CN110396432A - A kind of Horizontal water cooling wall type plasma gasification furnace - Google Patents
A kind of Horizontal water cooling wall type plasma gasification furnace Download PDFInfo
- Publication number
- CN110396432A CN110396432A CN201910681376.6A CN201910681376A CN110396432A CN 110396432 A CN110396432 A CN 110396432A CN 201910681376 A CN201910681376 A CN 201910681376A CN 110396432 A CN110396432 A CN 110396432A
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- 238000001816 cooling Methods 0.000 title claims abstract description 51
- 238000009272 plasma gasification Methods 0.000 title claims abstract description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 14
- 238000002309 gasification Methods 0.000 claims abstract description 36
- 230000015572 biosynthetic process Effects 0.000 claims abstract description 19
- 238000003786 synthesis reaction Methods 0.000 claims abstract description 19
- 238000002407 reforming Methods 0.000 claims abstract description 13
- 239000000498 cooling water Substances 0.000 claims description 14
- 238000000197 pyrolysis Methods 0.000 claims 1
- 235000021050 feed intake Nutrition 0.000 abstract description 4
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 abstract description 3
- 239000011248 coating agent Substances 0.000 abstract description 3
- 238000000576 coating method Methods 0.000 abstract description 3
- 239000003063 flame retardant Substances 0.000 abstract description 3
- 239000007789 gas Substances 0.000 description 15
- 238000005516 engineering process Methods 0.000 description 5
- 239000002699 waste material Substances 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 3
- 239000010813 municipal solid waste Substances 0.000 description 3
- 239000011819 refractory material Substances 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 238000004056 waste incineration Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000004035 construction material Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 239000002920 hazardous waste Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 230000000306 recurrent effect Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000000844 transformation Methods 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/02—Fixed-bed gasification of lump fuel
- C10J3/20—Apparatus; Plants
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/46—Gasification of granular or pulverulent flues in suspension
- C10J3/48—Apparatus; Plants
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/72—Other features
- C10J3/74—Construction of shells or jackets
- C10J3/76—Water jackets; Steam boiler-jackets
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
- C10J2300/0913—Carbonaceous raw material
- C10J2300/0946—Waste, e.g. MSW, tires, glass, tar sand, peat, paper, lignite, oil shale
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/12—Heating the gasifier
- C10J2300/123—Heating the gasifier by electromagnetic waves, e.g. microwaves
- C10J2300/1238—Heating the gasifier by electromagnetic waves, e.g. microwaves by plasma
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Gasification And Melting Of Waste (AREA)
Abstract
The invention discloses a kind of Horizontal water cooling wall type plasma gasification furnace, gasification furnace is horizontal type structure, and burner hearth is divided into three sections, is followed successively by pyrolytic gasification section, second-time burning section, synthesis gas reforming sections from feed end to outlet extreme direction;Piece plasmatorch of top arranged off-centre of gasification furnace feed side;Pyrolytic gasification section is connected with feed system;Second-time burning section and pyrolytic gasification section cohesive position lay wind-supplying mouth, and wind-supplying mouth is tangential admission;Gasification furnace synthesis gas reforming sections end sets syngas outlet.Gasification furnace of the present invention is horizontal type structure, and inner wall is arranged three-stage water-cooling wall, protects entire burner hearth, and gasification furnace cost is greatly reduced in no setting is required flame retardant coating;Without considering the influence that is rapidly heated to refractory life, it can quickly open furnace and feed intake operation.
Description
Technical field
The invention belongs to gasification furnace fields, are related to a kind of plasma gasification furnace, in particular to a kind of Horizontal water cooling wall type
Plasma gasification furnace.
Background technique
Plasma gasification technology originate from earliest in the 1960s, U.S. NASA with its carry out material heat resistanceheat resistant test,
Start the seventies to start to process the solid waste such as medicine the eighties for metallurgy and material heat treatment industry, start in recent years
It attempts for handling city and industrial refuse.Different from traditional waste incineration mode, plasma gasification technology almost can be by rubbish
Rubbish 100% is converted into recyclable byproduct, and organic matter therein is converted into clean fuel gas (mainly CO and H2), can be direct
Burning or the fuels and chemicals for being refined into greater degree, and the harmless glassy state slag that inorganic matter melting generates is cooling
After can be used as construction material, be that waste incineration is most potential to realize real rubbish processing to be harmless and recycling application
A kind of substitute technology.(service life is long, stable) and plasma consumable are constantly improve with plasma generator technology
The continuous decline of electricity, converts China city and industrial refuse to using plasma gasification technology the ripe of the energy.
