CN108018056A - A kind of house refuse large-size horizontal destructive distillation device - Google Patents
A kind of house refuse large-size horizontal destructive distillation device Download PDFInfo
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- CN108018056A CN108018056A CN201711322437.7A CN201711322437A CN108018056A CN 108018056 A CN108018056 A CN 108018056A CN 201711322437 A CN201711322437 A CN 201711322437A CN 108018056 A CN108018056 A CN 108018056A
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Classifications
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B43/00—Preventing or removing incrustations
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B47/00—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion
- C10B47/18—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion with moving charge
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B47/00—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion
- C10B47/28—Other processes
- C10B47/32—Other processes in ovens with mechanical conveying means
- C10B47/44—Other processes in ovens with mechanical conveying means with conveyor-screws
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
Abstract
The invention discloses a kind of house refuse large-size horizontal destructive distillation device, including：Vacuumize feed mechanism, spiral retorting machine, heating arrangements, gas cooling separating mechanism and vacuum Chu Tan mechanisms；The material output terminal for vacuumizing feed mechanism is connected with the material input of spiral retorting machine；The gas output end of spiral retorting machine is connected with the gas input of gas cooling separating mechanism, the carbon outlet of spiral retorting machine and being connected into carbon mouth for vacuum Chu Tan mechanisms；Heating arrangements carry out the material in spiral retorting machine isolation air heating, the macromolecular chain segment of composition organic matter is set to occur to be broken and change into the energy substance of recycling gas-liquid-solid under certain pressure, temperature, time conditions, it not only avoid the use to conventional garbage treatment technology, solve that of high cost, time-consuming, environmental pollution and the technical problem taken up a large area, and realize energy substance circulation and regeneration.The present invention is applied to the processing of the rubbish such as house refuse, stalk, medical waste, sludge.
Description
Technical field
The present invention relates to technical field of energy saving and environmental protection, more particularly to a kind of house refuse large-size horizontal destructive distillation device.
Background technology
The biomass being scattered in domestic waste is distributed widely in human lives, existing to be scattered in urban life
Biomass processes technology in rubbish mainly has composting technology, incineration technology and Landfill.
Biomass is handled using composting technology, the deodorization improvement of compost is expensive, and the time needs one month, and
Tend to cause the exceeded of heavy metal.
And incineration technology processing biomass is used, it will cause environmental pollution.At present, for incineration technology bioxin
Pollution problem, debates endlessly, the cry and event for multiple people's opposition also occur and establishing incineration plant domestic in recent years.
And use Landfill processing biomass, then it can take substantial amounts of soil and make its hard to carry on, but also have
The puzzlement of foul smell and sewage.
Therefore, for a variety of drawbacks present in existing technology of garbage disposal, it is necessary to propose a kind of new rubbish destructive distillation
Treatment technology.
The content of the invention
The present invention solves of high cost, consumption in the prior art by providing a kind of house refuse large-size horizontal destructive distillation device
Duration, environmental pollution and the technical problem taken up a large area.
The present invention provides a kind of house refuse large-size horizontal destructive distillation device, including：Vacuumize feed mechanism, spiral destructive distillation
Machine, heating arrangements, gas cooling separating mechanism and vacuum Chu Tan mechanisms；The material output terminal for vacuumizing feed mechanism and institute
State the material input connection of spiral retorting machine；The gas output end of the spiral retorting machine and the gas cooling separating mechanism
Gas input connection, the carbon outlet of the spiral retorting machine connects with the vacuum Chu Tan mechanisms into carbon mouth；It is described to add
Heat engine structure carries out the material in the spiral retorting machine isolation air heating；The isolation air mode of heating is interior heating side
Formula and/or external heating mode.
Further, the feed mechanism that vacuumizes includes：Material bin, the first valve, storage bin hopper, the second valve, first
Screw conveyor, the second screw conveyor, the 3rd valve, vaccum-pumping equipment；The discharge port of the material bin and the storage bin hopper
Feed inlet connection；First valve is arranged between the material bin and the storage bin hopper；Second valve is arranged on
The discharge port of the storage bin hopper；First screw conveyor is arranged in the storage bin hopper, by material from the storage bin hopper
Discharge port exports；The feed inlet of second screw conveyor is connected with the discharge port of the storage bin hopper, second spiral transferring
The discharge port of machine is sent to be connected with the material input of the spiral retorting machine；The vaccum-pumping equipment is connected with the storage bin hopper；
3rd valve is arranged between the vaccum-pumping equipment and the storage bin hopper；The storage bin hopper is vertical storage bin hopper or horizontal
Storage bin hopper.
