CN206289222U - Fluidized gasification system separates dross coal and crushes recycling gasification installation - Google Patents

Fluidized gasification system separates dross coal and crushes recycling gasification installation Download PDF

Info

Publication number
CN206289222U
CN206289222U CN201621285518.5U CN201621285518U CN206289222U CN 206289222 U CN206289222 U CN 206289222U CN 201621285518 U CN201621285518 U CN 201621285518U CN 206289222 U CN206289222 U CN 206289222U
Authority
CN
China
Prior art keywords
gasification
coal
slag
pulverizer
slag coal
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
CN201621285518.5U
Other languages
Chinese (zh)
Inventor
张连华
马海军
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.)
JIANGSU HUAWEI MACHINERY MANUFACTURING Co Ltd
Original Assignee
JIANGSU HUAWEI MACHINERY MANUFACTURING 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 JIANGSU HUAWEI MACHINERY MANUFACTURING Co Ltd filed Critical JIANGSU HUAWEI MACHINERY MANUFACTURING Co Ltd
Priority to CN201621285518.5U priority Critical patent/CN206289222U/en
Application granted granted Critical
Publication of CN206289222U publication Critical patent/CN206289222U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Industrial Gases (AREA)

Abstract

流化床气化系统分离渣煤粉碎再循环气化装置包括:气化炉、旋风分离器、螺杆输送粉碎机。气化炉底部设有渣煤槽;螺杆输送粉碎机设置在渣煤槽下部,且其入口与气化炉底部的渣煤槽相通,出口并联在气化炉底部气化剂入口的通流管道上;旋风分离器的底部设有渣煤聚集斗,渣煤聚集斗与螺杆输送粉碎机的入口之间设有管道,旋风分离器底部的渣煤聚集斗与螺杆输送粉碎机的入口通过所述管道相连通。本实用新型将传统煤制气循环流化床气化系统中的旋风分离器分离下来的高温物料,不直接返回气化炉内进行气化再循环,而首先送入螺杆输送粉碎机内,对渣煤粉碎后再返回气化炉内进行气化,使粉碎后的渣煤更易于充分燃烧、更利于完全气化,从而实现提高煤气化率的目的。

The fluidized bed gasification system separates slag coal, pulverizes and recirculates the gasification device, including: gasifier, cyclone separator, and screw conveying pulverizer. There is a slag coal tank at the bottom of the gasifier; the screw conveyor pulverizer is set at the lower part of the slag coal tank, and its inlet is connected with the slag coal tank at the bottom of the gasifier, and its outlet is connected in parallel with the flow pipe of the gasification agent inlet at the bottom of the gasifier Above; the bottom of the cyclone separator is provided with a slag coal gathering hopper, and a pipeline is provided between the slag coal gathering hopper and the entrance of the screw conveying pulverizer, and the slag coal gathering bucket at the bottom of the cyclone separator and the entrance of the screw conveying pulverizer pass through the The pipes are connected. In the utility model, the high-temperature materials separated by the cyclone separator in the traditional coal gas circulating fluidized bed gasification system are not directly returned to the gasification furnace for gasification and recirculation, but are first sent into the screw conveying pulverizer, and the The slag coal is pulverized and then returned to the gasifier for gasification, which makes the pulverized slag coal easier to fully burn and more conducive to complete gasification, thereby achieving the purpose of increasing the coal gasification rate.

Description

流化床气化系统分离渣煤粉碎再循环气化装置Fluidized bed gasification system separation slag coal crushing recirculation gasification device

技术领域technical field

本实用新型涉及一种流化床气化系统中的渣煤再循环气化装置,尤其涉及一种对流化床气化系统中被旋风分离器分离下来的渣煤,进行粉碎再循环气化的装置,属于煤制气气化技术领域。The utility model relates to a slag coal recirculation gasification device in a fluidized bed gasification system, in particular to a slag coal separated by a cyclone separator in a fluidized bed gasification system for crushing and recirculating gasification The device belongs to the technical field of coal gasification.