Existing plasma gasification furnace, mostly vertical structure, inboard wall of burner hearth are formed by refractory material laying, due to fire proofed wood
Expect expensive, cause gasification furnace cost higher, while because refractory material density is larger, causing gasification furnace apparatus body heavier,
It is not easy to transport, move.
Summary of the invention
For the defects in the prior art and insufficient, the present invention provides a kind of Horizontal water cooling wall type plasma gasification furnace,
The plasma gasification furnace feature: gasification stove internal wall is equipped with three-stage water-cooling wall, and gasification furnace is greatly reduced in no setting is required flame retardant coating
Cost;Without considering the influence that is rapidly heated to refractory life, it can quickly open furnace and feed intake operation.
In order to achieve the above objectives, the invention adopts the following technical scheme:
A kind of Horizontal water cooling wall type plasma gasification furnace, including furnace body, the furnace body is horizontal type structure, the two of furnace body
End is respectively feed end and outlet end, from feed end to being followed successively by interconnected pyrolytic gasification section, secondary combustion between outlet end
Burn section and synthesis gas reforming sections;The plasma torch of one with furnace body centerline axis parallel are arranged in the end face eccentric of feed end;
It is equipped with feed inlet in the feed end, is equipped with syngas outlet in the outlet end;Pyrolytic gasification section with it is secondary
It is circumferential outside the furnace wall of burning zone junction to be cased with sealing and mend air duct, offer wind-supplying mouth on mending air duct, wind-supplying mouth be tangentially into
Gas;The air inlet hole of perforation furnace wall is equipped on mending the corresponding furnace wall of air duct;
The pyrolytic gasification section, second-time burning section and the corresponding furnace wall of synthesis gas reforming sections are water-cooling wall, and three Duan Shui
It is not connected between cold wall;
Cooling water intake and cooling water outlet, and the cooling water on every section of water-cooling wall are equipped on every section of water-cooling wall
Water inlet is than cooling water outlet closer to outlet end.
The invention also includes following technical characteristics:
Specifically, the corresponding furnace wall of the feed end is columnar structured, and the feed inlet is located at the side wall of feed end
On, the central axis of feed inlet and the central axis upright of feed end but non-intersecting;Feed inlet is directly connected in furnace body;
The corresponding furnace wall of the pyrolytic gasification section includes the columnar leading portion and connection second-time burning section for connecting feed end
Taper flared back segment;The corresponding furnace wall of the second-time burning section is columnar structured;The synthesis gas reforming sections are corresponding
Furnace wall include connect second-time burning section columnar leading portion and taper shrink mouth shape back segment.
Specifically, being equipped on the end face of the corresponding furnace wall of back segment of the taper shrink mouth shape of the synthesis gas reforming sections described
Syngas outlet, the central axis of syngas outlet and the centerline axis parallel of furnace body.
Specifically, the water-cooling wall include water-cooling wall internal layer, water-cooling wall outer layer and be located at water-cooling wall internal layer and water-cooling wall
Middle layer between outer layer is equipped with the cooling blade of spiral on the intermediate layer.
Compared with prior art, the present invention beneficial has the technical effect that
Gasification furnace of the present invention is horizontal type structure, and inner wall is arranged three-stage water-cooling wall, protects entire burner hearth, fire resisting that no setting is required
Layer, is greatly reduced gasification furnace cost;Without considering the influence that is rapidly heated to refractory life, it can quickly open furnace and feed intake fortune
Row.
Detailed description of the invention
Fig. 1 is longitudinal profile structure schematic of the invention;
Fig. 2 is A-A cross section schematic diagram in Fig. 1;
Fig. 3 is B-B-section schematic cross-sectional view in Fig. 1;
Fig. 4 is that the I partial enlargement in Fig. 1 is intended to.
Each label indicates in figure are as follows: 1- furnace body, 2- feed end, and the outlet end 3-, 4- pyrolytic gasification section, 5- second-time burning section,
6- synthesis gas reforming sections, 7- plasma torch, 8- mend air duct, 9- air inlet hole, 10- water-cooling wall;
21- feed inlet, 31- syngas outlet, 81- wind-supplying mouth;
101- cooling water intake, 102- cooling water outlet, 103- water-cooling wall internal layer, 104- water-cooling wall outer layer, 105-
Middle layer, the cooling blade of 106- spiral.
