CN206838753U - A kind of plastic garbage conveying equipment - Google Patents
A kind of plastic garbage conveying equipment Download PDFInfo
- Publication number
- CN206838753U CN206838753U CN201720722872.8U CN201720722872U CN206838753U CN 206838753 U CN206838753 U CN 206838753U CN 201720722872 U CN201720722872 U CN 201720722872U CN 206838753 U CN206838753 U CN 206838753U
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- Prior art keywords
- plastic garbage
- accumulator
- pipe
- discharging opening
- conveying
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- 239000004033 plastic Substances 0.000 title claims abstract description 98
- 229920003023 plastic Polymers 0.000 title claims abstract description 98
- 239000010813 municipal solid waste Substances 0.000 title claims abstract description 79
- 238000007599 discharging Methods 0.000 claims abstract description 39
- 238000005336 cracking Methods 0.000 claims abstract description 29
- 238000012545 processing Methods 0.000 claims abstract description 10
- 238000000197 pyrolysis Methods 0.000 claims description 67
- 239000003921 oil Substances 0.000 claims description 40
- 238000004519 manufacturing process Methods 0.000 claims description 13
- 239000000567 combustion gas Substances 0.000 claims description 9
- 238000011084 recovery Methods 0.000 claims description 9
- 238000003860 storage Methods 0.000 claims description 9
- 239000002245 particle Substances 0.000 abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 70
- 239000007789 gas Substances 0.000 description 37
- 235000019198 oils Nutrition 0.000 description 37
- 238000002485 combustion reaction Methods 0.000 description 35
- 239000002893 slag Substances 0.000 description 20
- 239000003337 fertilizer Substances 0.000 description 17
- 238000000926 separation method Methods 0.000 description 17
- 239000007788 liquid Substances 0.000 description 16
- 238000000034 method Methods 0.000 description 12
- 239000000203 mixture Substances 0.000 description 12
- 239000004575 stone Substances 0.000 description 12
- 239000000463 material Substances 0.000 description 11
- 230000003472 neutralizing effect Effects 0.000 description 11
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 10
- 239000011229 interlayer Substances 0.000 description 10
- 230000005540 biological transmission Effects 0.000 description 9
- 239000003546 flue gas Substances 0.000 description 9
- 238000010438 heat treatment Methods 0.000 description 9
- 239000000126 substance Substances 0.000 description 8
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 7
- 239000000654 additive Substances 0.000 description 7
- 230000000996 additive effect Effects 0.000 description 7
- 229910000831 Steel Inorganic materials 0.000 description 6
- 239000010959 steel Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 239000004744 fabric Substances 0.000 description 5
- 239000000446 fuel Substances 0.000 description 5
- 238000009434 installation Methods 0.000 description 5
- 238000006386 neutralization reaction Methods 0.000 description 5
- 239000002341 toxic gas Substances 0.000 description 5
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- 238000007664 blowing Methods 0.000 description 4
- 239000000110 cooling liquid Substances 0.000 description 4
- 239000012530 fluid Substances 0.000 description 4
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 4
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 239000010865 sewage Substances 0.000 description 4
- 239000007921 spray Substances 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- 238000010276 construction Methods 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 235000019476 oil-water mixture Nutrition 0.000 description 3
- 229910001220 stainless steel Inorganic materials 0.000 description 3
- 239000010935 stainless steel Substances 0.000 description 3
- 241000276425 Xiphophorus maculatus Species 0.000 description 2
- 238000005452 bending Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 238000004880 explosion Methods 0.000 description 2
- 239000012634 fragment Substances 0.000 description 2
- 238000007654 immersion Methods 0.000 description 2
- 230000008676 import Effects 0.000 description 2
- 238000003672 processing method Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 206010020852 Hypertonia Diseases 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 230000001133 acceleration Effects 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 235000011114 ammonium hydroxide Nutrition 0.000 description 1
- 238000000137 annealing Methods 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000003776 cleavage reaction Methods 0.000 description 1
- 239000003034 coal gas Substances 0.000 description 1
- 210000001520 comb Anatomy 0.000 description 1
- 238000009841 combustion method Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000005243 fluidization Methods 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 238000007429 general method Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000011796 hollow space material Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000003032 molecular docking Methods 0.000 description 1
- 239000002808 molecular sieve Substances 0.000 description 1
- 230000000505 pernicious effect Effects 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000007017 scission Effects 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 239000010913 used oil Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/141—Feedstock
- Y02P20/143—Feedstock the feedstock being recycled material, e.g. plastics
Landscapes
- Processing Of Solid Wastes (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
Abstract
A kind of plastic garbage conveying equipment, suitable for a kind of plastic garbage processing system, including air conveying device, accumulator, chain type lifting conveying device;Described air conveying device is arranged between plastic garbage sorting device and accumulator, and its charging aperture is connected with the discharging opening of plastic garbage sorting device, and its discharging opening is connected with accumulator;Including feeding channel, wind net is dissipated;Described feeding channel is arranged between the discharging opening and accumulator of plastic garbage sorting device, is tubular structure;Described scattered wind net is arranged on the suitable for reading of accumulator, and it is suitable for reading to cover whole accumulator;Described scattered wind net is network structure, and its mesh diameter is less than the particle diameter of plastic garbage;Described accumulator is arranged on the discharge port end of air conveying device, is the cavity body of open topped;Described chain type lifting conveying device one end is arranged on internal hopper, and the other end is connected with In Cracking Feedstock storehouse, has the characteristics of plastic garbage conveying function that can realize plastic garbage processing system.
Description
Technical field
The invention belongs to field of garbage disposal, it is more particularly to a kind of by plastic garbage continuous processing and comprehensively utilize method
In plastic garbage processing system in plastic garbage conveying equipment.
Background technology
Plastic garbage is one of rubbish common in daily production and life, due to the degradability that is difficult to of plastic garbage, mesh
The method of pre-treatment plastic garbage is mainly using landfill, burning, the method cracked;Landfill method is that plastic garbage is bought in into underground,
By its natural degradation, such way time cycle length, have greater environmental impacts, land occupation;Combustion method is by plastic garbage
Burnt, either with Other Waste or the combust of material one, as generating or other thermals source, such way is due to modeling
A large amount of toxic gases can be produced after material burning, secondary pollution is caused to environment;The method of cracking, it is that plastic garbage is put into cracking
Stove, plastics are decomposed again, petroleum substance is produced after decomposition, fuel or other raw materials can be used as to reuse;Existing
Method for cracking treatment in, problems be present, first, existing complete continuous cracking equipment is to plastics in plastic garbage
Composition requires, that is to say, that, it is desirable to the uniformity of the plastics variety in plastic garbage will get well, the ratio containing certain plastic components
Example is needed to reach more than 85%, and this can be realized, for refuse classification for the good country that refuse classification is done
Incompact country that is bad or doing is difficult to realize;It is existing if such component requirements can not be reached
Cracking apparatus cannot realize the cracking of plastic garbage, gently then equipment does not work, heavy then cause equipment explosion;It is furthermore right
Substantial amounts of toxic gas is produced in the processing method discontinuously cracked, cracking process can still be discharged into air, to environment
Secondary pollution is caused, while strong acid is produced after these toxic gases chance water, causes equipment corrosion serious, shortens equipment and use the longevity
Life;3rd, due to different plastic components in cracking be present, and cracking temperature is merely able to adapt to the cracking temperature of a certain plastics
Degree, it is impossible to the cracking of plastic garbage is realized on a pyrolysis furnace, while needs to be sorted plastics variety, it is residual after cracking
Slag is easily bonded on furnace wall, causes pyrolysis furnace to damage, while the residue for clearing up furnace wall will also result in the secondary pollution of environment;The
4th, the sorting of existing plastic garbage is the method by the way that plastic garbage is crushed, and so consumption energy is big, causes the energy unrestrained
Take.