背景技术Background technique

旋风分离器是煤制气循环流化床气化系统中的重要循环气化设备之一,它的作用是将气化炉气化后的高温煤气与颗粒的气固混合物进行气固分离,分离下来的高温物料直接再返回炉膛进行循环气化,循环物料中未反应的碳在气化炉炉膛中与气化剂进一步发生气化反应,以提高气化过程中碳的转化率。显然,旋风分离器分离的渣煤进行再循环气化,起到了提高煤气化率的作用,但在实际应用中,被旋风分离器分离下来的高温物料虽重返炉膛进一步气化,由于未燃尽的渣煤颗粒较大,却仍有一部分尚不能燃尽而不完全气化被排出而废弃。因此,传统煤制气流化床气化系统中的循环气化装置存在循环气化不完全,原煤热能利用率低,煤气化率不足的弊端。The cyclone separator is one of the important circulating gasification equipment in the coal-to-gas circulating fluidized bed gasification system. The high-temperature material that comes down is directly returned to the furnace for cyclic gasification, and the unreacted carbon in the circulating material further undergoes gasification reaction with the gasification agent in the hearth of the gasification furnace to increase the conversion rate of carbon during the gasification process. Obviously, the recycled gasification of the slag coal separated by the cyclone separator plays a role in increasing the gasification rate of coal. However, in practical applications, although the high-temperature material separated by the cyclone separator returns to the furnace for further gasification, due to the The exhausted slag coal particles are relatively large, but there is still a part of it that cannot be completely burned out and is not completely gasified to be discharged and discarded. Therefore, the circulation gasification device in the traditional coal-to-fluidized bed gasification system has the disadvantages of incomplete circulation gasification, low thermal energy utilization rate of raw coal, and insufficient coal gasification rate.

发明内容Contents of the invention

针对传统煤制气循环流化床气化系统中的循环气化装置存在的技术不足,本实用新型提供一种流化床气化系统分离渣煤粉碎再循环气化装置,实现提高煤气化率的目的。Aiming at the technical deficiencies of the circulating gasification device in the traditional coal-to-gas circulating fluidized bed gasification system, the utility model provides a fluidized bed gasification system separation slag coal crushing recycling gasification device to realize the improvement of coal gasification rate the goal of.

本实用新型的技术方案是:流化床气化系统分离渣煤粉碎再循环气化装置包含:气化炉、旋风分离器、螺杆输送粉碎机、插板阀、传感器和PLC可编程控制器,所述的气化炉底部设有渣煤槽;所述螺杆输送粉碎机设置在渣煤槽下部,螺杆输送粉碎机的入口与气化炉底部的渣煤槽相通,出口并联在气化炉底部气化剂入口的通流管道上;所述旋风分离器的底部设有渣煤聚集斗,其特征在于:The technical solution of the utility model is: the fluidized bed gasification system separates slag coal, pulverizes and recirculates the gasification device, which includes: a gasifier, a cyclone separator, a screw conveying pulverizer, a gate valve, a sensor and a PLC programmable controller, The bottom of the gasifier is provided with a slag coal tank; the screw conveying pulverizer is arranged at the lower part of the slag coal tank, the inlet of the screw conveying pulverizer communicates with the slag coal tank at the bottom of the gasifier, and the outlet is connected in parallel at the bottom of the gasifier On the flow pipe of the gasification agent inlet; the bottom of the cyclone separator is provided with a slag coal gathering bucket, which is characterized in that:

所述旋风分离器底部的渣煤聚集斗与螺杆输送粉碎机的入口之间设有管道,旋风分离器底部的渣煤聚集斗与螺杆输送粉碎机的入口通过所述管道相连通;A pipeline is arranged between the slag coal gathering bucket at the bottom of the cyclone separator and the entrance of the screw conveying pulverizer, and the slag coal gathering bucket at the bottom of the cyclone separator communicates with the entrance of the screw conveying pulverizer through the pipeline;

所述的渣煤聚集斗与螺杆输送粉碎机入口相连通的管道上依次设有传感器和插板阀;The pipeline connecting the slag coal gathering hopper and the inlet of the screw conveying pulverizer is provided with a sensor and a gate valve in sequence;

所述传感器将有无煤渣信号传输给PLC可编程控制器;所述PLC可编程控制器通过电信号指挥插板阀开闭。The sensor transmits the presence or absence of coal slag signal to the PLC programmable controller; the PLC programmable controller directs the gate valve to open and close through the electric signal.

