CN205664361U - Coal slurry, coal slime and dry gas multi -fuel fired boiler - Google Patents

Coal slurry, coal slime and dry gas multi -fuel fired boiler Download PDF

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Publication number
CN205664361U
CN205664361U CN201620541793.2U CN201620541793U CN205664361U CN 205664361 U CN205664361 U CN 205664361U CN 201620541793 U CN201620541793 U CN 201620541793U CN 205664361 U CN205664361 U CN 205664361U
Authority
CN
China
Prior art keywords
coal
slurry
furnace
dry gas
coal slime
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
CN201620541793.2U
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Chinese (zh)
Inventor
董志刚
王连民
郑爱侠
邹玉进
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.)
Shandong Huayuan Boiler Co Ltd
Original Assignee
Shandong Huayuan Boiler Co Ltd
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 Shandong Huayuan Boiler Co Ltd filed Critical Shandong Huayuan Boiler Co Ltd
Priority to CN201620541793.2U priority Critical patent/CN205664361U/en
Application granted granted Critical
Publication of CN205664361U publication Critical patent/CN205664361U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model discloses a coal slurry, coal slime and dry gas multi -fuel fired boiler, it belongs to the boiler and pressure vessel makes the field. It mainly includes the furnace who is supported by the steelframe, is equipped with the main part above furnace is interior and receives hot side and separation feedback device, separation feedback device to include separator and feedback passageway, is equipped with the bed material below furnace is interior, is equipped with futilely gas burner on the bed is expected, the separator passes through the dense region intercommunication of feedback passageway and furnace below, furnace is connected with the air preheater through the pipeline bottom, and furnace is connected with the air preheater through the economizer top, bed material bottom is equipped with air distribute device, be equipped with temperature sensor in the bed material, the last thick liquid rifle that is equipped with of furnace. The utility model discloses the operation is stable, and easy operation has realized the low -temperature combustion of three kinds of fuel, and is low to the requirement of coal slime and coal slurry quality, has improved combustion efficiency. The utility model discloses the multifuel combustion of mainly used coal slurry, coal slime and dry gas.

Description

Water-coal-slurry, coal slime and dry gas multi-fuel fired boiler
Technical field
This utility model belongs to boiler and pressure vessel and manufactures field, specifically, particularly relates to a kind of water-coal-slurry, coal slime And dry gas multi-fuel fired boiler.
Background technology
Water-coal-slurry is the novel coal derived fuel of one that country advocates energetically, for oil-burning gas-fired boiler, maximum Advantage is exactly that operating cost is cheap, combustion completion is stable;And coal slime is a kind of product in coal production process, according to producing The difference of journey, calorific value is different with water content height.If directly abandoned, not only pollute environment, especially a biggest energy wave Take;Dry gas is as the associated natural gas in oil field, and the content more than 95% of methane, calorific value is the highest.At present, also can not realize this three The product of class A fuel A multifuel combustion.
Summary of the invention
The purpose of this utility model is to overcome drawbacks described above, it is provided that a kind of water-coal-slurry, coal slime and dry gas multi-fuel fired boiler, its Stable, simple to operate, it is achieved that the low-temperature burning of three kinds of fuel, the requirement to coal slime and water-coal-slurry quality is low, improves Efficiency of combustion.
Described water-coal-slurry, coal slime and dry gas multi-fuel fired boiler, including the burner hearth supported by steelframe, is arranged over main in burner hearth Body heating surface and separation refluxing device, separate below in refluxing device includes separator and feeds back passage, burner hearth and be provided with bed, bed Material is provided with dry combustion gas device, and separator connects with the emulsion zone below burner hearth by feeding back passage;Burner hearth bottom passes through pipeline It is connected with air preheater, is connected with air preheater by economizer above burner hearth.
Further, it is provided with air-distribution device bottom described bed.
Further, it is provided with temperature sensor in described bed.
Further, described burner hearth is provided with slurry rifle.
Further, described burner hearth is provided with coal slime charge door.
Further, roof of the furnace is connected with drum by pipeline.
Compared with prior art, the beneficial effects of the utility model are:
1, this utility model high heating value dry gas is as fuel used during furnace lifting, additionally with addition of thermal source, and need not achieve The low-temperature burning of three kinds of fuel, solve that traditional suspension combustion brings is prone to coking, fluctuation of service, the asking of poor stability Topic, inhibits again generation and the discharge of thermal NO x simultaneously.
2, bed utilizes the media material that quartz sand is constituted with limestone, and auxiliary achieves water-coal-slurry in low-temperature burning technology And direct desulfurization during coal combustion, desulphurization system is simple, low cost;
3, achieving the water-coal-slurry after ignition and the circulating combustion of coal slime cluster of grains by feedback passage, it is right to reduce Coal slime and the requirement of water-coal-slurry quality, make slurrying cost reduce;Meanwhile, separation feedback mode is used to improve the utilization of limestone Rate, decreases the magnitude of recruitment of media material, improves efficiency of combustion.
4, this utility model is stable, simple to operate, and efficiency of combustion is high, and operation strategies is wide, and Load Regulation characteristic is good, Can stable operation in the range of the rated load of 70%~100%.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
In figure, 1, drum;2, main body heating surface;3, separator;4, floater;5, slurry rifle;6, dry combustion gas device;7, coal slime Charge door;8, emulsion zone, 9, bed;10, air-distribution device;11, temperature sensor;12, air preheater;13, economizer;14, platform; 15, passage is fed back.
Detailed description of the invention
The utility model is described in further detail below in conjunction with the accompanying drawings:
Embodiment one: as it is shown in figure 1, water-coal-slurry, coal slime and dry gas multi-fuel fired boiler, including the burner hearth supported by steelframe, stove Thorax is provided with platform 14, and roof of the furnace is connected with drum 1 by pipeline, is arranged over main body heating surface 2 and separates back in burner hearth Defeated device, separates lower section in refluxing device includes separator 3 and feeds back passage 15, burner hearth and is provided with bed 9, and bed 9 is provided with dry Air burner 6, is provided with temperature sensor 11 in bed 9, be provided with air-distribution device 10 bottom bed 9, and separator 3 is by feeding back passage 15 connect with the emulsion zone 8 below burner hearth;Burner hearth bottom is connected with air preheater 12 by pipeline, by economizer 13 above burner hearth It is connected with air preheater 12.
Embodiment two: described burner hearth is provided with slurry rifle 5, and other is identical with embodiment one.
Embodiment three: described burner hearth is provided with coal slime charge door 7, other is identical with embodiment two.
This utility model in use, first by putting into quartz sand and limestone in the bed 9 of lower furnace portion, is opened afterwards Dry combustion gas device 6 heats bed 9 so that it is temperature rises to about 600 DEG C, opens the slurry rifle 5 of water-coal-slurry immediately, by drop-wise water coal Slurry puts in red-hot bed 9, and its temperature is risen to about 750~850 DEG C.Then, coal is put into by coal slime charge door 7 Mud, makes this three class A fuel As co-fire, and utilizes temperature sensor 11 to control the inlet amount of water-coal-slurry and coal slime, thus control bed The bed temperature of material 9, last temperature-control range is about 850~950 DEG C.Water-coal-slurry and coal slime are rapid under the heating of red-hot bed 9 Separate out moisture, immediately Volatile ignition, make the graininess water-coal-slurry under fluidized state and coal slime group further Disintegrate as fine grained, and taken out of emulsion zone 8 by heat smoke and enter floater 4 and burn away.The media material taken out of by heat smoke Bigger water-coal-slurry and coal slime cluster of grains are separated by separator 3, catch by separating refluxing device, by separator 3 bottom The passage 15 that feeds back arranged returns the emulsion zone 8 of lower furnace portion, had both decreased the loss of media material, and had achieved again cluster of grains Material circulating combustion, thus obtain high efficiency of combustion, the high-temperature flue gas that burning produces by with drum 1, economizer 13 and sky Discharge after the heat exchange of pre-device 12.
Additionally, the low-temperature burning process of about 850~950 DEG C, efficiently control the formation of thermal NO x, and due to Media material is made up of quartz sand and limestone, and limestone is at high temperature calcined generation CaO, CaO and SO2Reaction generates further CaSO4, it is suppressed that SO2Discharge, and the running temperature of burner is the optimum operation temperature of CaO desulfurization, can effectively reduce SO2Discharge.