The content of the invention
For drawbacks described above existing for the processing method of existing plastic garbage, the present invention proposes a kind of place of plastic garbage
Reason method, it is characterised in that:Comprise the following steps:1st, plastic garbage is pre-processed, including sorting, go the removal of impurity;2nd, will
Plastic garbage after sorting loads conveying equipment, and is transported to In Cracking Feedstock storehouse;3rd, normal pressure anaerobic company is carried out into pyrolysis furnace
Continuous cracking;4th, the waste residue by pyrolysis furnace discharge is sent into building block production equipment, and is squeezed into building block and is supplied construction application;5th, will
Steam caused by pyrolysis furnace eliminates hydrogen chloride and sulfur dioxide in steam by neutralizing device;6th, by steaming caused by pyrolysis furnace
Vapour enters condenser, oils and water is become liquid;7th, air accumulator will be transported to by the fuel gas after condenser, and passed through
Pyrolysis furnace is transported to after compressor as fuel;8th, the liquid that condenser is discharged is transported to oil water separator, oil and water is entered
Row separation, and it is respectively delivered to pond and oil tank;9th, by by neutralizing the treated liquid of device by proportioning, liquefied is formed
Fertilizer;10th, above step is realized by plastic garbage processing system.
Described plastic garbage processing system, including pretreatment system, conveying equipment, additive-adding device, pyrolysis furnace,
Neutralize device, combustion gas recovery system, condenser, oil water separator, building block production equipment, storage of oils device;Described pre- place
Reason system is arranged on the feed inlet end of conveying equipment, is connected with conveying equipment;It is pre- that described pretreatment system includes plastic garbage
Drying unit, plastic garbage sorting device;Described plastic garbage pre-drying device is arranged on entering for plastic garbage sorting device
Material mouth one end, it is connected with plastic garbage sorting device;Described plastic garbage sorting device fills installed in plastic garbage prebake
The discharging opening one end put, its charging aperture are connected with plastic garbage pre-drying device, and the charging aperture of its discharging opening and conveying equipment connects
Connect;Described conveying equipment be arranged between pretreatment system and dore furnace, its import be connected with pretreatment system, its outlet and
Dore furnace connects;Described additive-adding device is arranged on conveying equipment, and its end is connected with dore furnace feeding warehouse;It is described
Pyrolysis furnace be arranged on conveying equipment discharging opening one end, its feeding warehouse is connected with conveying equipment and additive-adding device, and it goes out
Gas port is connected with gas transmission pipeline, and its slag notch is connected with building block production equipment;Described neutralization device is arranged on pyrolysis furnace
Top, be connected with the feeding warehouse bottom pyrolysis furnace furnace chamber of pyrolysis furnace by pipeline, and be connected with neutralization additive and water inlet pipe,
Its liquid fertilizer stoste outlet is connected with liquid fertilizer storage device by pipeline;Described combustion gas recovery system is arranged on condensation
Between device and pyrolysis furnace, connected respectively with condenser and pyrolysis furnace by pipeline;Described condenser is arranged on pyrolysis furnace side,
Connected by the gas outlet duct of pipeline and pyrolysis furnace;Described oil water separator is arranged on the bottom of condenser, and it is exported
It is connected respectively with oily output channel and water delivery pipe road;Described building block production equipment is arranged on the side of pyrolysis furnace, with cracking
The slag notch linking of stove;Described storage of oils equipment is arranged on the side of oil water separator, passes through pipeline and oil water separator
Oil-out connection.
Plastic garbage in described step 1 is carried out by plastic garbage pretreatment system, including preheating, sorting,
Conveying;Described preheating is that the plastic garbage pre-processed using the preheating of pyrolysis furnace to needs is preheated in course of conveying;
Described sorting is that the metal in plastic garbage, block inorganic matter, fiber-like article are passed through into sorting device using sorting device
Select respectively, metal object is sent into metal reclamation enterprise is recycled;Block inorganic matter such as stone etc. is sent to building block extruding
Equipment is squeezed into building block together with waste residue;Fiber-like such as clothes, shoes etc. are sold into such article recovery company to recycle;Institute
The conveying stated, it is that remaining plastic hybrid is sent into conveying device.
Described sorting device, it is characterised in that:Including frame, shell, conveyer belt, setting wheel, separation wheel, drawing-inroller,
Particle discharging opening, stone discharging opening, plastics discharging opening;Described frame is arranged in Equipment Foundations, including supporting leg and framework, is used
In supporting and install whole functional part;Described shell, in frame, it is enclosed in frame periphery;Described conveyer belt
It is Chain conveyer multiple roll support belt installed in one end of frame, can be by pending plastic garbage from one end of sorting device
It is sent to inside sorting device;Described setting wheel is arranged in frame, positioned at the top of conveyer belt, and positioned at conveying tail
One end;Switch-plate is provided with described setting wheel;Described switch-plate is activity installation;The diameter of described setting wheel with
The conveying chaindriven sprocket diameter of tail matches;The direction of rotation of described setting wheel and conveying tail drive sprocket
Direction of rotation is opposite;Described separation wheel is arranged in frame, positioned at the bottom of conveying tail one end drawing-inroller;Described point
Sorter is installed on choosing wheel;Described sorter is platy structure;Described sorter is uniformly covered with the excircle of separation wheel
Surface;The direction of rotation of described separation wheel is identical with the direction of rotation of drawing-inroller;Described drawing-inroller is arranged in frame, position
In the rear portion of setting wheel and the top of separation wheel;Feed appliance is provided with described drawing-inroller;Described feed appliance is tabular,
The even excircle for being covered with drawing-inroller;Described drawing-inroller excircle is additionally provided with blower, and described blower is evenly arranged in
The excircle of drawing-inroller;The direction of rotation of described drawing-inroller is identical with the direction of rotation of separation wheel;Described particle discharging opening
On shell, positioned at the bottom of separation wheel;Described particle discharging opening is screen cloth type, the aperture of its screen cloth and is sorted
The fragment of plastic garbage matches, i.e. the particle diameter less than plastic flakes;Described stone discharging opening is arranged on shell, positioned at point
Select the rear of wheel and positioned at the top of particle discharging opening;Described stone discharge outlet is provided with automatic stock stop;It is described from
Dynamic stock stop is made up of multiple material blocking rods;Described plastics discharging opening is arranged on shell, positioned at the rear portion oblique upper of drawing-inroller,
Docked with the entrance of conveying device.
Conveying equipment in described step 2, it is characterised in that:Including air conveying device, accumulator, chain type lifting conveying dress
Put;Described air conveying device is arranged between plastic garbage sorting device and accumulator, and its charging aperture is set with plastic garbage sorting
Standby discharging opening connection, its discharging opening are connected with accumulator;Including feeding channel, wind net is dissipated;Described feeding channel is arranged on
It is tubular structure between the discharging opening and accumulator of plastic garbage sorting device, it is connected one end with plastic garbage sorting device
Sectional area be less than the sectional area of one end be connected with accumulator;Described scattered wind net is arranged on the suitable for reading of accumulator, and covering is whole
Accumulator is suitable for reading;Described scattered wind net is network structure, and its mesh diameter is less than the particle diameter of plastic garbage.
Described accumulator is arranged on the discharge port end of air conveying device, is the cavity body of open topped.