本实用新型将传统煤制气循环流化床气化系统中的旋风分离器分离下来的高温物料,不直接返回气化炉内进行气化再循环,而首先送入螺杆输送粉碎机内,对渣煤粉碎后再返回气化炉内进行气化,使粉碎后的渣煤更易于充分燃烧、更利于完全气化,从而实现提高煤气化率的目的。In the utility model, the high-temperature materials separated by the cyclone separator in the traditional coal gas circulating fluidized bed gasification system are not directly returned to the gasification furnace for gasification and recirculation, but are first sent into the screw conveying pulverizer, and the The slag coal is pulverized and then returned to the gasifier for gasification, which makes the pulverized slag coal easier to fully burn and more conducive to complete gasification, thereby achieving the purpose of increasing the coal gasification rate.

本实用新型设计合理、结构简单,煤气化率高、节能效果好。The utility model has the advantages of reasonable design, simple structure, high coal gasification rate and good energy-saving effect.

附图说明Description of drawings

附图1为本实用新型的结构原理示意图。Accompanying drawing 1 is the structural principle schematic diagram of the utility model.

在附图1中:1为气化炉、101为渣煤槽、2为旋风分离器、201为渣煤集聚斗、3为螺杆输送粉碎机、4为气化剂入口的通流管道、5为插板阀、6为传感器、7为PLC可编程控制器。In accompanying drawing 1: 1 is a gasifier, 101 is a slag coal tank, 2 is a cyclone separator, 201 is a slag coal accumulation bucket, 3 is a screw conveyor pulverizer, 4 is a flow pipe for gasification agent inlet, 5 It is a gate valve, 6 is a sensor, and 7 is a PLC programmable controller.

具体实施方式detailed description

以下结合附图对本实用新型作进一步解释说明:Below in conjunction with accompanying drawing, the utility model is further explained:

如附图1所示,气化炉1底部设有渣煤槽101;螺杆输送粉碎机3设置在渣煤槽101下部,螺杆输送粉碎机3的入口与气化炉1底部的渣煤槽101相通,出口并联在气化炉1底部气化剂入口的通流管道4上;旋风分离器2的底部设有渣煤聚集斗201,渣煤聚集斗201与螺杆输送粉碎机3的入口之间设有管道,且渣煤聚集斗201与螺杆输送粉碎机3的入口通过管道相连通;渣煤聚集斗201与螺杆输送粉碎机3入口相连通的管道上依次设有传感器6和插板阀5;传感器6将有无煤渣信号传输给PLC可编程控制器7; PLC可编程控制器7通过电信号指挥插板阀5开闭。As shown in accompanying drawing 1, the bottom of gasifier 1 is provided with slag-coal tank 101; Connected, the outlet is connected in parallel on the flow pipe 4 of the gasification agent inlet at the bottom of the gasifier 1; the bottom of the cyclone separator 2 is provided with a slag coal gathering bucket 201, and the slag coal gathering bucket 201 and the inlet of the screw conveyor pulverizer 3 A pipeline is provided, and the slag coal gathering bucket 201 communicates with the entrance of the screw conveying pulverizer 3 through the pipeline; the pipeline connecting the slag coal gathering bucket 201 and the entrance of the screw conveying pulverizer 3 is provided with a sensor 6 and a slide valve 5 in sequence ; The sensor 6 transmits the cinder-free signal to the PLC programmable controller 7; the PLC programmable controller 7 directs the gate valve 5 to open and close through the electrical signal.

本实用新型将传统煤制气循环流化床气化系统中的旋风分离器2分离下来的高温物料,不直接返回气化炉1内进行气化再循环,而首先送入螺杆输送粉碎机3内,对渣煤粉碎后再返回气化炉1内进行气化,使粉碎后的渣煤更易于充分燃烧、更利于完全气化,从而实现提高煤气化率的目的。In the utility model, the high-temperature materials separated by the cyclone separator 2 in the traditional coal gas circulating fluidized bed gasification system are not directly returned to the gasification furnace 1 for gasification and recycling, but are first sent to the screw conveying pulverizer 3 Inside, the slag coal is pulverized and then returned to the gasifier 1 for gasification, so that the pulverized slag coal is easier to fully burn and more conducive to complete gasification, thereby achieving the purpose of increasing the coal gasification rate.

