CN206109302U - Unit is handled in innoxious dry distillation of municipal solid waste decrement - Google Patents
Unit is handled in innoxious dry distillation of municipal solid waste decrement Download PDFInfo
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- CN206109302U CN206109302U CN201621135423.5U CN201621135423U CN206109302U CN 206109302 U CN206109302 U CN 206109302U CN 201621135423 U CN201621135423 U CN 201621135423U CN 206109302 U CN206109302 U CN 206109302U
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Abstract
The utility model provides an unit is handled in innoxious dry distillation of municipal solid waste decrement, including at least one hot drying dehydration stove in advance, an at least retort house and a gas -liquid separation system, hot drying dehydration stove charge door sets up feed hopper through first high temperature rotary seal feed valve in advance, set up compulsory feeding device in the feed hopper, it pushes away the material main shaft to set up the spiral in the hot drying dehydration stove in advance, the retort house charge door is connected through second high temperature rotary seal feed valve to the discharge gate of hot drying dehydration stove in advance, set up retort house spiral pay -off subassembly in the retort house, the retort house outside sets up firstly, two intermediate frequency heating units, the charcoal export is connected through third high temperature rotary seal feed valve in the retort house bottom, it generates gas access and first pyrolysis formation gas outlet to set up first pyrolysis in advance on the hot drying dehydration stove, first pyrolysis generates the second pyrolysis formation gas outlet that retort house is connected to the gas access, and the second pyrolysis that first pyrolysis generated gas outlet connection gas -liquid separation system generates the gas access, gas -liquid separation system tail gas supplies gas turbine generator to compile and publish.
Description
Technical field
This utility model is related to domestic garbage disposer, and in particular to a kind of under isolation air conditionses, will life rubbish
Rubbish pyrolytic gasification dry distilling, it is to avoid garbage disposal produces the innoxious dry distilling datatron of application of city life garbage of the harmful substances such as bioxin
Group.
Background technology
At present, with global industry, Development of Urbanization, the change of people's lives mode and being continuously increased for population, rubbish
Rubbish process is increasingly becoming stubborn problem.The masses are day by day strong for the cry of domestic garbage was harmlessly treated, particularly domestic
Categorized consumer waste it is lack of standardization, more increase the treating capacity of house refuse, domestic rubbish disposal has become and is essential
A big livelihood issues to be solved.Domestic rubbish disposal both at home and abroad at present mainly has sanitary landfills, system（Heap）The sides such as fertilizer, burning
Method.
The current major part rubbish of China takes the mode of burning and burying, and only rural area is on a small quantity using system（Heap）Fertilizer, production natural pond
All there is secondary pollution in other processing modes such as vapour, these processing modes：Garbage loading embeading, although put than not filling and huddling
Improve, investment and operating cost are also low than burning, but exist long-term and be continuously increased land occupation, long-term pollution subsoil water
The problems such as with affecting the gases such as ambient air environment, generation alkanes to cause spontaneous combustion generation dioxin to endanger；Waste incineration, although
Volume reduction decrement and harmless treatment and to account for the aspects such as soil less more advantageous than landfill, but have that investment is big, operating cost is high, difficult
Effectively to contain the problems such as dioxin, waste gas discharge are big, heat utilization is low, comprehensive utilization is poor；System（Heap）Fertilizer, raw producing firedamp gas etc. other
Mode, though having carried out a certain degree of utilization to the Organic substance in rubbish, can not process not putrescible Organic substance and inorganic
Thing, thus garbage disposal minimizing is not high, innoxious not thorough（The hazardous materials such as waste gas, waste water, waste residue, waste plastics fail thoroughly
Solve, easily cause secondary pollution）, recycling it is poor.
Utility model content
The technical problems to be solved in the utility model is, for effectively containment is difficult to present in application of city life garbage process
Dioxin and waste water, waste residue, harmful gass etc. pollute, and garbage disposal minimizing is inadequate, recycling is poor, innoxious
Not thoroughly the problems such as, there is provided one kind can carry out cracking gasification process to house refuse under isolation air conditionses, effectively contain two
The innoxious dry distilling of application of city life garbage for disliking English processes unit.
To solve above-mentioned technical problem, the technical solution adopted in the utility model is：A kind of application of city life garbage decrement without
Evilization dry distilling processes unit, including at least one preheating and drying dehydration furnace, at least one dry distilling room and a set of Separate System of Water-jet.