Described chain type lifting conveying device one end is arranged on internal hopper, and the other end is connected with In Cracking Feedstock storehouse,
Including support, drive sprocket, sprocket wheel is supported, chain, conveys scraper plate, the pre-heat treatment device, outer cover, the rail of additive-adding device
Road;Described support is arranged between accumulator and pyrolysis furnace, is connected respectively with accumulator and pyrolysis furnace support member;Described
Drive sprocket is arranged on support one end, is connected with the drive of the power set of conveying equipment;Described drive sprocket has two,
On same axle, and it is located at support both sides;Described support sprocket wheel is rack-mount, and described support sprocket wheel has more
It is individual, positioned at support both sides, the longitudinal side of support is evenly distributed on, is put down respectively positioned at the identical of support both sides with drive sprocket
Face;Described chain has two, is separately mounted to the drive sprocket of support both sides and supports sprocket wheel excircle structure in a ring;Institute
The conveying scraper plate stated is arranged between two chains, and its both ends is connected with the chain of both sides respectively;Described conveying scraper plate has more
It is individual, it is parallel and be evenly arranged on ring chain;Described the pre-heat treatment device is arranged on inside outer cover close to pyrolysis furnace one end,
And positioned at the outer upper of conveying scraper plate;Including tube heater, blowing hot-air device;Described tube heater is by multiple heating
Pipe forms, and each heating tube is interconnected, and its heating tube connects with the outlet pipe of pyrolysis furnace;Described blowing hot-air device installation
In the discharge port end of chain type lifting conveying device, it is made up of warm-air pipe, the air outlet alignment chain type lifting conveying dress of its warm-air pipe
The spout area put;Described outer cover is arranged on bracket outer, and is thin-walled in side of the support in addition to both ends be wrapped in
Structure;The track of described additive-adding device, installed in support both sides, it is connected through outer cover with support;Described addition
The track of agent adding set is made up of two parallel tracks.
Normal pressure anaerobic continuous cracking described in described step 3, refers to plastic garbage mixture being sent to pyrolysis furnace
In, the cracking state in pyrolysis furnace is anaerobic, is normal pressure in pyrolysis furnace, its cracking process is continuous.
Described pyrolysis furnace, it is characterised in that:Including support, underdrive device, slag pan, lower blast pipe, lower interlayer, combustion are received
Tracheae, burner, combustion chamber, hot blast discharge pipe, fuel-air mixture efferent duct, fixed gas escape pipe, upper cover, charging axle driving dress
Put, charging axle, taper feed bin, feeding screw, feeder outer cover, upper cover plate, flowline, upper stock guide, one-level distributing device, on
Comb, upper cylinder, two level distributing device, lower comb, lower cylinder, lower cover and slag-scraper, main shaft, dregs-separating device, vapor pipe, outer swivel joint,
Inward turning adapter, lower water inlet pipe, lower warm-air pipe, body of heater;Described support is arranged on the periphery bottom of body of heater, can support and consolidate
Determine body of heater;Described underdrive device is arranged on bottom of furnace body, can drive main shaft and receive slag pan rotation;Described underdrive dress
It is worm gearing to put;Described receipts slag pan is arranged on the bottom of body of heater, is the thin wall cavity body of upper shed, can be around
Its center rotates;Described receipts slag pan edge is provided with slag notch;Described lower blast pipe is arranged on body of heater, with burner
Place space connects;Described lower interlayer is arranged on body of heater inner chamber bottom, and upper end is connected with the lower interlayer wall where burner, and
Confined space is formed with lower interlayer inwall;Described Gas Pipe is arranged on body of heater, is connected through furnace body wall with burner;It is described
Burner be arranged on combustion chamber lower wall on, extend into combustion chamber through combustion chamber lower wall;Described burner periphery have into
Air channel;Described burner has multiple, is evenly distributed on the lower wall of combustion chamber;Described combustion chamber is arranged in the middle part of body of heater, is
Relatively closed space;Its lower wall is connected with body of heater and lower interlayer, and upper wall has certain intervals, end and lower wall and body of heater with lower wall
Connection;Described combustion chamber is hollow at main shaft position, has distance with main shaft excircle;Described hot blast discharge pipe is arranged on
Outside body of heater, connected with combustion chamber;Described fuel-air mixture efferent duct is arranged on body of heater, on upper stock guide
Portion;The position of described fuel-air mixture efferent duct is higher than the position of flowline;Described fixed gas escape pipe is arranged on body of heater
On, positioned at taper feed bin and body of heater binding site;Described upper cover is arranged at the top of body of heater, be hemi-spherical cavities body, bottom and
Body of heater airtight connection;Described upper cover side is provided with charging aperture;Described charging axial brake device is arranged on upper cover top, with
Axis connection is fed, charging axle can be driven to rotate;Described charging axle is arranged between upper cover and taper feed bin, can be around itself
Axis rotates;Described taper feed bin is arranged on upper of furnace body, is back taper thin wall cavity body, along closed with body of heater in its taper
Connection, circular open is arranged at bottom;Described feeding screw is arranged on the lower end of charging axle, and is opened positioned at the lower end of taper feed bin
At mouthful, it is fixedly connected with charging axle;Described feeding screw matches with feeder outer cover internal diameter;Described feeder outer cover
It is tubular construction installed in the lower end of taper feed bin;Described feeder outer cover upper end is fixedly connected with taper feed bin, its internal diameter
Matched with feeding screw rotation external diameter;There is enlarging described feeder outer cover lower end;Described upper cover plate is arranged on conical material
The lower end in storehouse, it is umbrella shape, Open Side Down;Its outward flange interlocks with upper stock guide;Described flowline is set on body of heater, positioned at upper
The top of stock guide, its height are less than the position of fuel-air mixture efferent duct;Described upper stock guide is arranged on upper of furnace body position
In combustion chamber top, the bottom of upper cover, its overhanging end interlocks with upper cover;Described one-level distributing device is arranged on main shaft upper end, and one
End is fixedly connected with main shaft, and the other end is hanging, is made up of polylith drapery panel, and described drapery panel is interlaced, in flakey cloth
Put, its free end has certain interval with Inner Wall of Combustion Chamber;The drapery panel of described one-level distributing device has the angle tilted down;Institute
The upper comb stated is arranged between Inner Wall of Combustion Chamber and upper cylinder, for comb shape structure, both ends respectively with Inner Wall of Combustion Chamber and upper drum outer wall
Connection;Described upper cylinder is tubular structure, and its outer wall is fixedly connected with upper comb, and inner side is provided with the axle bed of supports main shaft;It is described
Two level distributing device be arranged on cylinder lower end, one end is connected with main shaft, and the other end is hanging, is made up of polylith drapery panel, described
Polylith drapery panel is interlaced, is arranged in flakey, and its free end has certain interval with Inner Wall of Combustion Chamber;Described two level cloth
The drapery panel of device has the angle tilted down;Described lower comb is arranged between Inner Wall of Combustion Chamber and lower cylinder, for comb shape structure, its
Both ends are connected with Inner Wall of Combustion Chamber and lower drum outer wall respectively;Described lower cylinder is arranged on cylinder bottom, has certain distance with upper cylinder,
For tubular structure, its outer wall is fixedly connected with lower comb;Described lower cover and slag-scraper are arranged on main shaft, its slag-scraper with
Combustion chamber lower inner wall contact;Described main shaft is arranged on underdrive seat, is hollow shaft, can be in the drive of underdrive device
Lower rotation;Water inlet pipe, warm-air pipe, vapor efferent duct are installed inside described main shaft;Described dregs-separating device is arranged on main shaft
On, it can be rotated with main shaft, be umbrella-shaped structure;Described vapor pipe, on main shaft, divided by stretching out to pass through inside main shaft
Slag device can provide vapor to the upper surface of dregs-separating device for the upper surface of dregs-separating device;Described outer swivel joint is arranged on bottom
On seat, one end is connected with the warm-air pipe in main shaft, and the other end is connected with lower warm-air pipe;Described inward turning adapter installation
Inside outer swivel joint, one end is connected with the water inlet pipe in main shaft, and the other end is connected with lower water inlet pipe;Under described
Water inlet pipe is arranged on inward turning adapter, is penetrated lower warm-air pipe and is connected with water source;Described lower warm-air pipe is transferred installed in outward turning
On head, one end is connected with outer swivel joint, and the other end is connected with heat air source;Described body of heater is tubular structure, installed in branch
On frame, upper end is connected with upper cover, and lower end is hanging.