Further, the spiral retorting machine includes：Engine base, hollow chassis, screw rod and motive power outputting apparatus；In described
Empty rack is arranged on the engine base；The screw rod is arranged in the hollow chassis；The power intake of the screw rod
It is connected with the power output end of the motive power outputting apparatus；The material input of the hollow chassis vacuumizes feeder with described
The material output terminal connection of structure, the gas input of the gas output end of the hollow chassis and the gas cooling separating mechanism
Connection, the carbon outlet of the hollow chassis are connected with the vacuum Chu Tan mechanisms into carbon mouth.
Further, the hollow chassis includes：Hollow, the first thermal insulation board and the second thermal insulation board；Described first is heat-insulated
Plate and second thermal insulation board are separately positioned in the both ends of the hollow；The screw rod is arranged in the hollow；
There are material input, gas output end and carbon outlet in the hollow.
Further, the screw rod includes：The body of rod, forward flight, reverse flight and shaft；The shaft and institute
State body of rod connection；The both ends of the shaft are connected with first thermal insulation board, second thermal insulation board respectively；The shaft and institute
State the power output end connection of motive power outputting apparatus；The forward flight and the reverse flight are arranged at the body of rod
On；The reverse flight is located at the top of the carbon outlet of the hollow；When using the interior mode of heating or described additional
During hot mode, the spacing of outer wall to the inner wall of the hollow of the body of rod is 50-300mm；When using the interior heating side
When formula and the external heating mode, the spacing of outer wall to the inner wall of the hollow of the body of rod is 100-600mm；Described
One is formed between the outer wall of the body of rod, the inner wall of the hollow, first thermal insulation board and second thermal insulation board can ensure that
Pyrolysate is by the large capacity space of abundant destructive distillation.
Further, the motive power outputting apparatus includes：Motor, vertical drive shaft, reverse drive gear and vertical solution
Seal apparatus；The power output end of the motor is connected with the first end of the vertical drive shaft；The of the vertical drive shaft
Two ends are connected with the first end of the reverse drive gear；The second end of the reverse drive gear is connected with the shaft；Institute
Vertical liquid seal device is stated to be connected with the vertical drive shaft, the hollow.
Further, the gas cooling separating mechanism includes：Cleaner, desulphurization plant, cooling device, multistage decoking
Equipment, oily water separating equipment and gas storage equipment；The gas input of the cleaner and the gas of the spiral retorting machine are defeated
Outlet connects, and the gas output end of the cleaner is connected with the gas input of the desulphurization plant；The desulphurization plant
Gas output end connected with the gas input of the cooling device；The gas output end of the cooling device and the multistage
The gas input connection of decoking equipment, the liquid material output terminal of the cooling device and the material of the oily water separating equipment
Input terminal connects；The gas material of the cooling device is passed through the gas storage equipment storage through the multistage decoking equipment except defocused
Deposit.
Further, the cooling device is multistage cooling device cascaded structure.
Further, the vacuum Chu Tan mechanisms include：It is spiral go out carbon machine, heat exchange cooling tube, it is spiral send carbon machine, storage carbon
Equipment, material inlet valve, electrically-controlled valve, discharge valve and vacuum extractor；It is described it is spiral go out carbon machine be arranged on heat exchange cooling
Guan Zhong；The heat exchange cooling tube is connected into carbon mouth with the carbon outlet of the spiral retorting machine, the heat exchange cooling tube
Carbon outlet spiral send being connected into carbon mouth for carbon machine with described；The spiral carbon outlet for sending carbon machine and the storage carbon equipment are into carbon
Mouth connection；The material inlet valve is arranged on the feed inlet of the storage carbon equipment；The discharge valve is arranged on the storage carbon equipment
Discharge port；The vacuum extractor is passed through the storage carbon equipment；The electrically-controlled valve be arranged on the vacuum extractor with it is described
Between storage carbon equipment.
Further, the heating arrangements are electric heating mechanism, charcoal heating arrangements and/or gas heater structure.
The one or more technical solutions provided in the present invention, have at least the following technical effects or advantages：
Isolation air is carried out to organic matter by heating arrangements to heat, makes the macromolecular chain segment of composition organic matter in a level pressure
Fracture occurs under the conditions of power, temperature, time etc. and changes into recycling gas (fuel gas), liquid (cracked oil), solid (carbon)
The primary energy material of tri-state, trickle into forest, biomass and animal Non-oxygen pyrolytic just as the lava that volcano eruption produces and
Tellurian coal, oil, natural gas are formed, not only avoid the use to conventional garbage treatment technology, is efficiently solved existing
It is of high cost in technology, time-consuming, environmental pollution and the technical problem taken up a large area, and realize energy substance circulation with again
Make profits use, greatly reduce destruction of the mankind's activity to environment and air, can effectively change and be produced at present with cereal crops
The short present situation of world food caused by the energy.