Charge door Jing the first high temperature expansion bellows of the preheating and drying dehydration furnace, the first High Temperature Rotating sealing feed valve are provided with and add
Funnel, be provided with charging hopper with screw rod push pressure feeding device, be provided with the preheating and drying dehydration furnace by
The spiral pusher main shaft of heat-resisting steel making, the first Y types resilient bearing of the discharging opening order Jing sealing of the preheating and drying dehydration furnace
Cover for seat, the second high temperature expansion bellow, the second High Temperature Rotating sealing feed valve connect the charge door of the dry distilling room, the dry distilling
Indoor setting dry distilling room screw feeding component, arranges first and second heating in medium frequency unit on the outside of the middle part of the dry distilling room, described dry
Evaporate the 2nd Y type resilient bearing sealed socket sleeves of bottom Jing order Jing of room, third high temperature expansion bellow, third high temperature rotation close
Envelope feed valve connection charcoal outlet.The outside of the shell of the preheating and drying dehydration furnace arranges thermostat layer, and the bottom of thermostat layer is arranged
First pyrolysis generates gas access, and the top of thermostat layer arranges the first pyrolysis and generates gas outlet, makes thermostat layer and preheating and drying
Pyrolysis is formed between the shell of dehydration furnace and generates gas passage.First pyrolysis generates gas access and connects the dry distilling room
Second pyrolysis generates gas outlet, and first pyrolysis generates the second pyrolysis life that gas outlet connects the Separate System of Water-jet
Into gas access.The afterbody order of the Separate System of Water-jet arranges air compressor, combustion gas storage tank, the combustion gas storage tank
Connection jet dynamic control.
The preheating and drying dehydration furnace, dry distilling room and Separate System of Water-jet are divided into three floors in workshop, and described pre-
Heated drying dehydration furnace is horizontally placed on top layer flooring, and the dry distilling room Jing housings support slide assemblies to be vertically arranged at middle building
Layer, makes the preheating and drying dehydration furnace arrange in inverted L shape with dry distilling room, and the Separate System of Water-jet is horizontally placed on bottom flooring
On.
The housing supports slide assemblies to include supporting slip by outer and interior the first housing located at top layer flooring installation place
Component, the second housing support slide assemblies and the 3rd housing located at middle level flooring installation place to support slide assemblies, and second shell
Body supports slide assemblies and the 3rd housing to support on the inside of slide assemblies and is provided with sliding bearing, and the lower case Jing bullets of dry distilling room
Property support base be fixed on the flooring of middle level, to eliminate because high temperature causes the stretcher strain of dry distilling chamber enclosure, realize float support
It is fixed.
The spiral pusher main shaft warp beam is held and is installed between the drive end bearing bracket and rear end cap of preheating and drying dehydration furnace, and front end
Lid Jing bolts are fixed on the cylinder of preheating and drying dehydration furnace, and preheating and drying dehydration furnace is stretched out in the front end of spiral pusher main shaft, and
Bearing fixed seat Jing preheating and drying dehydration furnace is placed on supports and pusher motor is connected to after fixing, and bearing fixed seat and pusher are electric
Machine is all fixedly installed on vehicle frame.Occur wearing and tearing or need to change when spiral pusher main shaft works long hours, unclamp positioned at front
The clamping screw of end cap, can move spiral pusher main shaft opposite direction by promoting vehicle frame, and spiral pusher main shaft is extensible pre-
Heated drying dehydration furnace, facilitates the Maintenance and Repair of preheating and drying dehydration furnace.
Dry gas relief valve and othermohygrometer detector unit, and othermohygrometer are provided with the preheating and drying dehydration furnace
The control end that detector unit seals feed valve with first High Temperature Rotating is connected；The top of the dry distilling room is provided with neutron material
Position meter, the bottom of the dry distilling room are provided with charcoal detector, neutron material-level meter and charcoal detector respectively with dry distilling room control system
Connection, the outfan of dry distilling room control system connect the control end that second and third High Temperature Rotating seals feed valve.
The outside of the first and second heating in medium frequency unit arranges heat-insulation layer.
The neighbouring setting water mist sprinkling dust-cleaning and refrigerating mechanism of the charcoal outlet.
