CN206709083U - A kind of garbage pyrolysis gasification incinerator - Google Patents

A kind of garbage pyrolysis gasification incinerator Download PDF

Info

Publication number
CN206709083U
CN206709083U CN201720563272.1U CN201720563272U CN206709083U CN 206709083 U CN206709083 U CN 206709083U CN 201720563272 U CN201720563272 U CN 201720563272U CN 206709083 U CN206709083 U CN 206709083U
Authority
CN
China
Prior art keywords
pyrolysis
combustion chamber
heating chamber
flue gas
vaporizer
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
CN201720563272.1U
Other languages
Chinese (zh)
Inventor
李正安
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to CN201720563272.1U priority Critical patent/CN206709083U/en
Application granted granted Critical
Publication of CN206709083U publication Critical patent/CN206709083U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Gasification And Melting Of Waste (AREA)
  • Incineration Of Waste (AREA)

Abstract

The utility model discloses a kind of garbage pyrolysis gasification incinerator, including the body of heater being made up of furnace wall;Air compartment, heating chamber, pyrolysis vaporizer and pyrolysis combustion chamber are sequentially provided with the body of heater from bottom to up;Casting furnace grate is provided between the air compartment and heating chamber, water-cooled grate is provided between the heating chamber and pyrolysis vaporizer, pyrolysis gas passage is provided between the pyrolysis vaporizer and pyrolysis combustion chamber;The side wall of the heating chamber is provided with the first combustor;The side wall of the pyrolysis combustion chamber is provided with the second combustor, is provided with flue gas shunting device in pyrolysis combustion chamber, the both sides of flue gas shunting device are provided with overfire air jet.Its operational reliability is good, burning is abundant and the feature of environmental protection is more preferable.