Specific embodiment
Specific embodiments of the present invention are given below, it should be noted that the invention is not limited to implement in detail below
Example, all equivalent transformations made on the basis of the technical solutions of the present application each fall within protection scope of the present invention.
Embodiment 1:
As shown in Figures 1 to 4, the present invention provides a kind of Horizontal water cooling wall type plasma gasification furnace, is suitable for plasma
Body torch realizes the innoxious of danger wastes as the powdered of heat source, pulpous state, paste hazardous waste disposal.With routine
Plasma gasification reacting furnace is compared, and difference is that the gasification furnace is horizontal type structure, and three-stage water-cooling wall is arranged in inner wall, is protected whole
A burner hearth, no setting is required flame retardant coating can quickly open furnace and feed intake operation.Material is fed from the feed inlet in furnace, gasification furnace feed side
The eccentrically mounted plasma torch in top provides energy for danger wastes thermal decomposition, danger wastes in furnace pyrolytic gasification,
Second-time burning, the synthesis gas for generation of gasifying carry fine particle and go to subsequent processing by gasification furnace end syngas outlet.This reality
The Horizontal water cooling wall type plasma gasification furnace of example, including furnace body 1 are applied, furnace body 1 is horizontal type structure, is distinguished at the both ends of furnace body 1
For feed end 2 and outlet end 3, from feed end 2 to being followed successively by interconnected pyrolytic gasification section 4, second-time burning between outlet end 3
Section 5 and synthesis gas reforming sections 6;The plasma torch of one with 1 centerline axis parallel of furnace body are arranged in the end face eccentric of feed end 2
7;It is equipped with feed inlet 21 in feed end 2, is equipped with syngas outlet 31 in outlet end 3;In pyrolytic gasification section 4 and second-time burning section 5
It is circumferential outside the furnace wall of junction to be cased with sealing and mend air duct 8, offer wind-supplying mouth 81 on mending air duct 8, wind-supplying mouth 81 be tangentially into
Gas;The air inlet hole 9 of perforation furnace wall is equipped on mending the corresponding furnace wall of air duct 8;Pyrolytic gasification section 4, second-time burning section 5 and synthesis gas
The corresponding furnace wall of reforming sections 6 is water-cooling wall 10, and is not connected between three sections of water-cooling walls 10;It is equipped on every section of water-cooling wall 10
Cooling water intake 101 and cooling water outlet 102, and the cooling water intake 101 on every section of water-cooling wall 10 goes out than cooling water
The mouth of a river 102 is closer to outlet end 3.
In the present embodiment, the corresponding furnace wall of feed end 2 is columnar structured, and feed inlet 21 is located at the side of feed end 2
On wall, the central axis of feed inlet 21 and the central axis upright of feed end 2 but non-intersecting;Feed inlet 21 is directly connected to furnace body
In 1;The corresponding furnace wall of pyrolytic gasification section 4 includes the columnar leading portion for connecting feed end 2 and the taper of connection second-time burning section 5
The back segment of flared;The corresponding furnace wall of second-time burning section 5 is columnar structured;The corresponding furnace wall of synthesis gas reforming sections 6 includes connecting
Connect the columnar leading portion of second-time burning section 5 and the back segment of taper shrink mouth shape.
More specifically, synthesis is equipped on the end face of the corresponding furnace wall of back segment of the taper shrink mouth shape of synthesis gas reforming sections 6
Gas outlet 31, the central axis of syngas outlet 31 and the centerline axis parallel of furnace body 1.
In the present embodiment, water-cooling wall 10 is including water-cooling wall internal layer 103, water-cooling wall outer layer 104 and is located at water-cooling wall internal layer
Middle layer 105 between 103 and water-cooling wall outer layer 104 is equipped with the cooling blade 106 of spiral on the intermediate layer.
The specific work process of the present embodiment is as follows:
Start the plasma torch for being installed on gasification furnace feed side top first, reach stable operation, controls temperature pre-
Determine range, while the water in water-cooling wall being made to enter recurrent state;Again by danger wastes using pneumatic conveying or pumping mode by
Gasification furnace feed inlet enters in furnace, while axially uniformly distributed wind-supplying mouth is passed through from second-time burning section and pyrolytic gasification section cohesive position
Pyrolytic gasification process occurs for certain air, danger wastes, and the synthesis gas that pyrolytic gasification generates fires completely in second-time burning section
It burns, then the syngas outlet through synthesis gas reformer section goes to subsequent processing.