The preheating and drying dehydration furnace and dry distilling room are respectively multiple, and the first pyrolysis life of all preheating and drying dehydration furnaces
The second pyrolysis for connecting the Separate System of Water-jet into gas outlet Jing gases integrator generates gas access.
The outfan connection utility network of the jet dynamic control.
The innoxious dry distilling of outfan connection application of city life garbage of the jet dynamic control processes the feeder ear of unit.
During utility model works, the rubbish of sorted crushing enters charging hopper, in the pressure charging pushed with screw rod
Device is forced under feeding, and the first High Temperature Rotatings of Jing sealing feed valve periodically enters preheating and drying dehydration furnace, preheating and drying dehydration
Spiral pusher main shaft in stove continues pusher and rubbish is pressurizeed, to exclude the residual air in rubbish, when quantity of refuse reaches one
Fixed number amount, the pressure that the propulsion of spiral pusher main shaft is produced reach and put on the second High Temperature Rotating sealing feed valve blade of end
Pressure transducer pressure value set in advance when, the second High Temperature Rotating sealing feed valve start working and push toward dry distilling room it is fixed
Amount rubbish material, the rubbish realized into dry distilling room are remained without air, are that subsequent high temperature dry distilling realizes that Domestic waste anaerobic is cracked,
Avoid producing the harmful gass such as dioxin.Rubbish of the first and second heating in medium frequency unit arranged outside dry distilling room persistently to entering adds
Heat so as to carbonization, generation pyrolysis gas.The steam that dry distilling room is pyrolyzed out enters preheating and drying dehydration furnace, is preheating and drying dehydration
The rubbish material of stove carries out heating, drying, vapor of generation etc. and sends into Separate System of Water-jet, the gas Jing Jing after gas-liquid separation
Jet dynamic control is entered after air compressor process.
Compared with prior art, this utility model has following beneficial effects：
1st, this utility model is respectively provided with Y type elastic shafts in the discharging opening of preheating and drying dehydration furnace, the discharging opening of dry distilling room
Sealed socket sleeve is held, while the discharging opening in the bottom of charging hopper, the discharging opening of preheating and drying dehydration furnace, dry distilling room is respectively provided with
High temperature expansion bellow, thus can eliminate because the high temperature that continuous heating is produced prolongs to preheating and drying dehydration furnace and dry distilling room housing
The impact of deformation is stretched, in addition, dry distilling room supports slide assemblies to be installed in top layer flooring and middle level flooring by the housing with bearing
Between, can further avoid impact of the continuous heating to dry distilling room housing in the vertical direction.
2nd, preheating and drying dehydration furnace is vertically arranged by this utility model, can make being heated everywhere for preheating and drying dehydration furnace
It is even, reduce the dry distilling room failure that high temperature causes the deformation of dry distilling room to cause as far as possible.
3rd, dry distilling room of the present utility model machine is entered to the material in dry distilling room using the mode of heating of intermediate frequency or resistance wire type
Row heating, while the heat-insulation layer that liner is made for fireclay insulating refractory is designed outside the housing of dry distilling room, in dry distilling room end
Discharging epistome is designed with water jacket, for carrying out cooling process to the solids after carbonization, after preventing cracking gasification
Product adheres to dry distilling room casing.
4th, this utility model spiral pusher main shaft pushes material under the driving of drive mechanism, persistently, only when positioned at spiral
Pressure transducer on the second High Temperature Rotating sealing feed valve blade of pusher main shaft end reaches pressure value set in advance, the
Two High Temperature Rotatings sealing feed valve is just started working and quantitative rubbish material is pushed toward in dry distilling room, so both can guarantee that dry distilling room
The abundant carbonization of interior material, and the sealing to dry distilling room charging aperture can be realized.
5th, the dry distilling room screw feeding component arranged in dry distilling room of the present utility model can ensure that rubbish material is done as far as possible
The adequacy for evaporating, and the loosening rubbish material during screw propulsion, it is to avoid the accumulation of rubbish material.
