CN206094094U - Spiral propulsive type solid waste continuous carbonization equipment - Google Patents

Spiral propulsive type solid waste continuous carbonization equipment Download PDF

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Publication number
CN206094094U
CN206094094U CN201620652117.2U CN201620652117U CN206094094U CN 206094094 U CN206094094 U CN 206094094U CN 201620652117 U CN201620652117 U CN 201620652117U CN 206094094 U CN206094094 U CN 206094094U
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China
Prior art keywords
carbonization
feed
deodorization
collection
conveying worm
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Expired - Fee Related
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CN201620652117.2U
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Chinese (zh)
Inventor
张立波
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Chenghe Environment Protection Scien-Tech Co Ltd
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Chenghe Environment Protection Scien-Tech Co Ltd
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Abstract

The utility model provides a spiral propulsive type solid waste continuous carbonization equipment, its characteristics are: including the charge -in system, material distribution system, carbonization system, result collecting system and the ejection of compact system that connect gradually, form sealing connection's screw propulsion material channel, carbonization headtotail deodorization system from the discharge gate of charge -in system's feed inlet to ejection of compact system. Charge -in system includes feed screw conveyer, feeding gear motor, an agitator motor, feed inlet, charge -in system's feed inlet is the back taper feeder hopper, and an agitator motor drive (mixing) shaft rotates, install the blade on the (mixing) shaft, the (mixing) shaft is located in charge -in system's the back taper feeder hopper. The commonality is strong, and produced carbonization result usage is extensive, can not produce secondary pollution, its is rational in infrastructure, compact, and its leakproofness is good, and the cost of manufacture is lower, degree of automation is high, and work efficiency is high.

Description

Screw-pushing type solid waste continuous carbonization equipment
Technical field
The utility model belongs to disposition of solid waste equipment manufacturing technology field, and specifically a kind of screw-pushing type is consolidated Body discarded object continuous carbonization equipment.
Background technology
The carbonizing apparatus or pyrolysis plant for occurring in the market are primarily used to process rubber, plastics, greasy filth, bamboo charcoal etc. Raw material, and be used to process the higher material of moisture content such as:The biomass solid waste such as weeds, branch, marine alga;Paper pulp, food debris etc. Industrial Solid Waste;The equipment of changing food waste, house refuse etc. is more rare.Traditional carbonization or cracking apparatus in processing procedure to producing Raw waste gas, only carries out simply physically or chemically adsorbing, and can produce secondary pollution.
Carbonization or cracking apparatus require that material is sealed in processing procedure, to improve the security of operating process.City The shortcomings of on field there is big floor space, high cost in the sealing device of existing equipment.Additionally, traditional carbonizing apparatus are due to processing Material is single, and the material of generation is commonly used for rubber black, roasts charcoal, makees fuel etc..
The content of the invention
The utility model is to solve the problems referred to above and the deficiency that prior art is present, there is provided a kind of screw-pushing type solid gives up Gurry continuous carbonization equipment, highly versatile, produced carbonized product is of many uses, will not produce secondary pollution;Its structure is closed Reason, it is compact, its good airproof performance, cost of manufacture is relatively low;High degree of automation, high working efficiency.
The purpose of this utility model is achieved through the following technical solutions:A kind of screw-pushing type solid waste is continuous Carbonizing apparatus, it is characterised in that including the feed system, material distributing system, carbonization system, the product collection system that are sequentially connected And discharge system, the screw propulsion being tightly connected is formed from the discharging opening of the charging aperture to the discharge system of the feed system Material channel, the carbonization system connects deodorizing system.
Improvement to above-mentioned technical proposal:The feed system include charging reducing motor, feeding spiral conveyer, first Stirring motor, the charging aperture, the charging aperture of the feed system is back taper feed hopper, described feeding spiral conveyer bag Include cylindrical housing, fixed first helical runner of the cylindrical housing inwall, first stirring motor drives a shaft Rotate, blade is installed on the shaft, the shaft is located in the back taper feed hopper of the feed system.