Described main shaft, it is characterised in that:Including axis body, axle bed, vapor pipe, enter warm-air pipe, water inlet pipe, baffle plate;Institute
The axis body stated is the cavity body of one end closing, and its open at one end is downward, is connected in open at one end with axle bed;Described axle bed is set
Installation bearing and the structure being connected with transmission device are provided with axis body open at one end, axle bed;Described steam pipe peace
In axis body internal cavities, there is distance at its upper end distance axis intracoelomic cavity top seal, axis body is stretched out in its lower end through baffle plate
Reach dregs-separating device surface outside and through dregs-separating device;Described steam pipe needs to be tightly connected with baffle plate junction;Described enters
Warm-air pipe is arranged on baffle plate, and with baffle plate fixed seal connection, its upper end is hanging, and lower end is connected with outer swivel joint;Described
Water inlet pipe is arranged on into warm-air pipe, and upper end is hanging, and lower end is connected with inward turning adapter;The upper end of described water inlet pipe stretch out into
The upper end of warm-air pipe;Described baffle plate is arranged at the cavities open of axle bed lower end, is tightly connected with axle bed;Described water steams
Steam pipe has multiple, is evenly distributed on the circumference of axis body intracavity section.
Described step 4 be will pyrolysis furnace discharge residue and sorting device in sort out block inorganic matter such as stone,
Cement block etc., crush, mix and add the building block that appropriate additive is squeezed into architectural engineering.
Described step 5 is to be allowed to be converted into by neutralizing device by caused hydrogen chloride in pyrolysis furnace and sulfur dioxide
Form the stoste of liquid fertilizer.
Described neutralizing device, it is characterised in that:Including flue gas inlet pipe, shell, petticoat pipe, blast pipe, spray equipment, chemical fertilizer
Stoste outlet;Described flue gas inlet pipe is arranged on the lower end of shell, and one end is connected with the combustion chamber installed in lower housing portion, lower end
The fixed gas escape pipe of middle part and pyrolysis furnace connects, and the other end stretches into enclosure;Described shell is arranged on combustion chamber upper end,
It is confined air cavity positioned at pyrolysis furnace top;Described petticoat pipe is arranged on the upper end of flue gas inlet pipe, is umbrella-shaped structure;Described
Petticoat pipe has gap with inner walls;There is gap described petticoat pipe bottom with flue gas inlet pipe upper end;Described blast pipe is arranged on outer
Shell top, it is tubular structure, one end connects with enclosure, the other end and atmosphere;Described spray equipment is arranged on row
Tracheal strips, there is certain distance with petticoat pipe above petticoat pipe, neutralising fluid can be sprayed to the sky between petticoat pipe and blast pipe
Between;Described chemical fertilizer stoste outlet is arranged on the bottom of shell, is connected with shell inner cavity.
Described step 6 is that steam caused by pyrolysis furnace is cooled by condenser, turns the higher gas of condensing temperature
Liquid is turned to, refers in particular to oil vapour and vapor in this step.
Described condenser, it is characterised in that:Including first-stage condenser, first-stage condenser shell, first-stage condenser heat is handed over
Parallel operation, right air inlet pipe, secondary condenser shell, non-condensable gas export, middle air inlet pipe, left air inlet pipe, secondary condenser heat exchange
Device;Described first-stage condenser is arranged on the upper end of oil water separator, the catch tray connection suitable for reading of its lower end and oil water separator;
Described first-stage condenser shell is arranged on the upper end of oil water separator;Described first-stage condenser heat exchanger is arranged on one-level
In condenser casing, there is cooling liquid to pass through in heat exchanger;Described right air inlet pipe is arranged on first-stage condenser shell upper
Right side, one end connect with the outlet of pyrolysis furnace cracked gas, and the other end connects with first-stage condenser shell inner cavity;Described two level is cold
Condenser shell is arranged on inside first-stage condenser, its underpart opening, upper periphery and first-stage condenser shell airtight connection;It is described
Non-condensable gas export be arranged on secondary condenser shell, connected with secondary condenser shell inner cavity;Described middle air inlet pipe
Placed in the middle installed in first-stage condenser shell upper, one end connects with the outlet of pyrolysis furnace cracked gas, the other end and first-stage condenser
Shell inner cavity connects;Described left air inlet pipe is arranged on the left of first-stage condenser shell upper, one end and pyrolysis furnace cracked gas
Outlet connection, the other end connect with first-stage condenser shell inner cavity;It is cold that described secondary condenser heat exchanger is arranged on two level
Condenser enclosure, the interior circulation of its heat exchanging pipe have cooling liquid.
Described step 7 is to will not be able to liquefied gas at normal temperatures, passes through combustion gas retracting device this step middle finger
It is carbon monoxide and hydrogen, is transported to air accumulator, is then transported to again after compressor in pyrolysis furnace and is used as fuel, thus
Addition fuel in addition is saved, saves the energy.
Described step 8 is that oil water mixture is sent into oil water separator, and oil is separated with water, and is respectively delivered to not
Same storage location.
Described oil water separator, it is characterised in that:Including outer shell of oil-water separator, oil-out, sewage draining exit, feed tube,
Outlet pipe, catch tray;Described outer shell of oil-water separator is arranged on the lower end of condenser, is thin wall cavity body, and outside condenser
Shell connects;Described oil-out is arranged on outer shell of oil-water separator, is connected with outer shell of oil-water separator inner chamber, described is fuel-displaced
Position height of the position height on outer shell of oil-water separator of mouth higher than the delivery port of outlet pipe;Described sewage outfalls setting
In the bottom of outer shell of oil-water separator, valve is installed;Described feed tube is arranged on outer shell of oil-water separator inner chamber, for pipe
Shape, upper end are connected with catch tray, and lower end is open;Described outlet pipe is arranged on outer shell of oil-water separator, passes through pipeline and oil
The position height of the upper end delivery port of the described outlet pipe of separator bottom of shell inner cavity connection is high less than the position of oil-out
Degree;Described catch tray is arranged on the inner chamber of outer shell of oil-water separator, be back taper thin-walled hollow body, on its upper end and condenser
First-stage condenser cage connection, lower end is connected with feed tube.
Described step 9, it is that the stoste of the liquid fertilizer of output in step 5 is made by adding appropriate additive
Meet the liquid fertilizer of chemical fertilizer standard index, and store.
Beneficial effect
The beneficial effects of the present invention are, the continuous cracking of multicomponent plastic garbage can be realized, and in cracking process not
Solid, the liquids and gases of any pollution environment are discharged, the comprehensive utilization of plastic garbage is realized, saves the energy.
Brief description of the drawings
Fig. 1 is the structural representation of the present invention
1. pretreatment system, 2. conveying equipments, 3. pyrolysis furnace feed bins, 4. pyrolysis furnaces, 5. pyrolysis furnace gas outlet ducts, 6.
Combustion gas recovery system, 7. air compressors, 8. condensers, in 9. and device, 10. oil water separators, 11. oils efferent ducts, 12.
Water delivery pipe, 13. oil-water mixture delivery pipes, 14. building block production equipments, 15. building blocks are pulverized and mixed device.
Fig. 2 is the structural representation of pretreatment system sorting device
1-1. frames, 1-2. shells, 1-3. conveyer belts, 1-4. setting wheels, 1-5. separation wheels, 1-6. drawing-inrollers, 1-7. are broken
Expect discharging opening, 1-8. stone discharging openings, 1-9. plastics discharging openings.
Fig. 3 is the structural representation of conveying equipment
2-1. air conveying devices, 2-2. accumulators, 2-3. dissipate wind net, 2-4. chain types lifting conveying device.