6th, this utility model uses for reference the production technology of gas generator, the Pintsch process gas produced using rubbish carbonization
The waste heat of body carries out drying preheating to the rubbish material in preheating and drying dehydration furnace, and the gas Jing gas-liquids point of generation are pyrolyzed after circulation
Carry out, after the process of the gas-liquids such as oil-water separation, the compression of fuel gas Jing air compressors being stored in gas storage tank from system,
Generate electricity for gas electricity generator, the electric energy of generation can generate electricity by way of merging two or more grid systems, and also be available for first and second heating in medium frequency unit of dry distilling room to dry distilling
Room carries out external heat, realizes fully recycling for heat energy, realizes the innoxious of rubbish, minimizing, recycling treatment, from
Garbage disposal cost is effectively reduced substantially.
Description of the drawings
Structural representations of the Fig. 1 for one embodiment of this utility model.
Life refuse processing method flow charts of the Fig. 2 for this utility model embodiment.
In figure：1-pressure the feeding device with screw rod push, 2-charging hopper, the 3-the first High Temperature Rotating sealing feed
Valve, the 4-the first high temperature expansion bellow, 5-pusher motor, 6-bearing fixed seat, 7-drive end bearing bracket, 8-vehicle frame, 9-spiral
Pusher main shaft, 10-spiral pusher blade, 11-preheating and drying dehydration stove outer covering, 12-preheating and drying dehydration furnace, 13-preheating
Drying and dehydrating stove support base, 14-thermostat layer, the 15-the first pyrolysis generate gas access, and the 16-the first pyrolysis generates gas and goes out
Mouthful, 17-othermohygrometer detector unit, 18-dry gas relief valve, 19-rear end cap, the 20-the one Y type resilient bearings are close
Envelope cover for seat, the 21-the second high temperature expansion bellow, the 22-the second High Temperature Rotating seal feeding valve, 23-dry distilling motor, 24-dry
Evaporate room spiral pushing motor bearing fixed seat, the 25-the first pyrolysis generates gas outlet, 26-dry distilling room, 27-the first
Housing supports slide assemblies, the 28-the second housing to support slide assemblies, 29-sliding bearing, 30-neutron material-level meter, 301-charcoal
Detector, the 31-the first heating in medium frequency unit, the 311-the first heating in medium frequency controller, 32-dry distilling room screw feeding component,
33-the second heating in medium frequency unit, the 331-the second heating in medium frequency controller, 34-heat-insulation layer, the 35-the three housing are supported and are slided
Component, the 36-the two Y type resilient bearing sealed socket sleeves, 37-elastic supporting seat, 38-third high temperature expansion bellow, 39-
Water jacket, 40-water jacket entrance, the outlet of 41-water jacket, 42-third high temperature rotary sealing material-feeding valve, the outlet of 43-charcoal, 44-water smoke
Spraying and dedusting chiller, 45-cooling pond, 46-Separate System of Water-jet, the 460-the second pyrolysis generate gas access,
461-gas-liquid dust cyclone separator, 462～466-gas-liquid separation tower, 467-air compressor, 468-combustion gas storage
Tank, 47-jet dynamic control, 48-dry distilling room control system.
Specific embodiment
Content of the present utility model is further described with specific embodiment below in conjunction with the accompanying drawings, to help understanding originally
The content of utility model.
Referring to Fig. 1, one embodiment of this utility model includes preheating and drying stove 12, dry distilling room 26 and the gas for being divided into three floors
Liquid separation system 46.Charge door Jing the first high temperature expansion bellows 4 of preheating and drying stove 12, the first High Temperature Rotating sealing feed valve
3 are provided with charging hopper 2, and the pressure feeding device 1 pushed with screw rod is provided with charging hopper 2.Preheating and drying dehydration furnace 12
It is horizontally placed on top layer flooring.The front end Jing bolts of preheating and drying dehydration furnace 12 are fixedly installed drive end bearing bracket 7, and rear end is fixed and set
End cap 19 is postponed, forward and backward end cap 7,19 realizes the front and back ends sealing of preheating and drying dehydration furnace 12.One spiral pusher main shaft, 9 Jing
Bearing is installed between drive end bearing bracket 7 and rear end cap 19, and preheating and drying dehydration furnace 12 is stretched out in the front end of spiral pusher main shaft 9, and
Bearing fixed seat 6 Jing preheating and drying dehydration furnace 12 is placed on is supported after fixing and is connected to pusher motor 5.6 He of bearing fixed seat
Pusher motor 5 is fixed on vehicle frame 8, so, when occurring the situation such as stuck in preheating and drying dehydration furnace 12, can be solid by removing
Determine the bolt of drive end bearing bracket 7, and the spiral pusher main shaft 9 that pusher motor 5 is connected by Jing vehicle frames 8 is overall from preheating and drying dehydration furnace 12
Interior extraction, facilitates repair and maintenance.Multigroup thermal conductive metal plate is evenly equipped with preheating and drying dehydration stove outer covering 11, it is ensured that preheating and drying takes off
Rubbish in water stove 12 is heated evenly.The outside of preheating and drying dehydration stove outer covering 11 arranges thermostat layer 14, the bottom of thermostat layer 14
First pyrolysis is set and generates gas access 15, the top of thermostat layer 14 arranges the first pyrolysis and generates gas outlet 16, makes thermostat layer
Pyrolysis is formed between 14 and preheating and drying dehydration stove outer covering 11 and generates gas passage.On the thermostat layer 14 of preheating and drying dehydration furnace 12
It is provided with dry gas relief valve 18 and othermohygrometer detector unit 17, and othermohygrometer detector unit 17 and the first High Temperature Rotating
The control end connection of sealing feed valve 3, with according to the situation adjustment charging rate in preheating and drying dehydration furnace 12.