Brief description of the drawings
Fig. 1 is the structure diagram of house refuse large-size horizontal destructive distillation device provided in an embodiment of the present invention；
Fig. 2 is the knot that feed mechanism 1 is vacuumized in house refuse large-size horizontal destructive distillation device provided in an embodiment of the present invention
Structure schematic diagram；
Fig. 3 is that the structure of spiral retorting machine 2 in house refuse large-size horizontal destructive distillation device provided in an embodiment of the present invention is shown
It is intended to；
Fig. 4 is gas cooling separating mechanism 4 in house refuse large-size horizontal destructive distillation device provided in an embodiment of the present invention
Structure diagram；
Fig. 5 is the structure of vacuum Chu Tan mechanisms 5 in house refuse large-size horizontal destructive distillation device provided in an embodiment of the present invention
Schematic diagram；
Wherein, 1- vacuumizes feed mechanism, the spiral retorting machines of 2-, 3- heating arrangements, 4- gas cooling separating mechanisms, and 5- is true
Vacate carbon mechanism, 6- material bins, the first valves of 7-, 8- storage bin hoppers, the second valves of 9-, the first screw conveyors of 10-, 11- second
Screw conveyor, the 3rd valves of 12-, 13- vaccum-pumping equipments, 14- engine bases, 15- hollows, the first thermal insulation boards of 16-, 17- second
Thermal insulation board, 18- flanges, the first closed boring covers of 19-, the second closed boring covers of 20-, the 21- bodies of rod, forward flight, 23- are reverse by 22-
Flight, 24- shafts, 25- motor, 26- vertical drive shafts, 27- reverse drive gears, 28- cleaners, 29- desulfurization are set
It is standby, 30- cooling devices, 31- multistage decoking equipments, 32- oily water separating equipments, 33- gas storage equipments, 34- it is spiral go out carbon machine, 35-
Heat exchange cooling tube, 36- is spiral to send carbon machine, upper storage carbon pipe tanks of the 37- containing sealing device, lower storage carbon pipes of the 38- containing sealing device
Tank, the vertical liquid seal devices of 39-.
Embodiment
The embodiment of the present invention solves cost in the prior art by providing a kind of house refuse large-size horizontal destructive distillation device
It is high, time-consuming, environmental pollution and the technical problem taken up a large area.
Technical solution in the embodiment of the present invention is to solve the above problems, general thought is as follows：
Isolation air is carried out to organic matter by heating arrangements to heat, makes the macromolecular chain segment of composition organic matter in a level pressure
Fracture occurs under the conditions of power, temperature, time etc. and changes into recycling gas (fuel gas), liquid (cracked oil), solid (carbon)
The primary energy material of tri-state, trickle into forest, biomass and animal Non-oxygen pyrolytic just as the lava that volcano eruption produces and
Tellurian coal, oil, natural gas are formed, not only avoid the use to conventional garbage treatment technology, is efficiently solved existing
It is of high cost in technology, time-consuming, environmental pollution and the technical problem taken up a large area, and realize energy substance circulation with again
Make profits use, greatly reduce destruction of the mankind's activity to environment and air, can effectively change and be produced at present with cereal crops
The short present situation of world food caused by the energy.
Above-mentioned technical proposal in order to better understand, in conjunction with appended figures and specific embodiments to upper
Technical solution is stated to be described in detail.
Referring to Fig. 1, house refuse large-size horizontal destructive distillation device provided in an embodiment of the present invention, including：Vacuumize feeder
Structure 1, spiral retorting machine 2, heating arrangements 3, gas cooling separating mechanism 4 and vacuum Chu Tan mechanisms 5；Vacuumize feed mechanism 1
Material output terminal is connected with the material input of spiral retorting machine 2；The gas output end of spiral retorting machine 2 is separated with gas cooling
The gas input connection of mechanism 4, the carbon outlet of spiral retorting machine 2 and being connected into carbon mouth for vacuum Chu Tan mechanisms 5；Heating arrangements
Material in 3 pairs of spiral retorting machines 2 carries out isolation air heating.
Referring to Fig. 2, the structure for vacuumizing feed mechanism 1 is illustrated, vacuumizing feed mechanism 1 includes：Material bin 6,
First valve 7, storage bin hopper 8, the second valve 9, the first screw conveyor 10, the second screw conveyor 11, the 3rd valve 12, pumping are true
Null device 13；The discharge port of material bin 6 is connected with the feed inlet of storage bin hopper 8；First valve 7 is arranged on material bin 6 and storage bin hopper 8
Between；Second valve 9 is arranged on the discharge port of storage bin hopper 8；First screw conveyor 10 is arranged in storage bin hopper 8, by material from
The discharge port output of storage bin hopper 8；The feed inlet of second screw conveyor 11 is connected with the discharge port of storage bin hopper 8, the second spiral transferring
The discharge port of machine 11 is sent to be connected with the material input of spiral retorting machine 2；Vaccum-pumping equipment 13 is connected with storage bin hopper 8；3rd valve
Door 12 is arranged between vaccum-pumping equipment 13 and storage bin hopper 8；Storage bin hopper 8 is vertical storage bin hopper or horizontal storage bin hopper.