Further improvement to above-mentioned technical proposal:The carbonization system includes carbonization kiln, outer hot stove, outer hot stove burning Device, burning blower fan, temperature adjustment blower fan, carbonization kiln motor, carbonization kiln reductor, front-seat smoke-box, heel row smoke-box, the carbon Changing kiln includes two parallel interior pusher spiral carbonization kilns, and interior pusher spiral carbonization kiln includes barrel shrond, the cylinder Enclosure is arranged and forms the second helical runner of integrative-structure, the carbonization kiln barrel shrond two with the barrel shrond inwall End is respectively provided with front-seat smoke-box and heel row smoke-box, and the barrel shrond front and back end connects respectively the smoke discharging pipe of opening upwards, and two The individual smoke discharging pipe is connected with deodorizing system, and the outer hot fender is wound on around the barrel shrond of the carbonization kiln, by external Burner heat supply, the carbonization kiln reducing motor by chain-driving be carbonized kiln rotate.
Further improvement to above-mentioned technical proposal:The second spiral in the interior pusher spiral carbonization kiln barrel shrond Impeller is divided into three sections of displacements, is sequentially reduced to material end, the pitch of each section of the second helical runner is gone out from material end is entered, each section second The width of helical runner is sequentially reduced.
Further improvement to above-mentioned technical proposal:The material distributing system includes material distribution reducing motor, material Distributing auger conveyer, the reducing motor that feeds intake, the conveying worm that feeds intake, the second stirring motor, the material distributes reducing motor By material distributing auger conveyer described in chain-driving, the material distributing auger conveyer includes cylinder-like shell, described Fixed 3rd helical runner of cylinder-like shell inwall, the 3rd helical runner is from the hand of spiral of centre to two ends conversely, institute State material distributing auger conveyer charging aperture respectively with the feed system, the conveying worm that feeds intake to be connected, the material point The position being connected with the conveying worm that feeds intake with conveying worm is provided with the second stirring motor, and second stirring motor drives One shaft is rotated, and blade is provided with the shaft, and the blade enters the material that material distributing auger conveyer is unloaded Row stirring, prevents feed blocking from feeding intake helical feed machine inlet;The material distributing auger conveyer horizontally set, it is described enter The center of the charging aperture of material system is corresponding up and down with the center of the material distributing auger conveyer, the material point Charging aperture with conveying worm is connected with the charging aperture of the feed system, and the material distributing auger conveyer connects two The conveying worm that feeds intake, each conveying worm that feeds intake connects a carbonization kiln, the reducing motor chain band that feeds intake The dynamic conveying worm rotation that feeds intake.
Further improvement to above-mentioned technical proposal:The material collection system includes material collection reducing motor, material Gathering screw conveyer, the material collection conveying worm includes cylindrical housing, the cylindrical housing inwall fixed the Four helical runners, the material collection conveying worm horizontally set, described material collection conveying worm one end arranges one Circular unloader mouth, the material collection conveying worm kiln discharge port that is carbonized described with two is tightly connected;The discharge system Including discharging reducing motor, discharging spiral conveyor, cooling water tank, the charging aperture of the discharge system and the material collection system The circular unloader mouth of system is connected by flange, and the discharging spiral conveyor is obliquely installed, the charging aperture position of the discharge system In low side, there is shell side outside the discharging spiral conveyor, the cooling water tank connects the shell side by water pipe, discharge spiral Conveyer centre position is left and right symmetrically arranged two stands, and two stands are respectively provided with cant beam support, and wheel is installed in the bottom of two stands.
Further improvement to above-mentioned technical proposal:The deodorizing system includes deodorization stove, deodorization burner, exhaust Tower, deodorization cooling water tank, the deodorization furnace bottom arranges deodorization burner, there is cooling water shell side, institute outside the deodorization stove State deodorization cooling water tank and the cooling shell side is connected by water pipe.