The first Y type resilient bearing sealed socket sleeves 20 of rear end discharging opening order Jing of preheating and drying dehydration furnace 12, the second high temperature
Expansion bellow 21, the feeding mouth of the connection dry distilling of the second High Temperature Rotating seal feeding valve 22 room 26.26 the first housings of Jing of dry distilling room
Slide assemblies 27, the second housing is supported to support slide assemblies 28 and the 3rd housing to support slide assemblies 35 to be vertically arranged at top floor
Between face and middle level flooring, and the second housing supports slide assemblies 28 and the 3rd housing to support the inner side of slide assemblies 35 to be provided with cunning
Dynamic bearing 29, when not only making dry distilling room 26 be heated, all directions can occur impartial deformation, and vertical direction extensional is occurring
When, can adjust automatically installation site.Dry distilling room 26 and 12 L-shaped arrangement of preheating and drying dehydration furnace.Housing supports slide assemblies 35
Including the dry distilling room screw feeding component 32 for arranging in dry distilling room 26 that Jing dry distilling motor 23 drives, and the first heating in medium frequency unit
31st, the second heating in medium frequency unit 33, is arranged on the outside of the first heating in medium frequency unit 31 of dry distilling room 26, the second heating in medium frequency unit 33
Heat-insulation layer 34.Neutron material-level meter 30 is set on the top dry distilling room 26 of heat-insulation layer 34, is set on the bottom dry distilling room 26 of heat-insulation layer 34
Charcoal detector 301 is put, neutron material-level meter 30 and charcoal detector 301 are connected with dry distilling room control system 48 respectively, the control of dry distilling room
The outfan of system 48 connects the control end of second and third High Temperature Rotating sealing material discharging valve 22,42.The bottom second of dry distilling room 26
Y type resilient bearings sealed socket sleeve 36, third high temperature expansion bellow 38, the connection charcoal of third high temperature rotatory sealing outlet valve 42 go out
Mouth arranges water jacket on the conveying pipeline between 43, and third high temperature expansion bellow 38 and third high temperature rotatory sealing outlet valve 42
39.The neighbouring setting water mist sprinkling dust-cleaning and refrigerating mechanism 44 of charcoal outlet 43, to carry out dedusting cooling to the charcoal that charcoal outlet 43 is sent.
The top of dry distilling room 26 arranges the second pyrolysis and generates gas outlet 25, and the second pyrolysis generates gas outlet 25 and connects
First pyrolysis of preheating and drying dehydration furnace 12 generates gas access 15, to recycle to the pyrolysis gas that dry distilling room 26 produces.
First pyrolysis of preheating and drying dehydration furnace 12 generates the second pyrolysis of the connection Separate System of Water-jet 46 of gas outlet 16 and generates gas
Entrance 460.
Separate System of Water-jet 46 is on bottom flooring, and the afterbody order of Separate System of Water-jet 46 arranges air compressor
467th, combustion gas storage tank 468, the air taking port connection jet dynamic control 47 of combustion gas storage tank 468.Jet dynamic control 47 it is defeated
Go out end connection utility network, or the power end of first and second heating in medium frequency unit 31,33 of connection.