Before house refuse is added into storage bin hopper 8, first the first valve 7 is opened, the second valve 9 is closed, then will life
Rubbish is added in storage bin hopper 8.The first valve 7 is then shut off, starts the 3rd valve 12 and vaccum-pumping equipment 13 so that storage bin hopper 8
It is interior to be in vacuum state, turn off the 3rd valve 12 and vaccum-pumping equipment 13.Then the second valve 9 is opened, house refuse is
The second screw conveyor 11 is reached under the action of one screw conveyor 10.Before house refuse is added again into storage bin hopper 8,
First the second valve 9 is closed, starts the 3rd valve 12 and vaccum-pumping equipment 13 so that is in vacuum state in storage bin hopper 8.Then
The first valve 7 is opened again, house refuse is added in storage bin hopper 8.The first valve 7 is then shut off, starts 12 He of the 3rd valve
Vaccum-pumping equipment 13 so that be in vacuum state in storage bin hopper 8.Then the 3rd valve 12 and vaccum-pumping equipment 13 are turned off, and
The second valve 9 is opened, house refuse reaches the second screw conveyor 11 under the action of the first screw conveyor 10.Here need
It is noted that the embodiment of the present invention can include more set storage bin hopper cutting agencies, the structure of each storage bin hopper cutting agency is identical.
There are multiple feed inlets on second screw conveyor 11.The discharge port of storage bin hopper in each storage bin hopper cutting agency correspondingly with
Each feed inlet connection on second screw conveyor 11, is used, and then ensure that not interrupting for destructive distillation operation so as to fulfill mutual wheel
Carry out.
In the present embodiment, the first valve 7 and the second valve 9 are electrically-controlled valve；3rd valve 12 is check valve；Vacuumize
Equipment 13 is vacuum pump.
Referring to Fig. 3, the structure of spiral retorting machine 2 is illustrated, spiral retorting machine 2 includes：Engine base 14, hollow chassis,
Screw rod and motive power outputting apparatus；Hollow chassis is arranged on engine base 14；Screw rod is arranged in hollow chassis；Screw rod moves
The power output end of power input terminal and motive power outputting apparatus connects；The material input of hollow chassis is with vacuumizing feed mechanism 1
Material output terminal connection, the gas output end of hollow chassis is connected with the gas input of gas cooling separating mechanism 4, hollow
The carbon outlet of rack is connected with vacuum Chu Tan mechanisms 5 into carbon mouth.
In the present embodiment, engine base 14 is that several piece bottom surface is rectangle, and top surface is arc-shaped, and bottom surface and top surface are arc-shaped most
Lower has the slab of proper height.
The structure of hollow chassis in spiral retorting machine 2 is illustrated, hollow chassis includes：Hollow 15, first every
16 and second thermal insulation board 17 of hot plate；First thermal insulation board 16 and the second thermal insulation board 17 are separately positioned in the both ends of hollow 15；Spiral shell
Swing arm is arranged in hollow 15；There are material input, gas output end and carbon outlet in hollow 15.
Specifically, flange 18 is equipped with the both ends of the inner wall of hollow 15；First thermal insulation board 16 and the second thermal insulation board 17
It is separately fixed on the flange 18 in 15 both ends of hollow.The first closed boring cover 19 is respectively arranged with the outside of 15 both ends of hollow
With the second closed boring cover 20.
The structure of screw rod in spiral retorting machine 2 is illustrated, screw rod includes：The body of rod 21, forward flight 22,
Reverse flight 23 and shaft 24；Shaft 24 is connected with the body of rod 21；The both ends of shaft 24 respectively with the first thermal insulation board 16, second every
Hot plate 17 connects；Shaft 24 is connected with the power output end of motive power outputting apparatus；Forward flight 22 and reverse flight 23 are equal
It is arranged on the body of rod 21；Reverse flight 23 is located at the top of the carbon outlet of hollow 15.Completely cut off air mode of heating to be interior to add
Hot mode and/or external heating mode；When using interior mode of heating or external heating mode, the outer wall of the body of rod 21 to hollow 15
The spacing of inner wall be 50-300mm；When using interior mode of heating and external heating mode, the outer wall of the body of rod 21 to hollow 15
The spacing of inner wall be 100-600mm；The inner wall of outer wall, hollow 15 in the body of rod 21, the first thermal insulation board 16 and second are heat-insulated
Forming one between plate 17 can ensure that pyrolysate by the large capacity space of abundant destructive distillation.