The utility model has the advantage that compared with prior art and good effect:
1st, the utility model highly versatile, the material variety of process is more, except for processing rubber, plastics, greasy filth, bamboo charcoal etc. Raw material, can also be used to process the higher material of water content, such as:The biomass solid waste such as weeds, branch, marine alga;Paper pulp, food are residual The Industrial Solid Wastes such as slag;The solid refuse of moisture content≤85% such as changing food waste, house refuse.Relatively low, energy is required to material water ratio The solid organic matters of enough carbonizations are all suitable for the utility model.By the material of moisture content≤85%(The higher material of moisture content need through Processed is into the equipment)Crushed, it is desirable to which fragment or grain diameter are less than 30mm after broken(The size is bank Product sealing reaches the necessary condition of good result).Equipment is heated with external burner to the kiln that is carbonized, and material is pushed away in spiral Rotating speed adjustable material transporting velocity, the heating-up temperature of control carbonization kiln are heated by during entering, it is ensured that not of the same race Class, the material of different water cut can be carbonized completely.
2nd, flue gas processing device of the present utility model is that deodorization stove is connected with the gas pipeline of carbonization kiln front and back end.It was carbonized The volatile substances produced in journey are directly entered deodorization stove by pipeline, and deodorization burner is heated to this portion gas, Ensure that the flue gas in deodorization stove produced by gas combustion is in high-temperature section(≥ 800°C), gas residence time >=2s.Through The flue gas dioxin content of deodorization stove process can effectively be reduced to 0.085 ng/Nm3, meet discharging standards 0.1ng/Nm3, Really realize the requirement of environmental protection.
3rd, carbonizing apparatus need the air capacity in control device(Mainly oxygen content), because carbonizing plant is in high temperature shape State, and device is contained within flammable explosive gas, air content is higher to cause a hidden trouble to equipment safety operation.The utility model is from entering The discharging opening of the charging aperture of material system to discharge system forms the screw propulsion material channel being tightly connected, due to screw propulsion thing Material passage is completely embedded, and does not exist and air communication phenomenon, two outlets i.e. charging aperture and the discharging opening being connected with the external world.Equipment Sealed by the way of solid accumulation into and out of material mouth, effectively reduced the air content of device interior, improve equipment Security, while reducing equipment cost.
4th, traditional carbonizing apparatus are due to processing store list one(Special disposal bamboo charcoal or greasy filth), the material of generation is commonly used for Rubber black, barbecue charcoal, fuel etc..The characteristics of carbonized product that the utility model is produced has light weight, odorless, its purposes is wide It is general, can serve as agricultural fertilizer, horticultural soil improved materials, Snow Agent, bioxin sorbing material, deodorization material, water imbibition pottery Ceramic material etc..
5th, material Transfer pipe of the present utility model is all by the way of helical feed, and high degree of automation, operation is simple It is single, it is required artificial few, workman's cost can be reduced.
Description of the drawings
Fig. 1 is a kind of main body schematic diagram of screw-pushing type solid waste continuous carbonization equipment of the utility model;
Fig. 2 is the left view of Fig. 1;
Fig. 3 is the smoke evacuation room schematic diagram in a kind of screw-pushing type solid waste continuous carbonization equipment of the utility model;
Fig. 4 is the signal of the deodorization stove in a kind of screw-pushing type solid waste continuous carbonization equipment of the utility model Figure;
Fig. 5 is the signal of the carbonization kiln in a kind of screw-pushing type solid waste continuous carbonization equipment of the utility model Figure;
Fig. 6 is external burner installation position in a kind of screw-pushing type solid waste continuous carbonization equipment of the utility model Put schematic diagram;
Fig. 7 is the material collection spiral transferring in a kind of screw-pushing type solid waste continuous carbonization equipment of the utility model Send the schematic diagram of machine;
Fig. 8 is the discharging spiral conveyor in a kind of screw-pushing type solid waste continuous carbonization equipment of the utility model Schematic diagram;
Fig. 9 is the feeding spiral conveyer in a kind of screw-pushing type solid waste continuous carbonization equipment of the utility model Schematic diagram.