In the embodiment shown in fig. 1, preheating and drying dehydration furnace 12 and dry distilling room 26 are independent one group, but this practicality is new
Type is not limited thereto, and preheating and drying dehydration furnace 12 and dry distilling room 26 are alternatively multigroup, and the of multigroup preheating and drying dehydration furnace 12
One pyrolysis generates the second pyrolysis generation gas access 460 that 16 Jing gas integrators of gas outlet are connected to Separate System of Water-jet 6.
When this utility model is used, first house refuse is sorted, rejected building waste and metal, while comprehensive examine
Consider the thermal energy conversion efficiency of heating in medium frequency, will be the garbage crushing after sorting stand-by.
Rubbish after sorting is crushed is sent into from charging hopper 2, while the pressure charging pushed in self gravitation and with screw rod
The screw rod of device 1 pushes lower into the first High Temperature Rotating seal feeding valve 3.First High Temperature Rotating seal feeding valve, 3 periodicity Jing
Rubbish is sent into preheating and drying dehydration furnace 12 by the first high temperature expansion bellow 4.The pusher motor 5 of preheating and drying dehydration furnace 12 drives
Spiral pusher main shaft 9 is rotated, using the 10 continuous pressing waste material of helical blade on spiral pusher main shaft 9, to exclude entrance
Air in the rubbish material of preheating and drying dehydration furnace 12.It is when preheating and drying dehydration furnace 12 is used, single according to othermohygrometer detection
The operating of the detection numerical control pusher motor 5 of unit 17, to ensure that rubbish material has appropriate mass dryness fraction, it is to avoid spontaneous combustion occurs and produces
Raw harmful gass, while according to detection the second High Temperature Rotating of numerical control seal feeding valve 22 of othermohygrometer detector unit 17
Setting pressure, to adjust the feed rate of dry distilling room 26.Multigroup thermal conductive metal plate is evenly equipped with preheating and drying dehydration stove outer covering 11,
Ensure that the rubbish in preheating and drying dehydration furnace 12 is heated evenly, while slowing down the first pyrolysis generates the high temperature that gas access 15 enters
The flowing velocity of pyrolysis gas.Preheating and drying dehydration furnace 12 is controlled by dry gas relief valve 18 because of the vapor that high-temperature baking is produced
System, after beyond safety value, dry gas relief valve 18 is automatically opened up and is lost heart to safety value, while spiral pusher main shaft 9 is continuous
Compressed garbage, excludes the residual air in rubbish, when quantity of refuse reaches certain amount, the pressure that the propulsion of spiral pusher main shaft 9 is produced
Power reaches the preset pressure value of the second High Temperature Rotating seal feeding valve 22, and the second High Temperature Rotating seal feeding valve 22 is started working simultaneously
Quantitative rubbish material is pushed toward dry distilling room 26.The continuous agitation material of dry distilling room screw feeding component 32, makes material in first and second
Anaerobic dry distilling, uniform carbonization are carried out under the collaboration heating of frequency heating unit 31,33.The top of dry distilling room 26 arranges neutron material-level meter
30, bottom arranges charcoal detector 301, and neutron material-level meter 30 and charcoal detector 301 are connected with dry distilling room control system 48 respectively, are done
The outfan for evaporating room control system 48 connects the control end of second and third High Temperature Rotating sealing material discharging valve 22,42, so as to can be according to dry
The height of materials and carbonization degree for evaporating room 26 controls charging or the feeding speed of second and third High Temperature Rotating sealing material discharging valve 22,42.It is dry
Evaporate the pyrolysis of room 26 and the first pyrolysis of gas waste-heat Jing generation gas access 15 is generated into preheating and drying dehydration furnace 12, be preheating and drying
The rubbish material of dehydration furnace 12 carries out heating, drying, carries out gas-liquid separation subsequently into Separate System of Water-jet 46, tail gas afterwards
Gas storage tank 468 is entered Jing after air compressor 467 compresses, jet dynamic control 47 is re-fed into afterwards and is generated electricity.Due to preheating
Vapor that drying and dehydrating stove 12 is produced etc. is discharged by dry gas relief valve 18, and the second High Temperature Rotating seal feeding valve 22 exists
Just start quantitatively to convey when reaching preset pressure material to dry distilling room 26, thus the rubbish into dry distilling room 26 remained without air,
Domestic waste anaerobic cracking is realized for follow-up intermediate frequency high-temperature retorting, it is to avoid the harmful gass such as generation bioxin.