本实用新型还在渣煤聚集斗201与螺杆输送粉碎机3入口相连通的管道上依次设置传感器6和插板阀5。即:传感器6将触点处有煤渣堆积的电信号传送到给PLC可编程控制器7指令插板阀5打开;将触点处无煤渣堆积的电信号传送到给PLC可编程控制器7指令插板阀5关闭,从而使旋风分离器2的底部始终处于两种密封状态,一为无煤渣堆积时插板阀5的关闭密封状态;二为有煤渣堆积时的自密封状态,从而使旋风分离器2内的高温煤气不可从底部外泄。The utility model also arranges the sensor 6 and the plug valve 5 sequentially on the pipeline where the slag coal gathering bucket 201 communicates with the entrance of the screw conveyor pulverizer 3 . That is: the sensor 6 transmits the electrical signal that there is cinder accumulation at the contact point to the PLC programmable controller 7 to instruct the flapper valve 5 to open; the sensor 6 transmits the electrical signal that there is no cinder accumulation at the contact point to the PLC programmable controller 7 to instruct The flapper valve 5 is closed, so that the bottom of the cyclone separator 2 is always in two sealing states, one is the closed sealing state of the flapper valve 5 when there is no cinder accumulation; the other is the self-sealing state when there is cinder accumulation, so that the cyclone The high-temperature gas in the separator 2 cannot leak from the bottom.

Claims (3)

1.流化床气化系统分离渣煤粉碎再循环气化装置,包含:气化炉、旋风分离器、螺杆输送粉碎机、插板阀、传感器和PLC可编程控制器,所述的气化炉底部设有渣煤槽;所述螺杆输送粉碎机设置在渣煤槽下部,螺杆输送粉碎机的入口与气化炉底部的渣煤槽相通,出口并联在气化炉底部气化剂入口的通流管道上;所述旋风分离器的底部设有渣煤聚集斗,其特征在于:1. The fluidized bed gasification system separates slag coal crushing and recycling gasification device, including: gasifier, cyclone separator, screw conveying pulverizer, flapper valve, sensor and PLC programmable controller, the gasification A slag coal tank is provided at the bottom of the furnace; the screw conveying pulverizer is arranged at the lower part of the slag coal tank, the inlet of the screw conveying pulverizer communicates with the slag coal tank at the bottom of the gasifier, and the outlet is connected in parallel with the inlet of the gasification agent at the bottom of the gasifier. On the flow pipe; the bottom of the cyclone separator is provided with a slag coal gathering bucket, which is characterized in that: 所述旋风分离器底部的渣煤聚集斗与螺杆输送粉碎机的入口之间设有管道,旋风分离器底部的渣煤聚集斗与螺杆输送粉碎机的入口通过所述管道相连通。A pipeline is provided between the slag coal gathering hopper at the bottom of the cyclone separator and the inlet of the screw conveying pulverizer, and the slag coal gathering bucket at the bottom of the cyclone separator communicates with the entrance of the screw conveying pulverizer through the pipeline. 2.根据权利要求1所述的流化床气化系统分离渣煤粉碎再循环气化装置,其特征在于:所述的渣煤聚集斗与螺杆输送粉碎机入口相连通的管道上依次设有传感器和插板阀。2. The fluidized bed gasification system separation slag coal pulverization recirculation gasification device according to claim 1, characterized in that: the pipeline connecting the slag coal gathering hopper and the inlet of the screw conveying pulverizer is successively provided with Sensors and flapper valves. 3.根据权利要求1或2所述的流化床气化系统分离渣煤粉碎再循环气化装置,其特征在于:所述传感器将有无煤渣信号传输给PLC可编程控制器,所述PLC可编程控制器通过电信号指挥插板阀开闭。3. The fluidized bed gasification system separation slag coal pulverization recirculation gasification device according to claim 1 or 2, characterized in that: the sensor transmits the presence or absence of coal slag signal to the PLC programmable controller, and the PLC The programmable controller directs the gate valve to open and close through the electric signal.
CN201621285518.5U 2016-11-28 2016-11-28 Fluidized gasification system separates dross coal and crushes recycling gasification installation Expired - Fee Related CN206289222U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201621285518.5U CN206289222U (en) 2016-11-28 2016-11-28 Fluidized gasification system separates dross coal and crushes recycling gasification installation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201621285518.5U CN206289222U (en) 2016-11-28 2016-11-28 Fluidized gasification system separates dross coal and crushes recycling gasification installation