Fig. 4 is that chain type lifting conveying device splits the structural representation after outer cover
2-41. supports, 2-42. drive sprockets, 2-43. support sprocket wheels, 2-44. chains, 2-45. conveying scraper plates, 2-46. are pre-
Annealing device, 2-47. outer covers, the track of 2-48. additive-adding devices.
Fig. 5 is the structural representation of pyrolysis furnace
41. support, 42. underdrive devices, 43. receipts slag pans, 44. lower blast pipes, 45. times interlayers, 46. Gas Pipes, 47.
Burner, 48. combustion chambers, 49. hot blast discharge pipes, 410. fuel-air mixture efferent ducts, 411. fixed gas escape pipes, on 412.
Cover, 413. charging axial brake devices, 414. charging axles, 415. taper feed bins, 416. feeding screws, 417. feeder outer covers,
418. upper cover plates, 419. flowlines, stock guide on 420., 421. one-level distributing devices, comb on 422., cylinder on 423., 424. two levels
Distributing device, 425. times combs, 426. times cylinders, 427. lower covers and slag-scraper, 428. main shafts, 429. dregs-separating devices, 430. vapor pipes,
431. outer swivel joints, 432. inward turning adapters, 433. times water inlet pipes, 434. times warm-air pipes, 435. bodies of heater.
Fig. 6 is the structural representation for neutralizing device
91. flue gas inlet pipe, 92 shells, 93. petticoat pipes, 94. blast pipes, 95. spray equipments, 96. chemical fertilizer stoste outlets.
Fig. 7 is the structural representation of condenser
8. condenser, 10. oil water separators, 81. first-stage condensers, 82. first-stage condenser shells, 83. first-stage condensers
Heat exchanger, 84. right air inlet pipe, 85. secondary condenser shells, 86. non-condensable gas exports, air inlet pipe in 87., 88. left air inlets
Pipe, 89. secondary condenser heat exchangers.
Fig. 8 is the structural representation of oil water separator
8. condenser, 101. outer shell of oil-water separator, 102. oil-outs, 103. sewage draining exits, 104. feed tubes, 105. water outlets
Mouthful, 106. catch trays.
Fig. 9 is the structural representation of main shaft
281. axis bodies, 282. axle beds, 283. vapor pipes, 284. enter warm-air pipe, 285. water inlet pipes, 286. baffle plates.
Embodiment
In order to further illustrate technical scheme, in conjunction with accompanying drawing, illustrate embodiment of the invention, such as
Fig. 1-8, frame 1-1 are used as from the general frame of the industry in this example, by frame 1-1 in Equipment Foundations, for propping up
Support and install whole functional part;Shell 1-2 is made from 1 millimeter of steel plate of thickness, shell 1-2 is arranged on frame 1-1;
From the general chain type conveyor belt of the industry as conveyer belt 1-3, by conveyer belt 1-3 installed in frame 1-1 one end, and with moving
Pending plastic garbage, can be sent at setting wheel 1-4 by power and control system connection from the charging aperture of sorting device;This example
Middle both ends set rotating shaft, and be connecteds with transmission device from main body of the hollow cylinder as setting wheel 1-4, by described group
Material wheel 1-4 is arranged on frame 1-1, and positioned at conveyer belt 1-3 top, and it is located at conveyer belt 1-3 afterbodys one end;In this example
Multiple switch-plates being hinged with setting wheel 1-4 are provided with setting wheel 1-4, are evenly arranged in setting wheel 1-4 excircle;Ensure
Setting wheel 1-4 direction of rotation is opposite with the direction of rotation of conveyer belt 1-3 afterbody drive sprockets;Hollow cylinder is selected in this example
Power transmission shaft is installed as separation wheel 1-5 main body, and at both ends, separation wheel 1-5 is arranged on frame 1-1, positioned at conveyer belt
The bottom of drawing-inroller 1-6 outside 1-3 afterbodys one end, power transmission shaft is connected with transmission device, ensures its direction of rotation and feeding
It is identical to take turns 1-6;Sorter is installed on separation wheel 1-6;Described sorter is platy structure;Uniformly it is covered with the excircle of separation wheel
Surface;Main body of the welded steel plate into cylinder type hollow body as drawing-inroller 1-6 is selected in this example, and installs and is driven at both ends
Axle, drawing-inroller 1-6 is arranged on frame 1-1, positioned at setting wheel 1-4 rear portion and separation wheel 1-5 top;On drawing-inroller
Feed appliance is set;Feed appliance is tabular, is uniformly covered with drawing-inroller 1-6 excircle;Also set up simultaneously in drawing-inroller 1-6 excircles
There is blower, blower is evenly arranged in drawing-inroller 1-6 excircle, and drawing-inroller 1-6 can produce tangential wind-force when rotating;Will
The power transmission shaft at drawing-inroller 1-6 both ends is connected the rotation side for ensureing drawing-inroller 1-6 direction of rotation with separation wheel 1-5 with transmission device
To identical, be so advantageous to when two-wheeled rotates, the delivery sheet and material selecting board of its excircle are interlaced, by plastic garbage
Fibre object or the larger plastic garbage of volume are cut short, torn up;From comb type frame as particle discharging opening 1-7 in this example, it is combed
Spacing distance is less than the minimum grain size of the conveying plastics of design;So ensure that dust and debris in small, broken bits can be from particle discharging opening 1-
Discharged in 7, and satisfactory plastics are not discharged;Particle discharging opening 1-7 is arranged on shell 1-2, positioned at separation wheel 1-5
Bottom;Stone discharging opening 1-8 is arranged on shell 1-2 as stone discharging opening 1-8 from self-weight reset formula baffle plate in this example
On, positioned at the rear of separation wheel and positioned at particle discharging opening 1-7 top;So when a kind of lightweight object of plastic flakes is encountered
During stone discharging opening 1-8, it will be stopped by stone discharging opening 1-8, when the weights such as stone, metal derby meet stone discharging opening 1-8
When, the gravity of striker plate can be overcome, and discharge outside shell 1-2;It is made to enter with air conveying device from thin-walled steel plate in this example
Plastics discharging opening 1-9 is arranged on shell 1-2, position by the section identical tubular article of material mouth matching as plastics discharging opening 1-9
In drawing-inroller 1-6 rear portion oblique upper, docked with the air conveying device entrance of conveying device, this completes pretreatment system 1
Sorting device implementation, in sorting device front end, from the chain type conveyor belt that the industry is general, and thereon install preheating remove
Wet device, is combined with sorting device, is formed pretreatment system 1.