A specific embodiment of the invention is described in detail in conjunction with attached drawing above, still, the present invention is not limited to above-mentioned realities
The detail in mode is applied, within the scope of the technical concept of the present invention, a variety of letters can be carried out to technical solution of the present invention
Monotropic type, these simple variants all belong to the scope of protection of the present invention.
It is further to note that specific technical features described in the above specific embodiments, in not lance
In the case where shield, can be combined in any appropriate way, in order to avoid unnecessary repetition, the present invention to it is various can
No further explanation will be given for the combination of energy.
In addition, various embodiments of the present invention can be combined randomly, as long as it is without prejudice to originally
The thought of invention, it should also be regarded as the disclosure of the present invention.
Claims (4)
1. a kind of Horizontal water cooling wall type plasma gasification furnace, including furnace body (1), which is characterized in that the furnace body (1) is horizontal
Structure is respectively feed end (2) and outlet end (3) at the both ends of furnace body (1), from feed end (2) between outlet end (3) successively
For interconnected pyrolytic gasification section (4), second-time burning section (5) and synthesis gas reforming sections (6);It is inclined in the end face of feed end (2)
The heart arranges the plasma torch (7) of one with furnace body (1) centerline axis parallel;
Feed inlet (21) are equipped in the feed end (2), are equipped with syngas outlet (31) in the outlet end (3);In pyrolysis gas
Change circumferential be cased with outside the furnace wall of section (4) and second-time burning section (5) junction and seal benefit air duct (8), is offered on mending air duct (8)
Wind-supplying mouth (81), wind-supplying mouth (81) are tangential admission;The air inlet hole of perforation furnace wall is equipped on mending air duct (8) corresponding furnace wall
(9);
The pyrolytic gasification section (4), second-time burning section (5) and the corresponding furnace wall of synthesis gas reforming sections (6) are water-cooling wall (10),
And it is not connected between three sections of water-cooling walls (10);
Cooling water intake (101) and cooling water outlet (102), and every section of water-cooling wall are equipped on every section of water-cooling wall (10)
(10) cooling water intake (101) on is than cooling water outlet (102) closer to outlet end (3).
2. Horizontal water cooling wall type plasma gasification furnace as described in claim 1, which is characterized in that the feed end (2) is right
The furnace wall answered is columnar structured, and the feed inlet (21) is located on the side wall of feed end (2), the central axis of feed inlet (21)
The central axis upright of line and feed end (2) but non-intersecting;Feed inlet (21) is directly connected in furnace body (1);
The corresponding furnace wall of the pyrolytic gasification section (4) includes columnar leading portion and the connection second-time burning of connection feed end (2)
The back segment of the taper flared of section (5);The corresponding furnace wall of the second-time burning section (5) is columnar structured;The synthesis gas weight
Whole section (6) corresponding furnace wall includes the columnar leading portion of connection second-time burning section (5) and the back segment of taper shrink mouth shape.
3. Horizontal water cooling wall type plasma gasification furnace as claimed in claim 2, which is characterized in that reformed in the synthesis gas
The end face of the corresponding furnace wall of back segment of the taper shrink mouth shape of section (6) is equipped with the syngas outlet (31), syngas outlet
(31) centerline axis parallel of central axis and furnace body (1).
4. Horizontal water cooling wall type plasma gasification furnace as described in claim 1, which is characterized in that water-cooling wall (10) packet
Include water-cooling wall internal layer (103), water-cooling wall outer layer (104) and between water-cooling wall internal layer (103) and water-cooling wall outer layer (104)
Middle layer (105), it is cooling blade (106) to be equipped with spiral on the intermediate layer.
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CN201910681376.6A CN110396432A (en) | 2019-07-26 | 2019-07-26 | A kind of Horizontal water cooling wall type plasma gasification furnace |
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CN201910681376.6A CN110396432A (en) | 2019-07-26 | 2019-07-26 | A kind of Horizontal water cooling wall type plasma gasification furnace |
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2019
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JP2003227603A (en) * | 2002-02-06 | 2003-08-15 | Hitachi Metals Ltd | Direct melting furnace |
CN201448851U (en) * | 2009-07-17 | 2010-05-05 | 张建路 | Domestic garbage gasifying incinerator |
CN102226091A (en) * | 2011-05-18 | 2011-10-26 | 浙江工业大学 | Apparatus for producing synthetic gas by pyrolysis gasification of biomass |
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