Specifically, the Bearning mechanism at the both ends of shaft 24 is separately positioned in the first thermal insulation board 16 and the second thermal insulation board 17
Between axis hole under rack platform on.Sealing mechanism is separately positioned in 24 and first thermal insulation board 16 of shaft and the second thermal insulation board 17
Between axis hole between.
The structure of motive power outputting apparatus in spiral retorting machine 2 is illustrated, motive power outputting apparatus includes：Motor
25th, vertical drive shaft 26 and reverse drive gear 27 and vertical liquid seal device 39；The power output end of motor 25 and vertical biography
The first end connection of moving axis 26；The second end of vertical drive shaft 26 is connected with the first end of reverse drive gear 27；Commutation transmission
The second end of device 27 is connected with shaft 24.Vertical liquid seal device 39 is connected with vertical drive shaft 26, hollow 15.
The structure of vertical liquid seal device 39 in motive power outputting apparatus is illustrated, vertical liquid seal device 39 includes upper
Multi-turn circular groove structure and lower multi-turn circular groove structure；Lower multi-turn circular groove structure is installed in hollow 15；Upper multi-turn circular groove structure peace
In lower multi-turn circular groove structure；There is sealing fluid in upper multi-turn circular groove structure and lower multi-turn circular groove structure.
In the present embodiment, motor 25 is vertical machine.
Referring to Fig. 4, the structure of gas cooling separating mechanism 4 is illustrated, gas cooling separating mechanism 4 includes：Dedusting
Equipment 28, desulphurization plant 29, cooling device 30, multistage decoking equipment 31, oily water separating equipment 32 and gas storage equipment 33；Dedusting is set
Standby 28 gas input is connected with the gas output end of spiral retorting machine 2, and gas output end and the desulfurization of cleaner 28 are set
Standby 29 gas input connects；The gas output end of desulphurization plant 29 is connected with the gas input of cooling device 30；Cooling
The gas output end of equipment 30 is connected with the gas input of multistage decoking equipment 31, the liquid material output terminal of cooling device 30
Connected with the material input of oily water separating equipment 32；The gas material of cooling device 30 is through multistage decoking equipment 31 except defocused
Gas storage equipment 33 is passed through to store.
In the present embodiment, other gases such as high-temperature steam, oil gas, combustible gas and carbon dioxide by cleaner 28 into
Row dust removal process, the gas after dedusting enter desulphurization plant 29 and carry out desulfurization process, and the gas after desulfurization enters cooling device 30.
High-temperature gas is cooled to 50 DEG C or so by cooling device 30, most water and tar is had in the process and is analysed through cooling
Go out, through being pumped into oily water separating equipment 32.Heavy oil can be deposited on the bottom of oily water separating equipment 32, and wood vinegar emerges in heavy oil
Top.Multistage decoking equipment 31 is entered by 30 gas after cooling of cooling device, by remaining dust, tar, moisture content in gas
Handled Deng impurity.Specifically, safety valve is housed at the top of multistage decoking equipment 31, bottom is equipped with selfdraining valve.Peace
Full valve can be automatically opened up when the pressure of multistage decoking equipment 31 exceedes preset value, and be discharged into escape way.Selfdraining valve energy
The impurity such as the moisture content in gas, tar are discharged into oily water separating equipment 32 automatically, purified gas is passed through gas storage equipment 33
Stored.Preferably, multistage decoking equipment 31 has two, is arranged in parallel, and is used alternatingly, and further ensures destructive distillation operation
Do not interrupt progress.
In the present embodiment, cleaner 28 is cyclone dust collectors；Desulphurization plant 29 is desulfurizing tower；Cooling device 30 is cold
But tank, and be multistage cooling device cascaded structure；Multistage decoking equipment 31 adsorbs decoking device for high-effective dust-removing；Gas storage equipment 33 is
Air accumulator.
Referring to Fig. 5, the structure of vacuum Chu Tan mechanisms 5 is illustrated, vacuum Chu Tan mechanisms 5 include：It is spiral go out carbon machine 34,
Heat exchange cooling tube 35, spiral send carbon machine 36, storage carbon equipment, material inlet valve, electrically-controlled valve, discharge valve and vacuum extractor；Spiral shell
Carbon machine 34 is screwed out to be arranged in heat exchange cooling tube 35；The carbon outlet into carbon mouth and spiral retorting machine 2 of heat exchange cooling tube 35
Connection, the carbon outlet of heat exchange cooling tube 35 send being connected into carbon mouth for carbon machine 36 with spiral；The spiral carbon outlet for sending carbon machine 36 with
Store up being connected into carbon mouth for carbon equipment；Material inlet valve is arranged on the feed inlet of storage carbon equipment；Discharge valve is arranged on storage carbon equipment
Discharge port；Vacuum extractor is passed through storage carbon equipment；Electrically-controlled valve is arranged between vacuum extractor and storage carbon equipment, it is ensured that storage carbon is set
It is standby to be in vacuum state in charging.
