CN203404781U - Sludge carbonization material incineration device - Google Patents

Sludge carbonization material incineration device Download PDF

Info

Publication number
CN203404781U
CN203404781U CN201320384667.7U CN201320384667U CN203404781U CN 203404781 U CN203404781 U CN 203404781U CN 201320384667 U CN201320384667 U CN 201320384667U CN 203404781 U CN203404781 U CN 203404781U
Authority
CN
China
Prior art keywords
air
cyclone separator
smoke
main chamber
carbonized stock
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
CN201320384667.7U
Other languages
Chinese (zh)
Inventor
赵洪明
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 HONGLI PUMP ENERGY CO., LTD.
Original Assignee
SHANDONG HONGLI AIR-CONDITIONING EQUIPMENT 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 HONGLI AIR-CONDITIONING EQUIPMENT Co Ltd filed Critical SHANDONG HONGLI AIR-CONDITIONING EQUIPMENT Co Ltd
Priority to CN201320384667.7U priority Critical patent/CN203404781U/en
Application granted granted Critical
Publication of CN203404781U publication Critical patent/CN203404781U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/34Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery

Landscapes

  • Gasification And Melting Of Waste (AREA)
  • Fluidized-Bed Combustion And Resonant Combustion (AREA)

Abstract

The utility model belongs to the technical field of sludge treatment, and particularly relates to a sludge carbonization material incineration device which comprises a vertically-arranged incinerator body, an air distributing plate, a cyclone separator, an induced draft fan, a heat exchanger, an air preheater and a secondary air channel. The air distributing plate separates the incinerator body into a main combustion chamber and a primary air chamber which are communicated up and down. A limestone inlet and a carbonization material inlet are formed in the side wall of the main combustion chamber. A primary air channel is connected to the side wall of the primary air chamber. A smoke inlet and a material falling opening of the cyclone separator are communicated with the upper portion and the lower portion of the main combustion chamber respectively. A smoke conveying pipeline is connected between a smoke discharging opening of the cyclone separator and the induced draft fan. The heat exchanger and the air preheater are arranged on the smoke conveying pipeline in the smoke-flowing direction. The primary air channel penetrates through the air preheater. The secondary air channel is communicated with the main combustion chamber and the smoke discharging opening of the cyclone separator. Carbonization material independent stable combustion can be achieved, the using quantity of auxiliary fuel is lowered, the generating quantity of oxynitride is lowered, atmosphere pollution is avoided, desulfuration cost is lowered, and waste heat is recycled.