Description

A kind of garbage pyrolysis gasification incinerator
Technical field
The utility model belongs to waste incinerator technical field, and in particular to a kind of garbage pyrolysis gasification incinerator.
Background technology
The fire grate of conventional garbage incinerator pyrolysis vaporizer is fabricated to gridiron, this fire grate with cast iron or cast steel 600 degrees Celsius are operated in being easily deformed or burn out under the conditions of 700 celsius temperatures, poor reliability.It is pyrolyzed combustion chamber not Secondary Air is set, and fuel and air mixing condition are poor, and flame combustion chamber flue-gas temperature is low, incomplete combustion, in the flue gas of discharge Containing not burning gas and flammable fly ash granule.
Utility model content
Based on this, in view of the above-mentioned problems, the utility model proposes a kind of operational reliability is good, burn abundant and environmental-protecting performance More preferable garbage pyrolysis gasification incinerator.
The technical solution of the utility model is:A kind of garbage pyrolysis gasification incinerator, including the body of heater being made up of furnace wall;Institute State and be sequentially provided with air compartment, heating chamber, pyrolysis vaporizer and pyrolysis combustion chamber in body of heater from bottom to up;The air compartment and heating chamber Between be provided with casting furnace grate, water-cooled grate, the pyrolysis vaporizer and pyrolysis are provided between the heating chamber and pyrolysis vaporizer Pyrolysis gas passage is provided between combustion chamber;The side wall of the heating chamber is provided with the first combustor;The pyrolysis combustion chamber Side wall be provided with the second combustor, is provided with flue gas shunting device in pyrolysis combustion chamber, the both sides of flue gas shunting device are provided with Overfire air jet.
Preferably, the angle between the water-cooled grate and horizontal plane is 5 degree to 20 degree, and cooling is connected with water-cooled grate Water.
Preferably, the flue gas shunting device is triangular prism shape, and flue gas shunting device is vertical at the pyrolysis gas burning It is indoor.
Preferably, lime-ash door and blast pipe are respectively equipped with the adjacent both walls of the air compartment.
Preferably, the side wall of the pyrolysis vaporizer is provided with upper furnace door.
Preferably, the side wall of the heating chamber is provided with lower furnace door.
Preferably, one end of the pyrolysis combustion chamber is provided with exhanst gas outlet.
The beneficial effects of the utility model are:
(1)Garbage pyrolysis gasification incinerator operational reliability provided by the utility model is good, and rubbish and pyrolysis gas burning are filled Point, and environmental-protecting performance is more preferable;
(2)Rubbish in pyrolysis vaporizer, cracked after the fire smoke gases heating risen in room is heated under poor oxygen condition Gasification, caused fixed carbon and a small amount of remaining rubbish are fallen on the casting furnace grate of heating chamber after gasification, then are burnt, and make rubbish Thoroughly burnt, reach sterilizing, the effect of decrement, meanwhile, fixed carbon and remaining rubbish burn again caused by heat can be to heat Rubbish in solution vaporizer continues heating and gasifying, has saved the heating fuel of the first combustor, reduces incinerator operation Cost;
(3)Flue gas shunting installation weight is big, and amount of stored heat is big, promotes flameholding to carry out;Flue gas shunting device both sides and stove Road narrows circulation section between wall is small, and flue gas flow rate is high, promotes air to be sufficiently mixed with not burning gas and flammable fly ash granule, Burning is enhanced, pyrolysis gas is fully burnt;
(4)The Secondary Air flow velocity that overfire air jet sprays is high, at the Road narrows between flue gas shunting device and furnace wall and hot Vent one's spleen strong disturbance, strengthen the mixing of pyrolysis gas and air, enhance burning, make pyrolysis gas burning more abundant;
(5)During work, cooling water is connected with water-cooled grate, it can be made to bear 500 degrees Celsius to 800 degrees Celsius of high temperature, Compared with traditional fire grate, it will not be burned, reliability is high;
(6)Water-cooled grate is tilted horizontal by 5-20 degree and installed by steel pipe is in parallel or paliform in series, cooling Water enters from the low level of water-cooled grate, and a high position goes out, can effective cooling pipe, ensure that steel pipe heating surface operating temperature is stable 130 It is safe and reliable to operation degree Celsius in 350 degrees Celsius.
Brief description of the drawings
Fig. 1 is the sectional view of garbage pyrolysis gasification incinerator described in embodiment;
Fig. 2 is the A-A sectional views in Fig. 1;
Fig. 3 is the B-B sectional views in Fig. 1;
Description of reference numerals:
1 air compartment, 2 heating chambers, 3 pyrolysis vaporizer, 4 pyrolysis combustion chambers, 5 casting furnace grates, 6 water-cooled grates, 7 pyrolysis gas lead to Road, 8 overfire air jets, 9 flue gas shunting devices, 10 first combustors, 11 second combustors, 12 exhanst gas outlets, 13 upper furnace doors, 14 Lime-ash door, 15 blast pipes, 16 furnace walls, 17 bodies of heater, 18 bases, 19 lower furnace doors.
Embodiment
Embodiment of the present utility model is described in detail below in conjunction with the accompanying drawings.
Embodiment:
As shown in Figure 1, Figure 2 and Figure 3, a kind of garbage pyrolysis gasification incinerator, including the body of heater 17 being made up of furnace wall 16;Institute State and be sequentially provided with air compartment 1, heating chamber 2, pyrolysis vaporizer 3 and pyrolysis combustion chamber 4 in body of heater 17 from bottom to up;The air compartment 1 Casting furnace grate 5 is provided between heating chamber 2, water-cooled grate 6, the pyrolysis are provided between the heating chamber 2 and pyrolysis vaporizer 3 Pyrolysis gas passage 7 is provided between vaporizer 3 and pyrolysis combustion chamber 4;The side wall of the heating chamber 2 is provided with the first combustor 10;The side wall of the pyrolysis combustion chamber 4 is provided with the second combustor 11, and flue gas shunting device is provided with pyrolysis combustion chamber 4 9, the both sides of flue gas shunting device 9 are provided with overfire air jet 8.
