficient is low and the Air Pollutant Emission amount is big, and providing a kind of is the uphole steam generator of fuel with the coal dust.
The utility model is to adopt following technical scheme to realize: with the coal dust is the uphole steam generator of fuel, comprises pulverized coal combustion system, boiler body and fume treatment auxiliary; Powder storehouse, machine supplying powder, blender, coal burner, primary air fan, overfire air fan and petroleum oil liquid gas storage tank in the middle of said pulverized coal combustion system comprises; The delivery outlet in middle powder storehouse is communicated with the input port of machine supplying powder, and the delivery outlet of machine supplying powder is communicated with the input port of blender, and the delivery outlet of blender is communicated with the input port of coal burner, and the delivery outlet of petroleum oil liquid gas storage tank is communicated with the mouth of igniting of coal burner; Said boiler body comprises J-shaped burner hearth, furnace roof and convection pass; Coal burner is installed on the front wall of J-shaped burner hearth, and the delivery outlet of coal burner is communicated with the input port of J-shaped burner hearth; In the J-shaped burner hearth with in the furnace roof water-cooling wall is installed all; The J-shaped roof of the furnace is communicated with the convection pass top through furnace roof; High-temperature economizer, air preheater, low-level (stack-gas) economizer, exhaust opening are installed in the convection pass from top to bottom successively; First input port of air preheater is communicated with primary air fan, and first delivery outlet of air preheater is communicated with the input port of blender; Second input port of air preheater is communicated with overfire air fan, and second delivery outlet of air preheater is communicated with the input port of coal burner; The J-shaped burner hearth bottom is equipped with first ash bucket; The convection pass bottom is equipped with second ash bucket; Said fume treatment auxiliary comprises sack cleaner, air-introduced machine, devulcanizer and chimney; The input port of sack cleaner is communicated with exhaust opening, and the delivery outlet of sack cleaner is communicated with the input port of air-introduced machine, and the delivery outlet of air-introduced machine is communicated with the input port of devulcanizer, and the delivery outlet of devulcanizer is communicated with the input port of chimney.Said water-cooling wall is the structure that those skilled in the art realize easily, and multiple malformation can be arranged.
The concrete course of work is following: with the input port in powder storehouse in the middle of the coal dust input; Coal dust successively through middle powder storehouse, machine supplying powder gets into blender; Mix with wind primary air fan output, that also heat at this, and carried, be delivered to coal burner by a wind through air preheater.Simultaneously, the secondary wind by overfire air fan output, also process air preheater heating gets into coal burner.Oil liquefied gas input coal burner in the petroleum oil liquid gas storage tank is lighted a fire; Coal dust is lighted the back in J-shaped burner hearth internal combustion in coal burner; And with the water-cooling wall of J-shaped burner hearth and the high-temperature economizer in the convection pass, air preheater, low-level (stack-gas) economizer heat exchange, thereby produce steam.The lime-ash that coal dust firing produces reclaims through first ash bucket and second ash bucket.The flue gas that coal dust firing produces enters sack cleaner through exhaust opening; The flying dust (the coal powder boiler flying ash share accounts for more than 90% of lime-ash total amount) that in the flue gas 99% is above filters and collects; Flue gas after being purified is attracted by air-introduced machine and sends into the devulcanizer desulfurization, and the flue gas through pollutant removing, compliance with environmental protection requirements enters atmosphere through chimney at last.Based on said process; Compare with existing oil field gas injection boiler of fuel coal; The utility model is described to be that the uphole steam generator of fuel has been realized low energy consumption, low emission with the coal dust, has solved the problem that existing oil field gas injection boiler of fuel coal efficient is low and the Air Pollutant Emission amount is big thus.
The utility model is based on brand new; Realized the clean burning of coal; Under subcritical pressure boiler, produce saturated vapor, solved the problem that existing oil field gas injection boiler of fuel coal efficient is low and the Air Pollutant Emission amount is big, be applicable to crude oil thermal recovery technology process.
Description of drawings
Fig. 1 is the structural representation of the utility model.
Fig. 2 is the structural representation of the boiler body of the utility model.
Fig. 3 is the structural representation of the water-cooling wall of the utility model.
Among the figure: powder storehouse in the middle of the 1-, 2-machine supplying powder, 3-blender, 4-coal burner, 5-primary air fan, 6-overfire air fan; The 7-petroleum oil liquid gas storage tank, 8-J shape burner hearth, 9-furnace roof, 10-convection pass, 11-high-temperature economizer; The 12-air preheater, 13-low-level (stack-gas) economizer, 14-exhaust opening, 15-first ash bucket, 16-second ash bucket; The 17-sack cleaner, 18-air-introduced machine, 19-devulcanizer, 20-chimney, 21-monowall tube.