Specific embodiment
It is a kind of embodiment of screw-pushing type solid waste continuous carbonization equipment of the utility model referring to Fig. 1-Fig. 9, Including the feed system, material distributing system, carbonization system, product collection system and the discharge system that are sequentially connected, from it is described enter The discharging opening 32 of the charging aperture 5 of material system to the discharge system forms the screw propulsion material channel being tightly connected, the carbon Change system connects deodorizing system.
Specifically:As shown in Fig. 2, Fig. 9, above-mentioned feed system includes charging reducing motor 36, feeding spiral conveyer 38th, charging aperture 5, the first stirring motor 10, the charging aperture 5 of the feed system is back taper feed hopper, the first stirring electricity Machine 10 drives a shaft to rotate, and blade is provided with the shaft, and the shaft is located at the back taper of the feed system In shape feed hopper.
Carbonization system is core cell.Above-mentioned carbonization system includes carbonization kiln 7, outer hot stove 8, outer hot burner 15, combustion Burning blower fan, temperature adjustment blower fan, carbonization kiln reducing motor 18, front-seat smoke-box 6, heel row smoke-box 11, the carbonization kiln 7 includes Two parallel interior pusher spiral carbonization kilns, interior pusher spiral carbonization kiln includes barrel shrond, inside the barrel shrond The second helical runner 25 that integrative-structure is formed with the barrel shrond inwall, the carbonization kiln 7 barrel shrond two ends point are set Not She Zhi front-seat smoke-box 6 and heel row smoke-box 11, the water vapour produced in heating process for discharges material and other volatility Gas, these gases are transported to the deodorization stove 22 of deodorizing system and carry out second-time burning, it is to avoid the harmful substance pollution in gas Environment.Barrel shrond front and back end connects respectively smoke discharging pipe, and two smoke discharging pipes are connected with deodorizing system.The outer hot stove 8 are centered around around the barrel shrond of the carbonization kiln 7, by the external heat supply of outer hot burner 15.Carbonization kiln 7 is built with temperature Detector, so as to control the opening and closing of outer hot burner 15, can control furnace temperature with real-time monitoring kiln temperature.Described feeding intake subtracts Speed motor 1 is rotated with the conveying worm 2 that feeds intake described in chain-driving, and the carbonization kiln reducing motor 18 is carbonized by chain-driving Kiln 7.Material is heated by regulation carbonization kiln 18 rotating speeds of reducing motor during advancing in carbonization kiln 7 right so as to realize The control of material time of staying in carbonization kiln 7, it is ensured that different material can be carbonized completely.
Volume reduces during material enters before heating, and material is extruded propulsion during advance, according to this feelings Condition, 25 points of the second helical runner in above-mentioned interior pusher spiral carbonization kiln barrel shrond is three sections of displacements, from enter material end to Go out material end, the pitch of each section of the second helical runner 25 is sequentially reduced, and the width of each section of the second helical runner 25 is sequentially reduced.This Structure is conducive to axial direction of the material in carbonization kiln 7 to wriggle, it is to avoid accumulation of the material in carbonization kiln 7.
Above-mentioned material distributing system includes material distributing auger conveyer 3, material distribution reducing motor 4, feed intake deceleration electricity Machine 1, the conveying worm 2 that feeds intake, the second stirring motor 19, the material distribution reducing motor 4 passes through material described in chain-driving Distributing auger conveyer 3, the material distributing auger conveyer 3 includes cylinder-like shell, and the cylinder-like shell inwall is fixed 3rd helical runner, the 3rd helical runner is from the hand of spiral of centre to two ends conversely, material distributing auger conveying The charging aperture 5 respectively with the feed system of machine 3, the conveying worm 2 that feeds intake are connected, the material distributing auger conveyer 3 with The connected position of the conveying worm 2 that feeds intake is provided with the second stirring motor 19, and the material distributing auger conveyer 3 laterally sets Put, the center of the charging aperture 5 of the feed system is right up and down with the center of the material distributing auger conveyer 3 Should, the charging aperture of material distributing auger conveyer 3 is connected with the charging aperture 5 of the feed system, and the material distributes spiral shell Rotation conveyer 3 two ends are distributed two discharge ports, and each discharge port corresponds to respectively the conveying worm 2 that feeds intake, each helical feed that feeds intake Machine 2 has a dog-house.The material entered by feed system charging aperture 5, after material distributing auger conveyer 3 is conveyed, Material is divided equally to two carbonization kilns 7.During helical feed, by the installation direction for adjusting the 3rd helical runner, thing is realized Material it is bi-directionally transmitted, and then material carried out to two carbonization kilns 7 divide equally.