In the present embodiment, storage carbon equipment includes：Upper storage carbon pipe tank 37 containing sealing device and the lower storage containing sealing device
Carbon pipe tank 38；It is spiral to send the carbon outlet of carbon machine 36 and being connected into carbon mouth for the upper storage carbon pipe tank 37 containing sealing device；Filled containing sealing
The carbon outlet for the upper storage carbon pipe tank 37 put is connected with the lower storage carbon pipe tank 38 containing sealing device into carbon mouth；Material inlet valve is arranged on
It is spiral send the carbon outlet of carbon machine 36 and the upper storage carbon pipe tank 37 containing sealing device between carbon mouth；In the upper storage containing sealing device
The carbon outlet of carbon pipe tank 37 and lower storage carbon pipe tank 38 containing sealing device into being provided with intermediate transition valve between carbon mouth；Discharging
Valve is arranged on the carbon outlet of the lower storage carbon pipe tank 38 containing sealing device；In the upper storage carbon pipe tank 37 containing sealing device and containing sealing
A set of electrically-controlled valve and vacuum extractor are respectively configured with the lower storage carbon pipe tank 38 of device.
The structure of heating arrangements 3 is illustrated, heating arrangements 3 are electric heating mechanism, charcoal heating arrangements and/or gas
Heating arrangements.In the present embodiment, heating arrangements 3 can be in electric heating mechanism, charcoal heating arrangements and gas heating arrangements
Any one, or any two kinds therein, can also be three kinds of common mode of heatings.Wherein, electric heating mechanism is main
Have：Electromagnetic wire, high frequency, intermediate frequency, superaudio, plasma, microwave, electric-heating-wire-heating mechanism etc..In the present embodiment, the electricity of use
Heating and cooking appliance will have comprehensive and reliable heat insulation and preservation device, and ensure that electrically heated each heating module is independent
Power supply and each gas heating cooler independent gas supply of gas heating, not shut down when ensuring and replacing heating module and/or kitchen range.Need
It is noted that electrical heating and gas heating can be external heat or interior heating, only need to ensure to meet distillation process condition.
In order to improve the automatization level of the embodiment of the present invention, further include：Controller；The signal output part difference of controller
With vacuumize feed mechanism 1, spiral retorting machine 2, heating arrangements 3, gas cooling separating mechanism 4, vacuum Chu Tan mechanisms 5 letter
Number input terminal communication connection, so as to fulfill automated control.
In order to improve the seal of equipment, also to hollow chassis, feed mechanism 1,4 and of gas cooling separating mechanism are vacuumized
Encapsulation process is done by vacuum Chu Tan mechanisms 5.
When the embodiment of the present invention at work, house refuse is first subjected to broken bag, magnetic separation and selects iron, selection by winnowing to exclude metal, pottery
Porcelain, brick and stone, into crusher in crushing, the house refuse after crushing is dried, and acid wood feed bin is entered after drying, is used
Conveyer is sent into material bin 6, and is vacuumized in storage bin hopper 8.House refuse after vacuumizing enters the hollow of hollow chassis
In 15, vertical machine drives vertical drive shaft 26 to start reverse drive gear 27, is converted into Horizontal rotary vertical, drives
Shaft 24 rotates, thus drive forward flight 22 and reverse flight 23 by house refuse hollow chassis hollow 15
Move ahead in large capacity space between inner side and the outside of the body of rod 21.Under the anaerobic heating environment of totally-enclosed, carry out anaerobic and split
Reduction reaction is solved, house refuse is converted into gas (other gases such as steam, oil gas, combustible gas and carbon dioxide) and carbon, produces
Gas enter cleaner 28.Carbon under gravity, heat exchange cooling is fallen into plus the collaboration of reverse flight 23
In pipe 35.Explanation is needed exist for, the heating-up temperature in the embodiment of the present invention is 400-1100 degree, the primary life of destructive distillation per hour
Garbage treatment quantity living is 2-50 tons.
【Technique effect】
1st, isolation air is carried out to organic matter by heating arrangements 3 to heat, makes the macromolecular chain segment of composition organic matter one
Fracture occurs under the conditions of constant-pressure, temperature, time etc. and changes into recycling gas (fuel gas), liquid (cracked oil), consolidate
The primary energy material of (carbon) tri-state, trickles into forest, biomass and animal anaerobic heat just as the lava that volcano eruption produces
Solve and form tellurian coal, oil, natural gas, not only avoid the use to conventional garbage treatment technology, efficiently solve
It is of high cost in the prior art, time-consuming, environmental pollution and the technical problem taken up a large area, and realize energy substance circulation
With regeneration, destruction of the mankind's activity to environment and air is greatly reduced, can effectively change and use cereal crops at present
Produce the short present situation of the world food caused by the energy.