In another embodiment, the angle between the water-cooled grate 6 and horizontal plane is 5 degree, can also 15 degree or 20 degree, cooling water is connected with water-cooled grate 6.
In another embodiment, the flue gas shunting device 9 is triangular prism shape, and flue gas shunting device 9 is vertical at institute State in pyrolysis combustion chamber 4.
In another embodiment, lime-ash door 14 and blast pipe 15 are respectively equipped with the adjacent both walls of the air compartment 1.
In another embodiment, the side wall of the pyrolysis vaporizer 3 is provided with upper furnace door 13.
In another embodiment, the side wall of the heating chamber is provided with lower furnace door 19.
In another embodiment, one end of the pyrolysis combustion chamber 4 is provided with exhanst gas outlet 12.
In another embodiment, the bottom of the body of heater 17 is provided with base 18.
Operation principle is as follows:
Refuse pyrolysis gasification is a kind of endothermic reaction process, need to have and successively rubbish is heated.Refuse gasification institute The heat needed, along with the first combustor 10 burns, caused heat provides heat as caused by incineration firing.Can be by this Rubbish handled by incinerator is divided into 2 classes:A, for carried out after pyrolytic gasification burn processing rubbish, account for garbage disposal total amount 85%;B, 15% rubbish that remaining moisture content is less and composition containing combustible is more carries out burning processing in heating chamber 2, produces Heat go for other 85% refuse pyrolysis gasification.Cracked using heat caused by the more incineration firing of combustible composition Gasify remaining 85% rubbish, reduce cracking gasification needed for fuel, saved cost.
During work, from the input of lower furnace door 19 rubbish that moisture content is less and composition containing combustible is more to casting furnace grate 5, Combustion air passes through outside pressure fan and enters air compartment 1 from blast pipe 15, then flows up into heating chamber 2, the first combustor 10 Start the rubbish lighted in heating chamber 2, produce heat, the rubbish in pyrolysis vaporizer 3 is gasified.
The rubbish for carrying out pyrolytic gasification is needed to be put into from upper furnace door 13 in pyrolysis vaporizer 3, in oxygen deprivation(Excess air coefficient ﹤ 0.3)It is heated under state and carries out pyrolytic gasification, caused pyrolysis gas enters pyrolysis combustion chamber 4 through pyrolysis gas passage 7, through the The ignition of two combustor 11, when being pyrolyzed the chamber flue gas temperature of combustion chamber 4 higher than 900 DEG C, the second combustor 11 closes automatically Machine, pyrolysis gas are lighted, continuously and stably burnt, and saved the fuel of the second combustor 11 automatically by scorching hot radiation of burner hearth heat Consumption.When as little as 890 DEG C of chamber flue gas temperature, the second combustor automatic ignition, continue it is stable burn, it is safe and reliable to operation.
Wherein, the main function of the first combustor 10 is that igniting and increase heating chamber 2 are supplied needed for refuse pyrolysis gasification Heat, the second combustor 11 have igniting, stable burning and ensure that the fire smoke gases temperature in pyrolysis combustion chamber 4 exists all the time More than 890 degrees Celsius of function, the effect for the Zhong bioxin that removes smoke is reached;First combustor 10 and the second combustor 11 Fuel uses diesel oil, natural gas or liquefied gas.
Flue gas shunting device 9 and overfire air jet 8 are provided with combustion chamber 4 is pyrolyzed, overfire air jet 8 is arranged on pyrolysis The top of combustion chamber 4, at the Road narrows between its air outlet face furnace side wall and flue gas shunting device 9.Overfire air jet 8 sprays Secondary Air at Road narrows with pyrolysis gas strong disturbance, strengthen the mixing of pyrolysis gas and air, enhance burning.Flue gas shunting Device 9 is made up of refractory material, be vertically installed at pyrolysis combustion chamber 4 longitudinal centre line it is latter half of.Flue gas shunting fills Put that 9 weight are big, and amount of stored heat is big, promote flameholding.The both sides of flue gas shunting device 9 Road narrows circulation section it is small, promote air with The flue gas not burnt is sufficiently mixed, and enhances burning.Finally, the flue gas in incinerator in the presence of air-introduced machine draft through flue gas Export and excluded at 12, the lime-ash after burning is removed from lime-ash door 14.
Water-cooled grate 6 is arranged between heating chamber 2 and pyrolysis vaporizer 3, and during work, cooling water is connected with water-cooled grate 6, It can be made to bear 500 degrees Celsius to 800 degrees Celsius of high temperature, compared with traditional fire grate, will not be burned;Water-cooled grate 6 is by steel Pipe is in parallel or paliform in series, and installation is tilted horizontal by 5 degree, or 15 degree or 20 degree inclinations are installed, cold But the low level of water from water-cooled grate 6 enters, and a high position goes out, can effective cooling pipe, ensure that steel pipe heating surface operating temperature is stable and exist It is 130 degrees Celsius to 350 degrees Celsius, safe and reliable to operation.
Embodiment described above only expresses specific embodiment of the present utility model, and its description is more specific and detailed, But therefore it can not be interpreted as the limitation to the utility model patent scope.It should be pointed out that for the common of this area For technical staff, without departing from the concept of the premise utility, various modifications and improvements can be made, these all belong to In the scope of protection of the utility model.