Dried material is in the case where the reductor 1 that feeds intake drives using the mode of movement continuous feed of screw propulsion.Spiral transferring The sealing method of shipment for sending, can prevent the dust pollution of dried material.Charging aperture 5 is by the way of solid accumulation to the kiln that is carbonized Helical conveyer system is sealed, with the low-oxygen environment for keeping being carbonized in kiln 7, it is ensured that production safety is carried out.Feed auger support 39 foldable for storage, save operating space.
Above-mentioned material collection system includes material collection reducing motor 27, material collection conveying worm 28, the material Gathering screw conveyer 28 includes cylindrical housing, and fixed 4th helical runner of the cylindrical housing inwall, the material is received Collection conveying worm horizontally set, described one end of material collection conveying worm 28 arranges a circular unloader mouth, the material Gathering screw conveyer 28 passes through to be tightly connected with the discharge port of corresponding carbonization kiln 7.Product in two carbonization kilns 7, through material Gathering screw conveyer 28 is collected, and is finally transported to discharge port.
The discharge system includes discharging opening 32, discharging reducing motor 31, discharging spiral conveyor 30, cooling water tank, institute The charging aperture 29 for stating discharge system is connected with the circular unloader mouth of the material collection system by flange, the discharging spiral transferring Machine 30 is sent to be obliquely installed, the charging aperture 29 of the discharge system is located at low side, has shell side outside the discharging spiral conveyor 30, The cooling water tank connects the shell side by water pipe, and the product of carbonization, still in the condition of high temperature, leads to after the kiln 7 that is carbonized Supercooled water is lowered the temperature to high temperature cabonization product, prevents the scald that high temperature discharge is caused.The interposition of discharging spiral conveyor 30 Put and be left and right symmetrically arranged two stands 35, two stands are respectively provided with cant beam 33 and support, wheel 34 is installed in the bottom of two stands, be easy to move It is dynamic.The support foldable for storage of discharging spiral conveyor, saves operating space.
Above-mentioned deodorizing system includes deodorization stove 22, deodorization burner, exhaust tower 9, deodorization cooling water tank 20, the deodorization The bottom of stove 22 arranges deodorization burner, there is cooling water shell side outside the deodorization stove 22, and the deodorization cooling water tank 20 passes through Water pipe connects the cooling shell side.The gas that material is produced in heating process carries out second-time burning in deodorization stove 22, burns During need the flue gas controlled in deodorization stove 22 produced by gas combustion to be in high-temperature section(≥ 800°C), and ensure gas The time of staying >=2s of the body in deodorization stove 22.Above-mentioned condition can ensure that a small amount of bioxin in carbonization gas decomposes complete.Examination Test result to show, 0.085 ng/Nm is less than by content of dioxin in cracking gas after deodorization stove 223, meet country's discharge mark 0.1 ng/Nm of standard3
A kind of continuously carbonating method of above-mentioned screw-pushing type solid waste continuous carbonization equipment of the utility model, including Following steps:
(1)Material after crushing(The material of moisture content≤85%, it is desirable to which fragment or grain diameter are less than 30mm after broken) Or feed system charging aperture is delivered to by feed system through dry material;
(2)Into feed system charging aperture material through material distributing system be divided equally to two it is flat
In capable carbonization kiln;
(3)Outer hot stove is heated to the kiln that is carbonized, and is controlled heating-up temperature, is passed through by controlling the opening and closing of external burner Control is carbonized kiln rotating speed to control the different material thermal response time;
(4)Material collection system is collected the carbonized product in two carbide furnaces, is finally transported to discharge system;
(5)Material is transported to carbide storage warehouse by the discharge system with cooling water tank, simultaneously to thing during transport Material is lowered the temperature;
(6)The escaping gas that material is produced in heating process is transported to deodorant stove by smoke discharging pipe, after carry out height Temperature heating, reduces Qi body Zhong content of dioxin so as to reach the discharge standard of national regulation, it is to avoid produce in carbonisation secondary Pollution.