Claims (6)

1. water-coal-slurry, coal slime and a dry gas multi-fuel fired boiler, including the burner hearth supported by steelframe, it is characterised in that: in burner hearth Side is provided with main body heating surface (2) and separates refluxing device, separates refluxing device and includes separator (3) and feed back passage (15), stove In thorax, lower section is provided with bed (9), and bed (9) is provided with dry combustion gas device (6), and separator (3) is by feeding back passage (15) and stove Emulsion zone (8) connection below thorax;Burner hearth bottom is connected with air preheater (12) by pipeline, by economizer (13) above burner hearth It is connected with air preheater (12).
Water-coal-slurry the most according to claim 1, coal slime and dry gas multi-fuel fired boiler, it is characterised in that: described bed (9) bottom It is provided with air-distribution device (10).
Water-coal-slurry the most according to claim 2, coal slime and dry gas multi-fuel fired boiler, it is characterised in that: described bed sets in (9) There is temperature sensor (11).
Water-coal-slurry the most according to claim 3, coal slime and dry gas multi-fuel fired boiler, it is characterised in that: described burner hearth is provided with Slurry rifle (5).
Water-coal-slurry the most according to claim 4, coal slime and dry gas multi-fuel fired boiler, it is characterised in that: described burner hearth is provided with Coal slime charge door (7).
Water-coal-slurry the most according to any one of claim 1 to 5, coal slime and dry gas multi-fuel fired boiler, it is characterised in that: burner hearth Top is connected with drum (1) by pipeline.
CN201620541793.2U 2016-06-06 2016-06-06 Coal slurry, coal slime and dry gas multi -fuel fired boiler Expired - Fee Related CN205664361U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620541793.2U CN205664361U (en) 2016-06-06 2016-06-06 Coal slurry, coal slime and dry gas multi -fuel fired boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620541793.2U CN205664361U (en) 2016-06-06 2016-06-06 Coal slurry, coal slime and dry gas multi -fuel fired boiler

Publications (1)

Publication Number Publication Date
CN205664361U true CN205664361U (en) 2016-10-26

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620541793.2U Expired - Fee Related CN205664361U (en) 2016-06-06 2016-06-06 Coal slurry, coal slime and dry gas multi -fuel fired boiler

Country Status (1)

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CN (1) CN205664361U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109058978A (en) * 2018-09-29 2018-12-21 青岛特利尔环保股份有限公司 Double fuel boiler system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109058978A (en) * 2018-09-29 2018-12-21 青岛特利尔环保股份有限公司 Double fuel boiler system

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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: 20161026

Termination date: 20210606

CF01 Termination of patent right due to non-payment of annual fee