2nd, since heating arrangements 3 have carried out organic matter the heating of isolation air, thus avoid and bring oxygen into charging,
So as to avoid the generation of explosion, and then realize safety in production.
3rd, by the use to reverse flight 23, it is more advantageous to falling into hot friendship by the carbon of anaerobic cracking reduction reaction generation
Change in cooling tube 35.
4th, the embodiment of the present invention designs the spacing of outer wall to the inner wall of hollow 15 of the body of rod 21, makes the body of rod 21
Diameter it is sufficiently large, so as to improve the strength and stiffness of the body of rod 21, thus avoid because the strength and stiffness of the body of rod 21 are inadequate
The generation of caused flexural deformation situation.
5th, Horizontal enclosed is changed to vertical sealed by the embodiment of the present invention, the Horizontal enclosed in hollow chassis be reduced to first it is anti-
Line, vertical 39 reliability service of liquid seal device, improves the running seal of equipment.The reliable hermetic design of hollow chassis, adds
On vacuumize the seal of feed mechanism 1, gas cooling separating mechanism 4 and vacuum Chu Tan mechanisms 5, make the seal of equipment significantly
Improve, built an efficiency of heating surface height and easy to the large space of conveying, so as to solve horizontal destructive distillation dress of the prior art
The problem of yield is not high in the process of running is put, safe and reliable, economic equipment is provided for large-scale destructive distillation treatment plant.
Provided in an embodiment of the present invention is a kind of anaerobic destructive distillation device of totally-enclosed, and reduction reaction is cracked using anaerobic, will
House refuse is converted into combustible gas, oil and carbon, will be sent out after combustible gas purifying, cooling, storage into combustible gas generating set
Electricity, the rubbish such as house refuse, stalk, medical waste, sludge are can be widely applied to from innoxious, recycling, the angle of minimizing
The processing of rubbish.The embodiment of the present invention realizes domestic rubbish disposal process continous way, self-heating, does not block, is air tight, is indeformable
And the domestic rubbish disposal on the same day can be finished, after building waste and metal is rejected, house refuse realizes full dose
Innoxious (high temperature), the minimizing of full dose and the recycling of full dose.
Although preferred embodiments of the present invention have been described, but those skilled in the art once know basic creation
Property concept, then can make these embodiments other change and modification.So appended claims be intended to be construed to include it is excellent
Select embodiment and fall into all change and modification of the scope of the invention.
Obviously, various changes and modifications can be made to the invention without departing from essence of the invention by those skilled in the art
God and scope.In this way, if these modifications and changes of the present invention belongs to the scope of the claims in the present invention and its equivalent technologies
Within, then the present invention is also intended to comprising including these modification and variations.
Claims (10)
- A kind of 1. house refuse large-size horizontal destructive distillation device, it is characterised in that including：Vacuumize feed mechanism, spiral retorting machine, Heating arrangements, gas cooling separating mechanism and vacuum Chu Tan mechanisms；The material output terminal for vacuumizing feed mechanism with it is described The material input connection of spiral retorting machine；The gas output end of the spiral retorting machine and the gas cooling separating mechanism Gas input connects, and the carbon outlet of the spiral retorting machine is connected with the vacuum Chu Tan mechanisms into carbon mouth；The heating Mechanism carries out the material in the spiral retorting machine isolation air heating；The isolation air mode of heating is interior mode of heating And/or external heating mode.
- 2. device as claimed in claim 1, it is characterised in that the feed mechanism that vacuumizes includes：Material bin, the first valve Door, storage bin hopper, the second valve, the first screw conveyor, the second screw conveyor, the 3rd valve, vaccum-pumping equipment；The pan feeding The discharge port of bucket is connected with the feed inlet of the storage bin hopper；First valve be arranged on the material bin and the storage bin hopper it Between；Second valve is arranged on the discharge port of the storage bin hopper；First screw conveyor is arranged in the storage bin hopper, Material is exported from the discharge port of the storage bin hopper；The feed inlet of second screw conveyor and the discharge port of the storage bin hopper Connection, the discharge port of second screw conveyor are connected with the material input of the spiral retorting machine；Described vacuumize sets It is standby to be connected with the storage bin hopper；3rd valve is arranged between the vaccum-pumping equipment and the storage bin hopper；The storing Struggle against as vertical storage bin hopper or horizontal storage bin hopper.