A Y type resilient bearings sealed socket sleeve 20 and preheating and drying dehydration furnace that 12 rear end of preheating and drying dehydration furnace is arranged
12 drive end bearing bracket 7 realizes combination sealing, it is ensured that the sealing of whole preheating and drying dehydration furnace.
It is installed at the second High Temperature Rotating sealing material discharging valve 22 and preheating and drying dehydration furnace feeding mouth at dry distilling chamber inlet
The combination of the first High Temperature Rotating sealing material discharging valve 3 realize the closed of preheating and drying dehydration furnace, it is to avoid outside air is entered affects dry
Evaporate effect.
Claims (10)
1. the innoxious dry distilling of a kind of application of city life garbage decrement processes unit, including at least one preheating and drying dehydration furnace（12）、
At least one dry distilling room（26）With a set of Separate System of Water-jet（46）, it is characterised in that：The charging of the preheating and drying dehydration furnace
Mouth Jing the first high temperature expansion bellows（4）, the first High Temperature Rotating sealing feed valve（3）It is provided with charging hopper（2）, charging hopper
The pressure feeding device pushed with screw rod is provided with inside（1）, in the preheating and drying dehydration furnace, it is provided with spiral pusher main shaft
（9）, the first Y type resilient bearing sealed socket sleeves of discharging opening order Jing of the preheating and drying dehydration furnace（20）, the second high temperature ripple
Expansion joint（21）, the second High Temperature Rotating sealing feed valve（22）Connect the dry distilling room（26）Charge door, the dry distilling room
（26）Interior setting dry distilling room screw feeding component（32）, the dry distilling room（26）Middle part on the outside of first and second heating in medium frequency is set
Unit（31、33）, the dry distilling room（26）The 2nd Y type resilient bearing sealed socket sleeves of bottom Jing order Jing（36）, third high temperature
Expansion bellow（38）, third high temperature rotary sealing feeding valve（42）Connection charcoal outlet（43）；The preheating and drying dehydration furnace
Shell（11）Outside arrange thermostat layer（14）, thermostat layer（14）Bottom arrange first pyrolysis generate gas access（15）, it is permanent
The top of warm layer arranges the first pyrolysis and generates gas outlet (16), makes to be formed between the shell of thermostat layer and preheating and drying dehydration furnace
Pyrolysis generates gas passage；First pyrolysis generates gas access（15）The second pyrolysis for connecting the dry distilling room generates gas
Outlet (25), first pyrolysis generate gas outlet (16) and connect the Separate System of Water-jet（46）Second pyrolysis generate gas
Body entrance（460）；The Separate System of Water-jet（46）Afterbody order arrange air compressor（467）, combustion gas storage tank
（468）, the combustion gas storage tank（468）Connection jet dynamic control（47）.
2. the innoxious dry distilling of a kind of application of city life garbage decrement according to claim 1 processes unit, it is characterised in that：Institute
State preheating and drying dehydration furnace（12）, dry distilling room（26）And Separate System of Water-jet（46）It is divided into three floors in workshop, wherein institute
State preheating and drying dehydration furnace（12）It is horizontally placed on top layer flooring, the dry distilling room（26）Jing housings support slide assemblies vertical
It is arranged between top layer flooring and middle level flooring, makes the preheating and drying dehydration furnace（12）With dry distilling room（26）Arrange in inverted L shape,
The Separate System of Water-jet（46）It is horizontally placed on bottom flooring.
3. the innoxious dry distilling of a kind of application of city life garbage decrement according to claim 2 processes unit, it is characterised in that：Institute
Stating housing supports slide assemblies to include supporting slide assemblies by outer and interior the first housing located at top layer flooring installation place（27）,
Two housings support slide assemblies（28）Slide assemblies are supported with the 3rd housing located at middle level flooring installation place（35）, and second shell
Body supports slide assemblies（28）And the 3rd housing support slide assemblies（35）Inner side be provided with sliding bearing（29）, and dry distilling room
（26）Lower case Jing elastic supporting seats（37）It is fixed on the flooring of middle level.