The specific embodiment
With the coal dust is the uphole steam generator of fuel, comprises pulverized coal combustion system, boiler body and fume treatment auxiliary;
Powder storehouse 1, machine supplying powder 2, blender 3, coal burner 4, primary air fan 5, overfire air fan 6 and petroleum oil liquid gas storage tank 7 in the middle of said pulverized coal combustion system comprises; The delivery outlet in middle powder storehouse 1 is communicated with the input port of machine supplying powder 2; The delivery outlet of machine supplying powder 2 is communicated with the input port of blender 3; The delivery outlet of blender 3 is communicated with the input port of coal burner 4, and the delivery outlet of petroleum oil liquid gas storage tank 7 is communicated with the mouth of igniting of coal burner 4.
Said boiler body comprises J-shaped burner hearth 8, furnace roof 9 and convection pass 10; Coal burner 4 is installed on the front wall of J-shaped burner hearth 8, and the delivery outlet of coal burner 4 is communicated with the input port of J-shaped burner hearth 8; In the J-shaped burner hearth 8 with in the furnace roof 9 water-cooling wall is installed all; J-shaped burner hearth 8 tops are communicated with convection pass 10 tops through furnace roof 9; High-temperature economizer 11, air preheater 12, low-level (stack-gas) economizer 13, exhaust opening 14 are installed in the convection pass 10 from top to bottom successively; First input port of air preheater 12 is communicated with primary air fan 5, and first delivery outlet of air preheater 12 is communicated with the input port of blender 3; Second input port of air preheater 12 is communicated with overfire air fan 6, and second delivery outlet of air preheater 12 is communicated with the input port of coal burner 4; J-shaped burner hearth 8 bottoms are equipped with first ash bucket 15; Convection pass 10 bottoms are equipped with second ash bucket 16.
Said fume treatment auxiliary comprises sack cleaner 17, air-introduced machine 18, devulcanizer 19 and chimney 20; The input port of sack cleaner 17 is communicated with exhaust opening 14, and the delivery outlet of sack cleaner 17 is communicated with the input port of air-introduced machine 18, and the delivery outlet of air-introduced machine 18 is communicated with the input port of devulcanizer 19, and the delivery outlet of devulcanizer 19 is communicated with the input port of chimney 20.
Said water-cooling wall is coiled to form by monowall tube 21.
Said coal burner 4 is the precombustion chamber coal burner.
During practical implementation, in conjunction with accurately supplying the powder technology (to comprise the accurate control of coal dust supply, the wind of different phase, the control of powder mixing ratio; Can realize automatic adjusting after demarcating in the debug phase), fast firing technique (comprise adopt three transfer wind eddy flow scalable heat accumulating type precombustion chamber coal burner, through the reasonable Arrangement gas burner position of igniting, rationally regulate once distinguished and admirable speed; Regulate the measures such as swirl strength of basic secondary wind, interior secondary wind, outer secondary wind; Guarantee that coal dust in time lights the fast and stable burning), the low nitrogen burning technology (through the classification air feed, is divided into rich fuel fire district and oxygen rich air combustion zone with coal dust firing; Realize the burning of coal dust low temperature; Reduce formation of nitrogen oxides), the utility model is described to be that the uphole steam generator of fuel can satisfy on the basis of the coal that adapts to broad with the coal dust, realizes quick non-oil ignition; Promptly open promptly and stop, realize the low temperature low nitrogen burning simultaneously as far as possible.Water-cooling wall adopts the direct current endless form, still can reliably working to satisfy under subcritical state that the carbonated drink density contrast reduces.J-shaped burner hearth form and size satisfy the requirement of the coal dust firing subcritical pressure boiler saturated vapor required with producing oil field gas injection simultaneously.
Claims (3)
1. one kind is the uphole steam generator of fuel with the coal dust, it is characterized in that: comprise pulverized coal combustion system, boiler body and fume treatment auxiliary;
Powder storehouse (1), machine supplying powder (2), blender (3), coal burner (4), primary air fan (5), overfire air fan (6) and petroleum oil liquid gas storage tank (7) in the middle of said pulverized coal combustion system comprises; The delivery outlet in middle powder storehouse (1) is communicated with the input port of machine supplying powder (2); The delivery outlet of machine supplying powder (2) is communicated with the input port of blender (3); The delivery outlet of blender (3) is communicated with the input port of coal burner (4), and the delivery outlet of petroleum oil liquid gas storage tank (7) is communicated with the mouth of igniting of coal burner (4);
Said boiler body comprises J-shaped burner hearth (8), furnace roof (9) and convection pass (10); Coal burner (4) is installed on the front wall of J-shaped burner hearth (8), and the delivery outlet of coal burner (4) is communicated with the input port of J-shaped burner hearth (8); In the J-shaped burner hearth (8) and in the furnace roof (9) water-cooling wall is installed all; J-shaped burner hearth (8) top is communicated with convection pass (10) top through furnace roof (9); High-temperature economizer (11), air preheater (12), low-level (stack-gas) economizer (13), exhaust opening (14) are installed in the convection pass (10) from top to bottom successively; First input port of air preheater (12) is communicated with primary air fan (5), and first delivery outlet of air preheater (12) is communicated with the input port of blender (3); Second input port of air preheater (12) is communicated with overfire air fan (6), and second delivery outlet of air preheater (12) is communicated with the input port of coal burner (4); J-shaped burner hearth (8) bottom is equipped with first ash bucket (15); Convection pass (10) bottom is equipped with second ash bucket (16);
Said fume treatment auxiliary comprises sack cleaner (17), air-introduced machine (18), devulcanizer (19) and chimney (20); The input port of sack cleaner (17) is communicated with exhaust opening (14); The delivery outlet of sack cleaner (17) is communicated with the input port of air-introduced machine (18); The delivery outlet of air-introduced machine (18) is communicated with the input port of devulcanizer (19), and the delivery outlet of devulcanizer (19) is communicated with the input port of chimney (20).