The tubular of square-section is made in this example from thin-walled steel plate, as air conveying device 2-1, air conveying device 2-1 is pacified
Between plastic garbage sorting device and accumulator 2-2, the plastics discharging opening 1-9 of its charging aperture and plastic garbage sorting device
Connection, its discharging opening are connected with accumulator 2-2;In order to reduce the pressure and wind speed in accumulator 2-2, selected in this example and plastics
The sectional area that garbage sorting equipment connects one end is less than the sectional area that one end is connected with accumulator 2-2;Plastic wire is selected in this example
As scattered wind net 2-3, by scattered wind net 2-3 installed in the suitable for reading of accumulator 2-2, cover that whole accumulator 2-2 is suitable for reading and and storing
Device 2-2 is fixedly connected, and its mesh diameter is less than the particle diameter of plastic garbage, and can either so play the effect of scattered wind and have can prevent plastics
Fragment flies out;The tapered upper shed cavity body of chamfered edge is made from thin-walled steel plate in this example, as accumulator 2-2, is installed
In air conveying device discharge port end and chain type lifting conveying device feed inlet end;It is defeated from the general chain scraper of the industry in this example
Lifting device is sent as chain type lifting conveying device 2-4;Chain type lifting conveying device 2-4 one end is arranged on accumulator 2-3
Inside, the other end are connected with In Cracking Feedstock storehouse, from the frame conduct of the general chain scraper conveyer of the industry in this example
Support 2-41, by support 2-41 be arranged between accumulator 2-3 and pyrolysis furnace 4, respectively with accumulator 2-3 and pyrolysis furnace 4 branch
Support part part connection;From the general drive sprocket for meeting national standard of the industry respectively as drive sprocket 2-42 and support chain
2-43 is taken turns, drive sprocket 2-42 is arranged on support one end, is connected with the drive of the power set of conveying equipment;Driven in this example
Movable sprocket 2-42 has two, on same axle, and is located at support both sides, is so advantageous to keep two when load is heavier
Side is balanced in power, and avoids causing chain and scraper plate operating unstable;Support sprocket wheel 2-43 is arranged on support 2-41, in this example
Support sprocket wheel 2-43 has multiple, positioned at support 2-41 both sides, support 2-41 longitudinal side is evenly distributed on, with drive sprocket 2-
42 are located at the same level of support 2-41 both sides respectively;Chain has two in this example, is separately mounted to the drive of support 2-41 both sides
Movable sprocket 2-42 and support sprocket wheel 2-43 excircles structure in a ring;From the general conveying scraper plate of the industry as conveying scraper plate
2-45, between conveying scraper plate 2-45 is arranged on into two chains, its both ends is connected with the chain of both sides respectively;Conveying is scraped in this example
Plate 2-45 have it is multiple, it is parallel and be evenly arranged on ring chain, to ensure uniform load;From copper pipe as preheating in this example
Tube heater and blowing hot-air device in processing unit 2-46, the pre-heat treatment device 2-46 is arranged on inside outer cover 2-47 and leaned on
Nearly one end of pyrolysis furnace 4, and positioned at conveying scraper plate 2-45 top;Wherein heating tube is connected with the hot air duct of pyrolysis furnace 4, institute
Produce heat can heating of plastic rubbish, reduce water content when entering pyrolysis furnace 4;Blowing hot-air device is lifted installed in chain type
Conveying device 2-4 discharge port end, it is made up of multiple warm-air pipes, the air outlet alignment chain type lifting conveying device 2- of its warm-air pipe
Plastic garbage is heated to enter back into pyrolysis furnace feed bin after certain softening degree by 4 spout area, the hot blast of blowout;In this example
Outer cover 2-47 is made from thin-wall stainless steel plate bending, outer cover 2-47 is arranged on outside support 2-41, and support 2-47 is removed
In side outside both ends is wrapped in, so in order to avoid being that dust from flying causes production environment secondary in plastic garbage course of conveying
Pollution, while play insulation and the effect of safety;Track 2-48 of the square steel as additive-adding device is selected in this example, by it
Installed in support 2-41 both sides, it is connected, is made up of two parallel tracks, its track length with support 2-48 through outer cover 2-47
Identical with the support 2-41 length of chain type lifting conveying device, this completes the implementation of conveying equipment 2.
Described main shaft, it is characterised in that:Including axis body, axle bed, vapor pipe, enter warm-air pipe, water inlet pipe, baffle plate;Choosing
The commercially available stainless steel general by the use of the industry as axis body 281 material because axis body 281 is always in the state of temperature is higher
Work;The one end of axis body 281 closing one end open is formed into open cavity body, its open at one end is downward, in open at one end and axle bed
282 connections;Axle bed 282 is arranged on the open at one end of axis body 281, integrally manufactured axis body 281 and axle bed 282 are used in this example;Axle
Seat is equally hollow body, and the endoporus of its endoporus and axis body 281 matches;Peace is set on axle bed using the general method of the industry
Dress bearing and the structure being connected with transmission device;By steam pipe 283 be arranged on the internal cavities of axis body 281 in, its upper end away from
There is the distance of 10-100 millimeters at the off-axis inner cavity top closing of body 281,50 millimeters of distance is selected in this example, its lower end is passed through
Baffle plate 286, which stretches out outside axis body 281 and is upward through dregs-separating device 429 after bending, reaches the surface of dregs-separating device 429;By steam pipe 283
It is tightly connected with the junction of baffle plate 286;Warm-air pipe 284 will be entered on the baffle plate 286, and the fixed seal connection of baffle plate 286, its
Upper end is hanging, and lower end is connected with outer swivel joint 431, ensures to overlap with the axis of axle bed 282 into the center of warm-air pipe 284;Will
Water inlet pipe 285 is arranged on into warm-air pipe 284, and upper end is hanging, and lower end is connected with inward turning adapter 432;Set water inlet pipe 285
The upper end into warm-air pipe 284 is stretched out in upper end;Baffle plate 286 is arranged at the cavities open of the lower end of axle bed 282, with axle bed 282
It is tightly connected;3 steam pipes 283 are selected in this example, are evenly distributed on the circumference of the intracavity section of axis body 281, it is thus complete
Into the implementation of main shaft 428.
Add crossbearer to form support 41 from four general supporting legs of the industry in this example, support 41 is arranged on body of heater 435
Periphery bottom, for supporting and fixing body of heater, keep the stabilization of whole pyrolysis furnace 4;Filled in this example from Worm Wheel System
The bottom that body of heater 435 is disposed at as underdrive device 42 is put, main shaft 428 and receipts slag pan 43 can be driven to rotate;This example
The middle back taper cavity body from upper shed will receive slag pan 43 and be arranged on the bottom of body of heater 435, and be looped around as slag pan 43 is received
Around main shaft 428;The edge of slag pan 43 will be received slag notch is set, its slag notch is connected with building block extrusion equipment;From stainless steel
Lower blast pipe 44 is arranged on body of heater 435, connected with the place space of burner 47 as lower blast pipe 44 by pipe;By lower interlayer
45 are arranged on the inner chamber bottom of body of heater 435, and upper end is connected with the lower interlayer wall where burner 47, and is formed with the lower inwall of interlayer 45
Confined space;Gas Pipe 46 is arranged on body of heater 435, is connected through furnace body wall with burner 47;Fired in this example from coal gas
Burner 47 is arranged on the lower wall of combustion chamber 48 as burner 47, burning is extend into through the lower wall of combustion chamber 48 by burner
In room 48;On the periphery of burner 47, air inlet duct is set;Multiple burners 47 are selected in this example, are evenly distributed on the lower wall of combustion chamber 48
On, reach the effect of homogeneous heating;Combustion chamber 48 is arranged on the middle part of body of heater 435, is relatively closed space;Its lower wall and stove
Body 435 and lower interlayer 45 connect, and upper wall has certain intervals with lower wall, and end is connected with lower wall and body of heater;Ensure that combustion chamber 48 exists
The position of main shaft 428 is that have metric space with main shaft excircle;Hot blast discharge pipe 49 is arranged on outside body of heater 435, with burning
The inside of room 48 connects;Fuel-air mixture efferent duct 410 is arranged on body of heater 435, positioned at the upper top of stock guide 420;Setting oil
The position of gas mixture output tube 410 is higher than the position of flowline 419;Fixed gas escape pipe 411 is arranged on body of heater 435,
Near taper feed bin 415 and the binding site of body of heater 435;Upper cover 412 is arranged at the top of body of heater, is half from upper cover 412