- 3. device as claimed in claim 1, it is characterised in that the spiral retorting machine includes：It is engine base, hollow chassis, spiral Bar and motive power outputting apparatus；The hollow chassis is arranged on the engine base；The screw rod is arranged in the hollow chassis； The power intake of the screw rod is connected with the power output end of the motive power outputting apparatus；The material of the hollow chassis is defeated Enter end to connect with the material output terminal for vacuumizing feed mechanism, the gas output end of the hollow chassis and the gas are cold But the gas input connection of separating mechanism, the carbon outlet of the hollow chassis connect with the vacuum Chu Tan mechanisms into carbon mouth It is logical.
- 4. device as claimed in claim 3, it is characterised in that the hollow chassis includes：Hollow, the first thermal insulation board and Two thermal insulation boards；First thermal insulation board and second thermal insulation board are separately positioned in the both ends of the hollow；It is described spiral Bar is arranged in the hollow；There are material input, gas output end and carbon outlet in the hollow.
- 5. device as claimed in claim 4, it is characterised in that the screw rod includes：The body of rod, forward flight, reverse spiral shell Blade and shaft；The shaft is connected with the body of rod；The both ends of the shaft respectively with first thermal insulation board, described second Thermal insulation board connects；The shaft is connected with the power output end of the motive power outputting apparatus；The forward flight and described inverse It is arranged to flight on the body of rod；The reverse flight is located at the top of the carbon outlet of the hollow；Work as use When the interior mode of heating or the external heating mode, the spacing of outer wall to the inner wall of the hollow of the body of rod is 50- 300mm；When using the interior mode of heating and the external heating mode, the inner wall of the outer wall of the body of rod to the hollow Spacing be 100-600mm；Inner wall, first thermal insulation board and described second of outer wall, the hollow in the body of rod Forming one between thermal insulation board can ensure that pyrolysate by the large capacity space of abundant destructive distillation.
- 6. device as claimed in claim 5, it is characterised in that the motive power outputting apparatus includes：Motor, vertical type transmission Axis, reverse drive gear and vertical liquid seal device；The first end of the power output end of the motor and the vertical drive shaft Connection；The second end of the vertical drive shaft is connected with the first end of the reverse drive gear；The reverse drive gear Second end is connected with the shaft；The vertical liquid seal device is connected with the vertical drive shaft, the hollow.
- 7. device as claimed in claim 1, it is characterised in that the gas cooling separating mechanism includes：Cleaner, desulfurization Equipment, cooling device, multistage decoking equipment, oily water separating equipment and gas storage equipment；The gas input of the cleaner with The gas output end connection of the spiral retorting machine, the gas output end of the cleaner and the gas of the desulphurization plant are defeated Enter end connection；The gas output end of the desulphurization plant is connected with the gas input of the cooling device；The cooling device Gas output end connect with the gas input of the multistage decoking equipment, the liquid material output terminal of the cooling device and The material input connection of the oily water separating equipment；The gas material of the cooling device is devoked through the multistage decoking equipment After be passed through gas storage equipment storage.
- 8. device as claimed in claim 7, it is characterised in that the cooling device is multistage cooling device cascaded structure.
- 9. device as claimed in claim 1, it is characterised in that the vacuum Chu Tan mechanisms include：It is spiral go out carbon machine, heat exchange Cooling tube, spiral send carbon machine, storage carbon equipment, material inlet valve, electrically-controlled valve, discharge valve and vacuum extractor；It is described it is spiral go out carbon Machine is arranged in the heat exchange cooling tube；The heat exchange cooling tube connects into the carbon outlet of carbon mouth and the spiral retorting machine Logical, the carbon outlet of the heat exchange cooling tube spiral send being connected into carbon mouth for carbon machine with described；It is described it is spiral send carbon machine go out carbon Mouth is connected with the storage carbon equipment into carbon mouth；The material inlet valve is arranged on the feed inlet of the storage carbon equipment；The discharging Valve is arranged on the discharge port of the storage carbon equipment；The vacuum extractor is passed through the storage carbon equipment；The electrically-controlled valve is set Between the vacuum extractor and the storage carbon equipment.
- 10. device as claimed in any one of claims 1-9 wherein, it is characterised in that the heating arrangements are electric heating mechanism, charcoal Heating arrangements and/or gas heater structure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711322437.7A CN108018056A (en) | 2017-12-12 | 2017-12-12 | A kind of house refuse large-size horizontal destructive distillation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711322437.7A CN108018056A (en) | 2017-12-12 | 2017-12-12 | A kind of house refuse large-size horizontal destructive distillation device |
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| CN108018056A true CN108018056A (en) | 2018-05-11 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711322437.7A Pending CN108018056A (en) | 2017-12-12 | 2017-12-12 | A kind of house refuse large-size horizontal destructive distillation device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110791304A (en) * | 2019-09-25 | 2020-02-14 | 珠海格力绿色再生资源有限公司 | Continuous microwave cracking equipment and method |
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