Description

Mud carbonized stock incinerator
Technical field
The utility model belongs to technical field of sludge treatment, relates in particular to a kind of mud carbonized stock incinerator.
Background technology
The calorific value of the mud carbonized stock made from mud is very low, and smooth combustion separately adopts the mode of mud carbonized stock and coal or other auxiliary fuel multifuel combustions to carry out burning disposal conventionally.Along with the sharply increase of sewage plant sludge quantity, a large amount of mud carbonized stock of meeting generation in sludge handling process, so just need to consume a large amount of coals or other auxiliary fuels burn jointly.
In combustion process, can produce a large amount of nitrogen oxide (NO x) be discharged in atmosphere, can contaminated air.
Utility model content
The technical problems to be solved in the utility model is: a kind of mud carbonized stock incinerator is provided, to realize the independent smooth combustion of mud carbonized stock, reduces the use amount of auxiliary fuel, reduce the generation of nitrogen oxide, prevent atmosphere pollution, reduce desulphurization cost, recycle waste heat.
The utility model is to realize like this, a kind of mud carbonized stock incinerator, described mud carbonized stock incinerator comprises: the vertical burning body of heater arranging, in the burner hearth of described burning body of heater, be provided with air distribution plate, described air distribution plate is divided into described burning body of heater main chamber and the air compartment communicating up and down, the sidewall of described main chamber is provided with lime stone import, carbonized stock import, and the sidewall of a described air compartment is provided with the air channel communicating with wind regime;
Cyclone separator, the smoke air inlet of described cyclone separator is connected with the top of described main chamber, and its blanking port is connected with the bottom of described main chamber;
Air-introduced machine, is connected with smoke conveying duct between the flue gas exhaust mouth of described air-introduced machine and described cyclone separator; On described smoke conveying duct, along flow of flue gas direction, be provided with heat exchanger, air preheater, a described air channel is through described air preheater;
Secondary air duct, described secondary air duct is connected between the flue gas exhaust mouth and described main chamber of described cyclone separator.
As a kind of improvement, on described smoke conveying duct, be serially connected with active carbon adsorber, described active carbon adsorber is between described air preheater and described air-introduced machine.
Owing to adopting technique scheme, when the mud carbonized stock incinerator that the utility model provides moves, from lime stone import, carbonized stock import, in main chamber, add lime stone and carbonized stock respectively, the lime stone adding and mud carbonized stock are burnt jointly, can carry out desulphurization reaction to mud carbonized stock, remove the sulphur in carbonized stock; Wind enters in main chamber through air compartment and air distribution plate after air preheater preheating again, contributes to mud carbonized stock fully to burn; The smoke air inlet of cyclone separator is connected with the top of main chamber, and blanking port is communicated with the bottom of main chamber, can send the inert bed material of separating back to main chamber; Secondary Air, for separate a part for flue gas from cyclone separator, enters the top of main chamber by secondary air duct, nitrogen in dilution stove, controls the generation of nitrogen oxide; The waste heat of the high-temperature flue gas that the heat exchanger recoverable burning being connected in series on smoke conveying duct produces, air preheater can carry out preheating to the air entering from air channel, from cyclone separator most of flue gas out, through heat exchanger and air preheater, carry out after heat exchange, temperature is down to 180 ℃ and following through air-introduced machine, pumped to chimney and drain.
The mud carbonized stock incinerator that the utility model provides can be realized the independent smooth combustion of carbonized stock, reduces the use amount of auxiliary fuel, and the generation that reduces nitrogen oxide prevents atmosphere pollution, reduces desulphurization cost, recycles waste heat.
Accompanying drawing explanation
Fig. 1 is the structural representation of mud carbonized stock incinerator of the present utility model;
Wherein, 10, burn body of heater, 11, air distribution plate, 12, main chamber, 13, air compartments, 14, lime stone import, 15, carbonized stock import, 16, air channels, 17, cyclone separator, 18, air-introduced machine, 19, heat exchanger, 20, air preheater, 21, active carbon adsorber, 22, smoke conveying duct, 23, secondary air duct, 24, residue discharge pipe.
The specific embodiment
In order to make the purpose of this utility model, technical scheme and advantage clearer, below in conjunction with drawings and Examples, the utility model is further elaborated.Should be appreciated that specific embodiment described herein is only in order to explain the utility model, and be not used in restriction the utility model.
As shown in Figure 1, this mud carbonized stock incinerator comprises: the vertical burning body of heater 10 arranging, in the burner hearth that burns body of heater 10, be provided with air distribution plate 11, this air distribution plate 11 is divided into burning body of heater 10 main chamber 12 and the air compartment 13 communicating up and down, the sidewall of this main chamber 12 is provided with lime stone import 14, carbonized stock import 15, the bottom of this main chamber 12 is provided with for discharging the sidewall of 24, air compartments 13 of residue discharge pipe of combustion residue and is provided with the air channel 16 communicating with wind regime; Cyclone separator 17, the smoke air inlet of this cyclone separator 17 is connected with the top of main chamber 12, and its blanking port is connected with the bottom of main chamber 12; Air-introduced machine 18, is connected with smoke conveying duct 22 between this air-introduced machine 18 and the flue gas exhaust mouth of cyclone separator 17; Along flow of flue gas direction, be arranged on heat exchanger 19, air preheater 20, the active carbon adsorber 21 on smoke conveying duct 22, this air channel 16 is through air preheater 20; And the flue gas exhaust mouth of connection cigarette cyclone separator 17 and the secondary air duct 23 between main chamber 12.
In the present embodiment, the quartz sand that main chamber 12 employing average diameters are 0.6mm is as inert bed material, from lime stone import 14, carbonized stock import 15 toward the interior interpolation lime stone of main chamber 12 and carbonized stock, add lime stone and carbonized stock jointly to burn respectively, can remove the sulphur in carbonized stock; Wind enters in main chamber 12 through air compartment 13 and air distribution plate 11 after air preheater 20 preheatings again; The smoke air inlet of cyclone separator 17 is connected with the top of main chamber 12, and blanking port is communicated with the bottom of main chamber 12, can send the inert bed material of separating back to main chamber 12; Secondary Air, for separate a part for flue gas from cyclone separator 17, enters the top of main chamber 12 by secondary air duct 23, nitrogen in dilution stove, controls the generation of nitrogen oxide; On smoke conveying duct 22, be serially connected with heat exchanger 19, air preheater 20, can carry out preheating to the gas entering from air channel 16, from cyclone separator 17 most of flue gas out, through heat exchanger 19 and air preheater 20, carry out after heat exchange, temperature is down to 180 ℃ and following through air-introduced machine 18, pumped to chimney and drain; Can realize the independent smooth combustion of carbonized stock, reduce the use amount of auxiliary fuel, the generation that reduces nitrogen oxide prevents atmosphere pollution, reduces desulphurization cost, recycles waste heat.
The mud carbonized stock incinerator that the utility model provides comprises: the vertical burning body of heater arranging, in the burner hearth that burns body of heater, be provided with air distribution plate, this air distribution plate is divided into burning body of heater main chamber and the air compartment communicating up and down, the sidewall of this main chamber is provided with lime stone import, carbonized stock import, and the sidewall of an air compartment is provided with the air channel communicating with wind regime; Cyclone separator, the smoke air inlet of this cyclone separator is connected with the top of main chamber, and its blanking port is connected with the bottom of main chamber; Air-introduced machine, is provided with smoke conveying duct between the flue gas exhaust mouth of this air-introduced machine and cyclone separator; On smoke conveying duct, along flow of flue gas direction, be provided with heat exchanger, air preheater, this air preheater is communicated with an air channel; And be arranged on the flue gas exhaust mouth of cigarette cyclone separator and the secondary air duct between main chamber; Can realize the independent smooth combustion of carbonized stock, reduce the use amount of auxiliary fuel, the generation that reduces nitrogen oxide prevents atmosphere pollution, reduces desulphurization cost, recycles waste heat.
The foregoing is only preferred embodiment of the present utility model; not in order to limit the utility model; all any modifications of doing within spirit of the present utility model and principle, be equal to and replace and improvement etc., within all should being included in protection domain of the present utility model.