2. according to claim 1 is the uphole steam generator of fuel with the coal dust, it is characterized in that: said water-cooling wall is coiled to form by monowall tube (21).
3. according to claim 1 and 2 is the uphole steam generator of fuel with the coal dust, it is characterized in that: said coal burner (4) is the precombustion chamber coal burner.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011205013033U CN202328136U (en) | 2011-12-06 | 2011-12-06 | Oil-field steam injection boiler taking pulverized coal as fuel |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011205013033U CN202328136U (en) | 2011-12-06 | 2011-12-06 | Oil-field steam injection boiler taking pulverized coal as fuel |
Publications (1)
Publication Number | Publication Date |
---|---|
CN202328136U true CN202328136U (en) | 2012-07-11 |
Family
ID=46440117
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2011205013033U Expired - Fee Related CN202328136U (en) | 2011-12-06 | 2011-12-06 | Oil-field steam injection boiler taking pulverized coal as fuel |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN202328136U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102418916A (en) * | 2011-12-06 | 2012-04-18 | 山西蓝天环保设备有限公司 | Oil field gas injection boiler taking pulverized coal as fuel |
CN102767816A (en) * | 2012-07-16 | 2012-11-07 | 山东泓奥电力科技有限公司 | System for lowering exhaust gas temperature of boiler in external-internal combined mode |
-
2011
- 2011-12-06 CN CN2011205013033U patent/CN202328136U/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102418916A (en) * | 2011-12-06 | 2012-04-18 | 山西蓝天环保设备有限公司 | Oil field gas injection boiler taking pulverized coal as fuel |
CN102767816A (en) * | 2012-07-16 | 2012-11-07 | 山东泓奥电力科技有限公司 | System for lowering exhaust gas temperature of boiler in external-internal combined mode |
CN102767816B (en) * | 2012-07-16 | 2015-07-08 | 山东泓奥电力科技有限公司 | System for lowering exhaust gas temperature of boiler in external-internal combined mode |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN104266217B (en) | A kind of grate furnace multipath denitrating system and method for denitration thereof | |
CN203190418U (en) | Novel garbage pyrolysis incineration equipment | |
CN202884901U (en) | Boiler capable of realizing reignition of exhaust gas coal powder by using high-temperature flue gas and reducing NOx | |
CN202546811U (en) | Compound furnace arch and compound secondary air structure | |
CN104501177A (en) | Waste incinerating circulating fluidized bed boiler | |
CN102679390B (en) | Compound furnace arch and compound secondary air structure for cooperatively controlling generation of nitrogen oxide (NOX) | |
CN102418916A (en) | Oil field gas injection boiler taking pulverized coal as fuel | |
CN202328136U (en) | Oil-field steam injection boiler taking pulverized coal as fuel | |
CN102829474A (en) | Double-bed system for preventing heating surface of boiler from being contaminated | |
CN102829473A (en) | System for solving high-sodium coal combustion contamination through pyrolysis combustion double-bed | |
CN203731393U (en) | Pulverized coal boiler with burner at top | |
CN101413674A (en) | Oxygen-enriched air mixed blowing combustion adjuvant boiler energy-saving method and employed equipment thereof | |
CN103383143A (en) | Novel efficient air heater | |
CN102425775A (en) | U-shaped flame vertical pulverized coal combustion oil field gas injection boiler with overhead burner | |
CN100434795C (en) | Biomass combustion device with low NOx emission and combustion method thereof | |
CN201748644U (en) | Biomass organic heat carrier furnace | |
CN205279074U (en) | Low nitrogen powder combustor of slag -tap formula | |
CN201193817Y (en) | Vertical coal water slurry industry boiler | |
CN204756894U (en) | Lower feeding formula biomass fuel furnace | |
CN202328137U (en) | U-shaped flame vertical pulverized coal burning oil field gas injection boiler placed at top of burner | |
CN103388820A (en) | Clean pulverized coal combustion industrial boiler device | |
CN103292317A (en) | Small-and-medium-size industrial boiler capable of replacing coal powder and oil gas | |
CN203231537U (en) | Efficient oxygen-enriched combustion multi-component powder heat conduction oil boiler system | |
CN203231538U (en) | Efficient oxygen-enriched combustion multi-component powder fused salt boiler system | |
CN103225881B (en) | Efficient oxygen-enriched-combmultiple-unit-powderheat multiple-unit-powderheat heat transfer oil boiler system |
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: 20120711 Termination date: 20151206 |
|
EXPY | Termination of patent right or utility model |