Spherical hollow space body, bottom and the upper end airtight connection of body of heater 435;Side sets fan-shaped charging aperture in upper cover 412, with conveying equipment
2 discharging opening docking;From the general motor acceleration and deceleration device of the industry as charging axial brake device 413, charging axle is driven
Device 413 is arranged on the upper outside of upper cover 412, is connected with charging axle 414, charging axle 414 can be driven to rotate;By charging axle
414 are arranged between upper cover 412 and taper feed bin 415, can be rotated around own axes;Taper feed bin 415 is arranged on body of heater
435 top, selects shape of the back taper thin wall cavity body as taper feed bin 415, edge and 435 closed company of body of heater in its taper
Connect, circular open is arranged at bottom;Feeding screw 416 is arranged on to the lower end of charging axle 414, and under taper feed bin 415
At end opening, it is fixedly connected with charging axle 414;Ensure that feeding screw 416 matches with the internal diameter of feeder outer cover 417;It will enter
Glassware outer cover 417 is arranged on the lower end of taper feed bin 415, is set as tubular construction;By the upper end of feeder outer cover 417 and conical material
Storehouse 415 is fixedly connected, and its internal diameter rotates external diameter with feeding screw 416 and matched;In order to facilitate discharging, by feeder outer cover 417
Lower end sets enlarging;Upper cover plate 418 is arranged on to the lower end of taper feed bin 415, is umbrella shape, Open Side Down, its outward flange with it is upper
Stock guide 420 interlocks;Flowline 419 is set on body of heater 435, positioned at the top of upper stock guide 420, its height is mixed less than oil gas
Close the position of gas efferent duct 410;Upper stock guide 420 is arranged on the top of body of heater 435 and positioned at the top of combustion chamber 48, upper cover
412 bottom, its overhanging end interlock with upper cover 412;One-level distributing device 421 is arranged on the upper end of main shaft 428, one end is consolidated with main shaft
Fixed connection, the other end is hanging, is made up of polylith drapery panel, and all drapery panels are interlaced, arranged in flakey, its free end
There is certain interval with the inwall of combustion chamber 48;In order to which the convenient drapery panel by one-level distributing device 421 of blanking sets the angle tilted down
Degree;Upper comb 422 is arranged between the inwall of combustion chamber 48 and upper cylinder 423, selection is comb shape structure in this example, around upper cylinder 423
Arranged in radiation shape, network structure can also be used;Both ends are connected with the inwall of combustion chamber 48 and the outer wall of upper cylinder 423 respectively;This
It is tubular structure that upper cylinder 423 is selected in example, and its outer wall is fixedly connected with upper comb 422, and inside circumference is provided with supports main shaft 428
Axle bed, bearing is installed in axle bed, upper support and rotation for main shaft 428;Two level distributing device 424 is arranged on upper cylinder
423 lower ends, one end are connected with main shaft 428, and the other end is hanging, are arranged to polylith drapery panel composition, polylith drapery panel is mutually handed over
Mistake, arranged in flakey, its free end has certain interval with the inwall of combustion chamber 48, is easy to plastics to pass through;, will in order to facilitate blanking
The drapery panel of two level distributing device sets the angle tilted down;By it is lower comb 425 be arranged on the inwall of combustion chamber 48 and lower cylinder 426 it
Between, capital and interest selection is comb shape structure, and its both ends is connected with the inwall of combustion chamber 48 and the lower outer wall of cylinder 426 respectively;Lower cylinder 426 is set
In the upper bottom of cylinder 423, there is certain distance with upper cylinder 423, select tubular structure, its outer wall is fixedly connected with lower comb 425, for propping up
The lower cylinder 426 of support;Lower cover and slag-scraper 427 are arranged on main shaft 428, its slag-scraper and the lower inner wall of combustion chamber 48 are connect
Touch, its effect is to strike off the residue for being bonded in inwall;Main shaft 428 is arranged on underdrive seat, is arranged to hollow shaft, Neng Gou
Rotated under the drive of underdrive device 42;Water inlet pipe, warm-air pipe, vapor efferent duct are installed inside main shaft 428;By dregs-separating device
429 are arranged on main shaft 428, can be rotated with main shaft 428, be arranged to umbrella-shaped structure;Vapor pipe 430 is arranged on master
On axle 428, stretched out by the inside of main shaft 428 through dregs-separating device 429 to the upper surface of dregs-separating device 429, can be the upper of dregs-separating device 429
Surface provides vapor, so that vapor is combined generation water-gas with hot-engine sludge;Outer swivel joint 431 is arranged on bottom
On seat, one end is connected with the warm-air pipe in main shaft 428, and the other end is connected with lower warm-air pipe 434;By inward turning adapter
432 are arranged on inside outer swivel joint 431, and one end is connected with the water inlet pipe in main shaft 428, the other end and lower water inlet pipe
433 connections;Lower water inlet pipe 433 is arranged on inward turning adapter 432, lower warm-air pipe 434 is penetrated and is connected with water source;By lower hot blast
Pipe 424 is arranged on outer swivel joint 431, and one end is connected with outer swivel joint 431, and the other end is connected with heat air source;Selection
The general tubular structure of the industry is installed on support 41, upper end is connected with upper cover 412, and lower end hangs as body of heater 435
Sky, this completes the implementation of pyrolysis furnace 4.
Flue gas inlet pipe 91 is arranged on to the lower end of shell 92, lower end is connected with the combustion chamber installed in the bottom of shell 92, under
End middle part is connected with the fixed gas escape pipe of pyrolysis furnace 4, and the other end is stretched into inside shell 92;Shell 92 is arranged on combustion chamber
End, is confined air cavity positioned at the top of pyrolysis furnace 4;Petticoat pipe 93 is arranged on to the upper end of flue gas inlet pipe 91, is arranged to umbrella knot
Structure;Ensure that petticoat pipe 93 and the inwall of shell 92 have gap during installation, so that ejecting liquid flows down;The bottom of petticoat pipe 93 is entered with flue gas
Pipe 91 leaves gap between upper end, so that gas flows out;Blast pipe 94 is arranged on the top of shell 92, is set to tubular structure, one
End connects with the inside of shell 92, the other end and atmosphere;Spray equipment 95 is arranged in blast pipe, above petticoat pipe 93
There is certain distance with petticoat pipe 93, neutralising fluid can be sprayed to the space between petticoat pipe and blast pipe, in order to pernicious gas
Fully contact mixing;Chemical fertilizer stoste outlet 96 is arranged on to the bottom of shell 92, connected with the inner chamber of shell 92, so as to what is sprayed out
The chemical fertilizer stoste outflow that neutralising fluid is formed after being mixed with flue gas, this completes the implementation for neutralizing device 9.
First-stage condenser 81 is arranged on to the upper end of oil water separator 10, its lower end and the catch tray of oil water separator 10
106 connections suitable for reading;First-stage condenser shell 82 is arranged on to the upper end of oil water separator 10;By first-stage condenser heat exchanger 83
In first-stage condenser shell 82, handed in this example from the general tubing heat exchanger of the industry as first-stage condenser heat
Parallel operation 83, there is cooling liquid to pass through in first-stage condenser heat exchanger 83;Right air inlet pipe 84 is arranged on first-stage condenser shell
82 upper rights, one end connect with the outlet of the cracked gas of pyrolysis furnace 4, and the other end connects with the inner chamber of first-stage condenser shell 82;Will
Secondary condenser shell 85 is arranged on inside first-stage condenser 81, its underpart opening, upper periphery and first-stage condenser shell 82
Airtight connection;Non-condensable gas export 86 is arranged on secondary condenser shell 85, connected with the inner chamber of secondary condenser shell 85;
Middle air inlet pipe 87 is placed in the middle installed in the top of first-stage condenser shell 82, and one end connects with the outlet of the cracked gas of pyrolysis furnace 4, another
End connects with the inner chamber of first-stage condenser shell 82;Left air inlet pipe 88 is arranged on the upper left-hand of first-stage condenser shell 82, one end
Export and connect with the cracked gas of pyrolysis furnace 4, the other end connects with the inner chamber of first-stage condenser shell 82;By secondary condenser heat exchange
Device 89 is arranged on inside secondary condenser shell 85, is handed over from the general tubing heat exchanger of the industry as secondary condenser heat
Parallel operation 89, the interior circulation of secondary condenser heat exchanger 89 have cooling liquid, and secondary condenser shell 85 is handed over secondary condenser heat
Parallel operation 89 forms secondary condenser, and this completes the implementation of condenser 8.