Above-mentioned steps(6)In, need to control the cigarette in deodorization stove produced by gas combustion in escaping gas combustion process Gas is in high-temperature section(≥ 800°C), and ensure the time of staying >=2s of the gas in deodorization stove.
Certainly, described above is not that, to restriction of the present utility model, the utility model is also not limited to the example above, this The those of ordinary skill of technical field, in essential scope of the present utility model, done change, remodeling, addition or replaces, Also protection domain of the present utility model should be belonged to.

Claims (9)

1. a kind of screw-pushing type solid waste continuous carbonization equipment, it is characterised in that including the feed system being sequentially connected, Material distributing system, carbonization system, product collection system and discharge system, the charging aperture from the feed system is to the discharging The discharging opening of system forms the screw propulsion material channel being tightly connected, and the carbonization system connects deodorizing system.
2. according to the screw-pushing type solid waste continuous carbonization equipment described in claim 1, it is characterised in that the charging System includes feeding spiral conveyer, charging reducing motor, the first stirring motor, the charging aperture, and the feed system enters Material mouth is back taper feed hopper, and described feeding spiral conveyer includes cylindrical housing, and the cylindrical housing inwall is fixed First helical runner, first stirring motor drives a shaft to rotate, and blade, the stirring are provided with the shaft Axle position prevents feed blocking charging aperture in the back taper feed hopper bottom of the feed system.
3. according to the screw-pushing type solid waste continuous carbonization equipment described in claim 2, it is characterised in that the carbonization System includes carbonization kiln, outer hot stove, outer hot burner, front-seat smoke-box, heel row smoke-box, burning blower fan, temperature adjustment wind Machine, carbonization kiln reducing motor, the carbonization kiln includes two parallel interior pusher spiral carbonization kilns, interior pusher spiral carbonization Kiln includes barrel shrond, and the barrel shrond inside arranges the second helical-blade that integrative-structure is formed with the barrel shrond inwall Wheel, the carbonization kiln barrel shrond two ends are respectively provided with front-seat smoke-box and heel row smoke-box, and the barrel shrond front and back end connects respectively The smoke discharging pipe of open horizontal is connect, two smoke discharging pipes are connected with deodorizing system, the outer hot fender is wound on the carbonization Around the barrel shrond of kiln, by outer hot burner heat supply, the carbonization kiln reducing motor is rotated by chain-driving carbonization kiln.
4. according to the screw-pushing type solid waste continuous carbonization equipment described in claim 3, it is characterised in that push away in described The second helical runner entered in formula spiral carbonization kiln barrel shrond is divided into three sections of displacements, from entering material end to going out material end, each section The pitch of the second helical runner is sequentially reduced, and the width of each section of the second helical runner is sequentially reduced.
5. according to the screw-pushing type solid waste continuous carbonization equipment described in claim 3 or 4, it is characterised in that described Material distributing system includes material distribution reducing motor, material distributing auger conveyer, the reducing motor that feeds intake, feed intake helical feed Machine, the second stirring motor, the material distribution reducing motor is by material distributing auger conveyer described in chain-driving, the thing Material distributing auger conveyer includes cylinder-like shell, fixed 3rd helical runner of the cylinder-like shell inwall, the 3rd spiral shell Propeller runner is from the hand of spiral of centre to two ends conversely, the material distributing auger conveyer enters respectively with the feed system Material mouth, the conveying worm that feeds intake are connected, and the position that the material distributing auger conveyer is connected with the conveying worm that feeds intake is installed There is the second stirring motor, second stirring motor drives a shaft to rotate, blade, the leaf are provided with the shaft Piece is stirred the material that material distributing auger conveyer is unloaded, and prevents feed blocking from feeding intake helical feed machine inlet;Institute State material distributing auger conveyer horizontally set, the center of the charging aperture of the feed system and the material distributing auger The center of conveyer corresponds to up and down, the charging aperture of the material distributing auger conveyer and the charging aperture of the feed system It is connected, the material distributing auger conveyer connects the conveying worm that feeds intake described in two, each conveying worm connection that feeds intake One carbonization kiln, the conveying worm that feed intake described in reducing motor chain-driving that feeds intake.