Claims (2)

1. mud carbonized stock incinerator, is characterized in that, described mud carbonized stock incinerator comprises:
The vertical burning body of heater arranging, in the burner hearth of described burning body of heater, be provided with air distribution plate, described air distribution plate is divided into described burning body of heater main chamber and the air compartment communicating up and down, the sidewall of described main chamber is provided with lime stone import, carbonized stock import, and the sidewall of a described air compartment is provided with the air channel communicating with wind regime;
Cyclone separator, the smoke air inlet of described cyclone separator is connected with the top of described main chamber, and its blanking port is connected with the bottom of described main chamber;
Air-introduced machine, is connected with smoke conveying duct between the flue gas exhaust mouth of described air-introduced machine and described cyclone separator; On described smoke conveying duct, along flow of flue gas direction, be provided with heat exchanger, air preheater, a described air channel is through described air preheater;
Secondary air duct, described secondary air duct is connected between the flue gas exhaust mouth and described main chamber of described cyclone separator.
2. mud carbonized stock incinerator according to claim 1, is characterized in that, on described smoke conveying duct, is serially connected with active carbon adsorber, and described active carbon adsorber is between described air preheater and described air-introduced machine.
CN201320384667.7U 2013-06-28 2013-06-28 Sludge carbonization material incineration device Expired - Fee Related CN203404781U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201320384667.7U CN203404781U (en) 2013-06-28 2013-06-28 Sludge carbonization material incineration device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201320384667.7U CN203404781U (en) 2013-06-28 2013-06-28 Sludge carbonization material incineration device