Outer shell of oil-water separator peace 101 is mounted in the lower end of condenser 8, thin wall cavity body is arranged to, with condenser casing
82 connections;Oil-out 102 is arranged on outer shell of oil-water separator 101, connected with the inner chamber of outer shell of oil-water separator 101, is set
Position height of the position height on outer shell of oil-water separator 101 of oil-out 102 higher than the delivery port 105 of outlet pipe;Will
Sewage draining exit 103 is arranged on the bottom of outer shell of oil-water separator 101, and valve is installed thereon, regularly to discharge dirt;By feed liquor
Pipe 104 is arranged on the inner chamber of outer shell of oil-water separator 101, is set to tubulose, and upper end is connected with catch tray 106, and lower end is open;By water outlet
Mouth 105 is arranged on outer shell of oil-water separator 101, is connected by pipeline with the intracavity bottom of outer shell of oil-water separator 101, to take out
Remove the water in portion;The position height for setting delivery port is less than the position height of oil-out;Catch tray 106 is arranged on water-oil separating
The inner chamber of device shell 101, is arranged to back taper thin-walled hollow body, and its upper end connects with the first-stage condenser shell 82 on condenser 8
Connect, lower end is connected with feed tube 104, and this completes the implementation of oil water separator 10.
Pretreatment system 1 is arranged on to the charging aperture section of conveying equipment 2, is connected with conveying equipment 2;Conveying equipment 2 is pacified
Between pretreatment system 1 and dore furnace 3, its import is connected with pretreatment system 1, and its outlet is connected with dore furnace 4;Using
The general hoist engine of the industry pulls the mode of dolly to set additive-adding device 3, and allows it on conveying equipment 2 is arranged on
Track on run, by additive-adding device 3 be arranged on conveying equipment 2 on, its end is connected with dore furnace feeding warehouse;It will split
Solution stove is arranged on the discharging opening one end of conveying equipment 2, and its feeding warehouse is connected with conveying equipment 2 and additive-adding device 3, its outlet
Mouth is connected with conveyance conduit, and its slag notch is connected with building block production equipment 14;Will neutralize device 9 be arranged on pyrolysis furnace 4 top,
It is connected by pipeline with the feeding warehouse upper cover of pyrolysis furnace 4, and is connected with neutralization additive and water inlet pipe, its liquid fertilizer stoste goes out
Mouth is connected with liquid fertilizer storage device by pipeline;Using other general recovery systems of the industry as combustion gas recovery system
6, combustion gas recovery system 6 is arranged between condenser 8 and pyrolysis furnace 4, connected respectively with condenser 8 and pyrolysis furnace 4 by pipeline
It is logical;Described condenser 8 is arranged on the side of pyrolysis furnace 4, is connected by pipeline with the gas outlet duct of pyrolysis furnace 4;By oil
Separator 10 is arranged on the bottom of condenser 8, and its outlet is connected with oily output channel and water delivery pipe road respectively;Using the industry
General building block production equipment is as building block production equipment 14, by building block production equipment 14 installed in the side of pyrolysis furnace 4, with splitting
Solve the slag notch linking of stove 4;Using the general oil tank of the industry as storage of oils equipment, storage of oils equipment is arranged on oil
The side of separator, connected by the oil-out of pipeline and oil water separator, just complete the reality of plastic garbage processing system
Apply.
Using when, the plastic garbage gathered is sent into plastic garbage pretreatment system 1, sent after prebake and sorting
Enter conveying equipment 2, conveying equipment 2 is heated to the plastic garbage of outlet again, and pyrolysis furnace is then entered together with additive
4;The additive used in this example mainly includes lime, hollow alumina, molecular sieve, used oil, primarily serves neutralization and fixed line
Hydrogen chloride and sulfur dioxide gas, prevent from that equipment is caused to corrode and lubricated and catalytic action;Normal pressure is carried out in pyrolysis furnace 4
Anaerobic continuous cracking;Gas caused by pyrolysis furnace 4 is liquefied by condenser 8, the oil water mixture after liquefaction enters oil
Separator 10, not liquefied gas come back to pyrolysis furnace 4 into combustion gas recovery system 6 and are used as fuel;In the bottom of pyrolysis furnace 4
Slagging is slagged tap using immersion type, to ensure that the internal cleavage room of pyrolysis furnace 4 does not have air exchange with extraneous;Into oil water separator
10 liquid mixture, recycled respectively through oil-out and delivery port into pond and oil tank by separating, by neutralizing
The hydrogen chloride and sulfur dioxide of device 9 neutralize by liquid, using ammoniacal liquor and additive as neutralising fluid in this example, after neutralization
Multicomponent liquid fertilizer stoste is generated, is applied to crops for manufacture chemical fertilizer or small range after storage.
Cracked as a result of anaerobic, reduce the generation of toxic gas;As a result of multi-step temperature section, that is, three
Level cloth, can adapt to the cracking of the plastic garbage of unlike material will not produce because stove caused by cracking temperature difference explodes
With the accident for bonding body of heater;As a result of immersion type deslagging, the secondary pollution to environment is avoided;Returned as a result of combustion gas
Receive and utilize, save the energy;Slag is drenched as a result of vapor, and has slag scraper continuously to work, reduces deslagging, produces more
Water-gas, and avoid body of heater bonding;As a result of continuous cracking, the air pollution of too many levels is avoided;As a result of
Conventional cracking, avoid because hypertonia produces pyrolysis furnace Explosion of boiler proper;Produce, recycled solid as a result of building block
Body waste material, reduces secondary pollution;As a result of device is neutralized, reduce toxic gas discharge, while produce fluidization
Fertilizer;Therefore this method has efficiency high, and environmental pollution is small, and salvage value is high.
One embodiment of the present invention simply is listed in the present embodiment, does not represent all technical sides of the present invention
Case, any deformation done on this basis, it is considered as invading technical scheme.
Claims (2)
1. a kind of plastic garbage conveying equipment, suitable for a kind of plastic garbage processing system, described plastic garbage processing system,
Including pretreatment system, conveying equipment, additive-adding device, pyrolysis furnace, device, combustion gas recovery system, condenser, oil are neutralized
Separator, building block production equipment, storage of oils device;It is characterized in that:It is defeated including air conveying device, accumulator, chain type lifting
Send device;Described air conveying device is arranged between plastic garbage sorting device and accumulator, its charging aperture and plastic garbage point
The discharging opening connection of equipment is picked, its discharging opening is connected with accumulator;Including feeding channel, wind net is dissipated;Described feeding channel peace
It is tubular structure between the discharging opening and accumulator of plastic garbage sorting device;Described scattered wind net is arranged on accumulator
It is suitable for reading, it is suitable for reading to cover whole accumulator;Described scattered wind net is network structure, and its mesh diameter is less than the grain of plastic garbage
Footpath;Described accumulator is arranged on the discharge port end of air conveying device, is the cavity body of open topped;Described chain type lifting conveying
Device one end is arranged on internal hopper, and the other end is connected with In Cracking Feedstock storehouse.
A kind of 2. plastic garbage conveying equipment according to claim 1, it is characterised in that:Described feeding channel and plastics
The sectional area that garbage sorting equipment connects one end is less than the sectional area that one end is connected with accumulator.
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CN201720722872.8U CN206838753U (en) | 2017-06-21 | 2017-06-21 | A kind of plastic garbage conveying equipment |
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Application Number | Priority Date | Filing Date | Title |
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CN201720722872.8U CN206838753U (en) | 2017-06-21 | 2017-06-21 | A kind of plastic garbage conveying equipment |
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ID=60801503
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CN201720722872.8U Expired - Fee Related CN206838753U (en) | 2017-06-21 | 2017-06-21 | A kind of plastic garbage conveying equipment |
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