Claims (7)

  1. A kind of 1. garbage pyrolysis gasification incinerator, it is characterised in that:Including the body of heater being made up of furnace wall;In the body of heater from it is lower to On be sequentially provided with air compartment, heating chamber, pyrolysis vaporizer and pyrolysis combustion chamber;Cast-iron stove is provided between the air compartment and heating chamber Row, water-cooled grate is provided between the heating chamber and pyrolysis vaporizer, is set between the pyrolysis vaporizer and pyrolysis combustion chamber There is pyrolysis gas passage;The side wall of the heating chamber is provided with the first combustor;The side wall of the pyrolysis combustion chamber is provided with the Two combustors, pyrolysis combustion chamber is interior to be provided with flue gas shunting device, and the both sides of flue gas shunting device are provided with overfire air jet.
  2. 2. garbage pyrolysis gasification incinerator according to claim 1, it is characterised in that:The water-cooled grate and horizontal plane it Between angle be 5 degree to 20 degree, cooling water is connected with water-cooled grate.
  3. 3. garbage pyrolysis gasification incinerator according to claim 1 or 2, it is characterised in that:The flue gas shunting device is Triangular prism shape, flue gas shunting device are vertical in the pyrolysis combustion chamber.
  4. 4. garbage pyrolysis gasification incinerator according to claim 3, it is characterised in that:In the adjacent both walls of the air compartment It is respectively equipped with lime-ash door and blast pipe.
  5. 5. according to the garbage pyrolysis gasification incinerator described in claim 1 or 2 or 4, it is characterised in that:The pyrolysis vaporizer Side wall is provided with upper furnace door.
  6. 6. garbage pyrolysis gasification incinerator according to claim 5, it is characterised in that:The side wall of the heating chamber is provided with Lower furnace door.
  7. 7. garbage pyrolysis gasification incinerator according to claim 5, it is characterised in that:One end of the pyrolysis combustion chamber Provided with exhanst gas outlet.
CN201720563272.1U 2017-05-19 2017-05-19 A kind of garbage pyrolysis gasification incinerator Expired - Fee Related CN206709083U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720563272.1U CN206709083U (en) 2017-05-19 2017-05-19 A kind of garbage pyrolysis gasification incinerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720563272.1U CN206709083U (en) 2017-05-19 2017-05-19 A kind of garbage pyrolysis gasification incinerator

Publications (1)

Publication Number Publication Date
CN206709083U true CN206709083U (en) 2017-12-05

Family

ID=60464853

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201720563272.1U Expired - Fee Related CN206709083U (en) 2017-05-19 2017-05-19 A kind of garbage pyrolysis gasification incinerator

Country Status (1)

Country Link
CN (1) CN206709083U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109681886A (en) * 2019-01-30 2019-04-26 陕西标远环境工程有限公司 A kind of vertical rotating pyrolysis gasification furnace

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109681886A (en) * 2019-01-30 2019-04-26 陕西标远环境工程有限公司 A kind of vertical rotating pyrolysis gasification furnace
CN109681886B (en) * 2019-01-30 2024-01-23 陕西标远环保科技有限公司 Vertical rotary pyrolysis gasifier

Similar Documents

Publication Publication Date Title
CN1916490B (en) Smokeless burning technique and equipment with fire fontanel being setup inside furnace
CN201014475Y (en) Solid fuel gasification combustion boiler
CN106931451B (en) Spiral-flow type incinerator
CN206709083U (en) A kind of garbage pyrolysis gasification incinerator
CN101126504B (en) Coal continuous cleaning burning device and method
JP4589832B2 (en) Incinerator
CN201262412Y (en) Biomass semi-gasification domestic boiler
CN201513880U (en) Integral gasifying combination burning boiler
CN2901154Y (en) Gasifying room burning boiler
CN201014730Y (en) Solid fuel side-set type combustion furnace
CN2864469Y (en) Vertical three-room gas boiler for coal gasification
CN201225756Y (en) Spherical briquette boiler
CN201748474U (en) Air-conditioning wood/coal gasification furnace
CN201697112U (en) Boiler combusting biomass fuel gas
CN200940928Y (en) Forward/reverse purifying burning boiler having coal gasifying 3 chambers
CN221036208U (en) Biomass-fired hot blast stove
CN103759415A (en) Energy-saving environment-friendly type back burning boiler
CN201310876Y (en) Gas-making compound combustion chain furnace
CN102818265A (en) Application of heat-accumulating high-temperature air burning method in burner and burning furnace
CN202852828U (en) Burning type wet combustion furnace
CN201954527U (en) Spiral automatic feed combustion boiler
CN101413658B (en) Gas making compound combustion chain furnace
CN102878564B (en) Counter-burning wet combustion furnace
CN201382405Y (en) Solid fuel combustion system for split-type boiler
CN201262424Y (en) Household coal and gas integrated boiler

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20171205

Termination date: 20190519