Publications (1)

Publication Number Publication Date
CN203404781U true CN203404781U (en) 2014-01-22

Family

ID=49940714

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201320384667.7U Expired - Fee Related CN203404781U (en) 2013-06-28 2013-06-28 Sludge carbonization material incineration device

Country Status (1)

Country Link
CN (1) CN203404781U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106765211A (en) * 2016-12-07 2017-05-31 洛阳明远石化技术有限公司 Catalytic cracking flue gas processing unit
CN108019764A (en) * 2016-11-02 2018-05-11 天津天控科技有限公司 A kind of sludge incineration device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108019764A (en) * 2016-11-02 2018-05-11 天津天控科技有限公司 A kind of sludge incineration device
CN106765211A (en) * 2016-12-07 2017-05-31 洛阳明远石化技术有限公司 Catalytic cracking flue gas processing unit
CN106765211B (en) * 2016-12-07 2024-01-09 洛阳明远石化技术有限公司 Catalytic cracking flue gas treatment device

Similar Documents

Publication Publication Date Title
CN205424878U (en) Biomass steam boiler
CN203215693U (en) Environment-friendly dust-collecting cleaning incinerator for combustible waste batteries
CN103939890A (en) Coal produced gas integration chain grate boiler
CN104964286A (en) Sludge treatment method capable of reducing discharge of nitrogen oxide in pulverized coal boiler at the same time
CN203404781U (en) Sludge carbonization material incineration device
CN206310480U (en) A kind of burner hearth for realizing NOx reduction reactions
CN203785241U (en) Thrice combusting hot-air boiler
CN116697359B (en) Folding three-effect fire grate process
CN103322676B (en) A kind of biomass fuel hot air apparatus
CN203549845U (en) Grate-fired furnace co-processing dangerous waste burning system
CN201680717U (en) Circulating fluid bed boiler for stone coal decarburization
CN102252325B (en) Circulating fluidized bed boiler capable of burning rice husks
CN203744230U (en) Coal production gas integrated chain grate boiler
CN202494117U (en) Paratactic type half gasification household garbage digestion furnace
CN201212685Y (en) Urban refuse fuel decomposition and gasification incinerator structure
CN103292317A (en) Small-and-medium-size industrial boiler capable of replacing coal powder and oil gas
CN100381756C (en) Method for high temperature borning away refuse and its equipment
CN210267247U (en) Mixed combustion stove and garbage gasification incinerator
CN202229394U (en) Energy-saving emission-reducing fire tube boiler with stock bin
CN201983272U (en) Novel solid waste incinerator
CN101545636A (en) Process and device for reclaiming blown gas made from coal and by oxygen-enriched combustion
CN203784962U (en) Multi-hearth-furnace sludge incineration device with secondary combustor
CN201137944Y (en) Mixed combustion apparatus
CN205481007U (en) Waste incinerator partly gasifies
CN203123958U (en) Chemical reaction furnace utilizing solid fuel

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C56 Change in the name or address of the patentee

Owner name: SHANDONG HONGLI HOT PUMP ENERGY CO., LTD.

Free format text: FORMER NAME: SHANDONG HONGLI AIR CONDITIONING EQUIPMENT CO., LTD.

CP01 Change in the name or title of a patent holder

Address after: 261205 Shandong Province, Weifang city high tech Development Zone Hui Yin Road No. 2751

Patentee after: SHANDONG HONGLI PUMP ENERGY CO., LTD.

Address before: 261205 Shandong Province, Weifang city high tech Development Zone Hui Yin Road No. 2751

Patentee before: Shandong Hongli Air-Conditioning Equipment Co., Ltd.

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

Granted publication date: 20140122

Termination date: 20160628

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