4. the innoxious dry distilling of a kind of application of city life garbage decrement according to claim 1 processes unit, it is characterised in that：Institute
State spiral pusher main shaft（9）Warp beam holds the drive end bearing bracket for being installed on preheating and drying dehydration furnace（7）With rear end cap（19）Between, and front end
Lid Jing bolts are fixed on the cylinder of preheating and drying dehydration furnace, and preheating and drying dehydration furnace is stretched out in the front end of spiral pusher main shaft, and
Jing is placed on the bearing fixed seat of preheating and drying dehydration furnace（6）Support pusher motor is connected to after fixing（5）, bearing fixed seat and
First pusher motor is all fixedly installed in vehicle frame（8）On.
5. the innoxious dry distilling of a kind of application of city life garbage decrement according to claim 1 processes unit, it is characterised in that：Institute
State preheating and drying dehydration furnace（12）On be provided with dry gas relief valve（18）And othermohygrometer detector unit（17）, and air pressure temperature
Degree detector unit seals feed valve with first High Temperature Rotating（3）Control end connection；The dry distilling room（26）Top set
It is equipped with neutron material-level meter（30）, the dry distilling room（26）Bottom be provided with charcoal detector（301）, neutron material-level meter（30）And charcoal
Detector（301）Respectively with dry distilling room control system（48）Connection, the outfan of dry distilling room control system connect second and third high temperature
Rotary sealing feeding valve（22、42）Control end.
6. the innoxious dry distilling of a kind of application of city life garbage decrement according to claim 1 processes unit, it is characterised in that：Institute
State first and second heating in medium frequency unit（31、33）Outside arrange heat-insulation layer（34）.
7. the innoxious dry distilling of a kind of application of city life garbage decrement according to claim 1 processes unit, it is characterised in that：Institute
State charcoal outlet（43）Neighbouring setting water mist sprinkling dust-cleaning and refrigerating mechanism（44）.
8. the innoxious dry distilling of a kind of application of city life garbage decrement according to claim 1 processes unit, it is characterised in that：Institute
State preheating and drying dehydration furnace（12）With dry distilling room（26）It is respectively multiple, and all preheating and drying dehydration furnaces（12）First pyrolysis
Generate gas outlet (16) Jing gases integrator and connect the Separate System of Water-jet（46）Second pyrolysis generate gas access
（460）.
9. the innoxious dry distilling of a kind of application of city life garbage decrement according to claim 1 processes unit, it is characterised in that：Institute
State jet dynamic control（47）Outfan connection utility network.
10. the innoxious dry distilling of a kind of application of city life garbage decrement according to claim 1 processes unit, it is characterised in that：
The jet dynamic control（47）The outfan innoxious dry distilling of connection application of city life garbage process the feeder ear of unit.
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| CN201621135423.5U CN206109302U (en) | 2016-10-19 | 2016-10-19 | Unit is handled in innoxious dry distillation of municipal solid waste decrement |
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| CN201621135423.5U CN206109302U (en) | 2016-10-19 | 2016-10-19 | Unit is handled in innoxious dry distillation of municipal solid waste decrement |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107520239A (en) * | 2017-09-21 | 2017-12-29 | 航天环境工程有限公司 | Plasma dangerous waste processing method |
| CN108393336A (en) * | 2018-03-26 | 2018-08-14 | 溆浦农达科技有限公司 | A kind of domestic garbage treating system and its processing method |
| CN109937096A (en) * | 2017-11-03 | 2019-06-25 | 董平年 | A kind of cracking reduction conversion reaction processing equipment of domestic organic garbage |
| CN112077131A (en) * | 2020-10-29 | 2020-12-15 | 内蒙古蒙投环境股份有限公司 | Continuous carbonization and pyrolysis system for municipal solid waste |
-
2016
- 2016-10-19 CN CN201621135423.5U patent/CN206109302U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107520239A (en) * | 2017-09-21 | 2017-12-29 | 航天环境工程有限公司 | Plasma dangerous waste processing method |
| CN109937096A (en) * | 2017-11-03 | 2019-06-25 | 董平年 | A kind of cracking reduction conversion reaction processing equipment of domestic organic garbage |
| CN108393336A (en) * | 2018-03-26 | 2018-08-14 | 溆浦农达科技有限公司 | A kind of domestic garbage treating system and its processing method |
| CN112077131A (en) * | 2020-10-29 | 2020-12-15 | 内蒙古蒙投环境股份有限公司 | Continuous carbonization and pyrolysis system for municipal solid waste |
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