6. according to the screw-pushing type solid waste continuous carbonization equipment described in claim 3 or 4, it is characterised in that described Material collection system includes material collection reducing motor, material collection conveying worm, the material collection conveying worm bag Include cylindrical housing, fixed 4th helical runner of the cylindrical housing inwall, the material collection conveying worm laterally sets Put, described material collection conveying worm one end arranges a circular unloader mouth, the material collection conveying worm and two The discharge port of the carbonization kiln is tightly connected;The discharge system includes discharging reducing motor, discharging spiral conveyor, cooling water Case, the charging aperture of the discharge system is connected with the circular unloader mouth of the material collection system by flange, the discharging spiral shell Rotation conveyer is obliquely installed, and the charging aperture of the discharge system is located at low side, there is shell side, institute outside the discharging spiral conveyor State cooling water tank and the shell side is connected by water pipe, discharging spiral conveyor centre position is left and right symmetrically arranged two stands, two Frame is respectively provided with cant beam support, and wheel is installed in the bottom of two stands.
7. according to the screw-pushing type solid waste continuous carbonization equipment described in claim 5, it is characterised in that the material Collection system includes material collection reducing motor, material collection conveying worm, and the material collection conveying worm includes circle Cylindrical outer casing, fixed 4th helical runner of the cylindrical housing inwall, the material collection conveying worm horizontally set, institute State material collection conveying worm one end and one circular unloader mouth, the material collection conveying worm and two carbon are set The discharge port for changing kiln is tightly connected;The discharge system includes discharging reducing motor, discharging spiral conveyor, cooling water tank, institute The charging aperture for stating discharge system is connected with the circular unloader mouth of the material collection system by flange, the discharging helical feed Machine is obliquely installed, and the charging aperture of the discharge system is located at low side, there is shell side, the cooling outside the discharging spiral conveyor Water tank connects the shell side by water pipe, and discharging spiral conveyor centre position is left and right symmetrically arranged two stands, two stands difference Arrange cant beam to support, wheel is installed in the bottom of two stands.
8. according to the screw-pushing type solid waste continuous carbonization equipment described in any one of claim 1-4, it is characterised in that The deodorizing system includes deodorization stove, deodorization burner, exhaust tower, deodorization cooling water tank, and the deodorization furnace bottom arranges de- Smelly burner, there is cooling water shell side outside the deodorization stove, the deodorization cooling water tank connects the cooling shell by water pipe Journey.
9. according to the screw-pushing type solid waste continuous carbonization equipment described in claim 7, it is characterised in that the deodorization System includes deodorization stove, deodorization burner, exhaust tower, deodorization cooling water tank, and the deodorization furnace bottom arranges deodorization stove burning Device, there is cooling water shell side outside the deodorization stove, the deodorization cooling water tank connects the cooling shell side by water pipe.
CN201620652117.2U 2016-06-28 2016-06-28 Spiral propulsive type solid waste continuous carbonization equipment Expired - Fee Related CN206094094U (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105927983A (en) * 2016-06-28 2016-09-07 成和环保科技股份有限公司 Screw propelling type solid waste continuous carbonization equipment and continuous carbonization method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105927983A (en) * 2016-06-28 2016-09-07 成和环保科技股份有限公司 Screw propelling type solid waste continuous carbonization equipment and continuous carbonization method

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