Publications (1)

Publication Number Publication Date
CN206289222U true CN206289222U (en) 2017-06-30

Family

ID=59100552

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201621285518.5U Expired - Fee Related CN206289222U (en) 2016-11-28 2016-11-28 Fluidized gasification system separates dross coal and crushes recycling gasification installation

Country Status (1)

Country Link
CN (1) CN206289222U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2019184097A1 (en) * 2018-03-30 2019-10-03 中科聚信洁能热锻装备研发股份有限公司 Novel circulating fluidized bed gasifier having electric heating-assisted temperature adjustment function, and control method therefor
CN114133943A (en) * 2021-11-30 2022-03-04 洛阳瑞华新能源技术发展有限公司 Low-rank coal gas-making combined process

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2019184097A1 (en) * 2018-03-30 2019-10-03 中科聚信洁能热锻装备研发股份有限公司 Novel circulating fluidized bed gasifier having electric heating-assisted temperature adjustment function, and control method therefor
CN114133943A (en) * 2021-11-30 2022-03-04 洛阳瑞华新能源技术发展有限公司 Low-rank coal gas-making combined process

Similar Documents

Publication Publication Date Title
CN105112577B (en) Dry granulating blast furnace slag waste heat recovery device and blast furnace slag waste heat recovery method
CN106675658B (en) A high-flux circulating fluidized bed low-order coal gasification device and method
WO2016145924A1 (en) Pyrolysis and gasification combined device of circulating fluidized bed
CN103911179A (en) Coal gasification method and device
CN206289222U (en) Fluidized gasification system separates dross coal and crushes recycling gasification installation
CN104762095A (en) Full-cycle low-temperature carbonization device and technique for semi coke production
CN205556581U (en) Fine coal pressurization conveyor
CN207279612U (en) A kind of water-coal-slurry circulating fluidized bed boiler based on fluidised form reconstruct
CN205556579U (en) Device of production synthetic gas
CN104566431B (en) Low-temperature drying and coal conveying integrated equipment for raw coal
CN103771141B (en) A kind of dust exhaustor unloads the anti-cryogenic gas access to plant of ash
CN201033773Y (en) Oil shale microwave dry distillation and fluidized combustion integrated system
CN204079999U (en) A kind of novel blast-furnace Coalblowing system
CN213866088U (en) Gasifier fly ash recirculation system capable of recycling coal gas
CN201046951Y (en) Oil shale refining furnace dry method decoking apparatus
CN203212472U (en) Expanded and vitrified small ball production line with waste heat control device
CN205295375U (en) Can avoid blast furnace furnace roof voltage -sharing system air feed facility of equalizing valve badge stopper
CN105485706A (en) Boiler smoke cyclone separation recycling device and smoke recycling method thereof
CN103727528B (en) Coal gasification and combustion fluid bed-the coal-powder boiler of series connection compound
CN104498068B (en) The carbonization furnace of a kind of band air seal set does coke discharging method
CN104593086B (en) It is a kind of to carry the powder coal gasification furnace that nitrogen, vapor, synthesis gas drive material return mechanism
CN1986733A (en) Dry decoking process for shale oil extracting furnace
CN101240176A (en) Recovery and Utilization of Remaining Energy of Coke Oven Flue Gas
CN207672003U (en) A kind of fluidized-bed gasification furnace goes into operation heating and ash discharge integrated apparatus
CN110746994A (en) Coupling system and process for coal-charging smoke treatment and coke oven flue gas purification of top-loading coke oven

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
EE01 Entry into force of recordation of patent licensing contract

Assignee: ZHONGKEJUXIN CLEAN ENERGY & HOT FORGING EQUIPMENT RESEARCH AND DEVELOPMENT Co.,Ltd.

Assignor: JIANGSU HUAWEI MACHINERY MANUFACTURING Co.,Ltd.

Contract record no.: X2023980045715

Denomination of utility model: Fluidized bed gasification system separation slag coal crushing and recycling gasification device

Granted publication date: 20170630

License type: Common License

Record date: 20231107

EE01 Entry into force of recordation of patent licensing contract
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20170630

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