CN108758644A - A kind of low temperature magnetic air refuse disposal installation - Google Patents
A kind of low temperature magnetic air refuse disposal installation Download PDFInfo
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- CN108758644A CN108758644A CN201810854457.7A CN201810854457A CN108758644A CN 108758644 A CN108758644 A CN 108758644A CN 201810854457 A CN201810854457 A CN 201810854457A CN 108758644 A CN108758644 A CN 108758644A
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- wall
- pyrolysis
- low temperature
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- 238000009434 installation Methods 0.000 title claims abstract description 31
- 238000000197 pyrolysis Methods 0.000 claims abstract description 50
- 239000000428 dust Substances 0.000 claims abstract description 12
- 230000000694 effects Effects 0.000 claims abstract description 6
- 230000007704 transition Effects 0.000 claims description 13
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 claims description 8
- 230000007246 mechanism Effects 0.000 claims description 7
- 230000004308 accommodation Effects 0.000 claims description 3
- 238000012544 monitoring process Methods 0.000 claims description 3
- 230000003247 decreasing effect Effects 0.000 claims description 2
- 238000004062 sedimentation Methods 0.000 claims description 2
- 238000010438 heat treatment Methods 0.000 abstract description 6
- 230000008878 coupling Effects 0.000 abstract description 2
- 238000010168 coupling process Methods 0.000 abstract description 2
- 238000005859 coupling reaction Methods 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 29
- 239000010813 municipal solid waste Substances 0.000 description 17
- 238000000034 method Methods 0.000 description 11
- 238000005516 engineering process Methods 0.000 description 9
- 230000008569 process Effects 0.000 description 8
- 239000005416 organic matter Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 239000000571 coke Substances 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- IKHGUXGNUITLKF-UHFFFAOYSA-N Acetaldehyde Chemical compound CC=O IKHGUXGNUITLKF-UHFFFAOYSA-N 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 239000002737 fuel gas Substances 0.000 description 2
- 239000000295 fuel oil Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 230000005415 magnetization Effects 0.000 description 2
- 238000005979 thermal decomposition reaction Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000185 dioxinlike effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 229910052745 lead Inorganic materials 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 231100000004 severe toxicity Toxicity 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 230000032258 transport Effects 0.000 description 1
- 238000004056 waste incineration Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/027—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
Abstract
The present invention relates to a kind of low temperature magnetic air refuse disposal installations, being pyrolyzed warehouse has two layers of inner wall, it is pyrolyzed on the innermost madial wall of warehouse and is evenly arranged with the second air inlet, there is gas outlet in top inner wall, dust and gas are entered by the gas outlet in top inner wall in second channel, and settled in second channel, the effect that slows down by second channel to air-flow, the dust in final second channel can be slipped in collecting bin room.Two layers of the channel formed by three layers of inner wall, since hotter air is from top into the second channel positioned at outside, hotter air is discharged after side wall and bottom wall at positioned at the discharge coupling of bottom, it is equivalent to and has carried out primary heating along entire pyrolysis warehouse surrounding, pyrolysis warehouse is isolated with outside simultaneously, temperature drop is reduced, improves heat utilization rate, temperature rise is more rapid when so that the temperature of pyrolysis warehouse is more uniformly distributed, and work being made just to proceed by.
Description
Technical field
The present invention relates to a kind of low temperature magnetic air refuse disposal installations, belong to garbage classification processing technology field.
Background technology
Traditional trash processing way mainly has the such as landfill, burning landfills that can occupy a large amount of valuable land resources, simultaneously
Environment (air, underground water etc.) is polluted, thus this simple process mode no longer uses substantially.Compared with landfill disposal, rubbish
Rubbish burning is a kind of preferable processing mode.By burning, not only volume greatly reduces, and is also sent out using the heat for burning generation
Electricity, heat supply achieve the purpose that energy recycles so oneself warp of incineration technology becomes a kind of current rubbish generally used both at home and abroad
Treatment technology.But rubbish directly burns that there is also many problems, such as：(1) secondary pollution problem；Organic matter is burnt in component of refuse
Burn sour gas (HCl, HF, the NO generatedxDeng), the high-molecular compound containing chlorine (general designation dioxin-like chemical) of severe toxicity and contain
The flying dust of Hg, Pb can all pollute the environment.(2) burning facility damages problem；Chlorine-containing compound is formed in stove in rubbish
The corrosive gas such as HCl, i.e. can heavy corrosion stove inner metal component at 300 DEG C or more.(3) component of refuse is complicated, various differences
Ingredient has different density, shape, chemical property, catches fire and combustion characteristics, and different flammabilities is presented in they in incinerator
Shape, thus it is difficult to control combustion process.In order to overcome the disadvantages mentioned above of garbage incineration technology, as waste incineration substitute technology
Refuse pyrolysis technology has obtained development and application.In fact, pyrolytic technique, which is applied to industrialization, has very long history, answer earliest
For timber and coal carbonization, to generate the products such as charcoal and coke, with the development that the technology is applied, pyrolysis is also used for
The gasification of heavy oil and coal.
Pyrolysis (Pyrolysis) is also known as destructive distillation, thermal decomposition or charing, refers to that organic matter adds in the state of anaerobic or anoxic
Heat is allowed to the process decomposed.I.e. pyrolysis is to utilize heat under conditions of anaerobic or anoxic using the thermal instability of organic matter
The chemical combination key of compound can be made to be broken, by the organic matter of macromolecule be converted into the fuel gas of small-molecular-weight, liquid fuel and
The process of coke.Pyrolysis and burn similarity be both thermochemical study process but they be entirely different again
Two kinds of process main distinctions are：(1) product burned is mainly CO2And H2O, and thermal decomposition product is mainly flammable degraded
Object is closed, it is gaseous to have H2、CH4,CO；Liquid has the organic matters such as methanol, acetone, acetic acid, acetaldehyde and tar, solvent naphtha etc.；Solid-state
Mainly have coke or carbon black.(2) burning is the oxidation reaction of the principal combustible substance carbon and hydrogen in solid waste, is one and puts
Thermal process, and it is then an endothermic process to be pyrolyzed, and needs to absorb a large amount of heat to make organic compound decompose.(3) it burns only
The heat of generation can be used for generating electricity or heat supply, and the product being pyrolyzed is fuel gas and fuel oil reproducible utilization, and be easy to store
It deposits and transports.
More dust is usually contained in pyrolytic process, in pyrolysis gas, therefore the dust being discharged is more, for gas
Subsequent processing bring big inconvenience.
Invention content
The technical problem to be solved by the present invention is to：For overcome the problems, such as in the prior art, provide a kind of dust generate it is few low
Warm magnetic air refuse disposal installation.
The technical solution adopted by the present invention to solve the technical problems is：
The present invention provides a kind of low temperature magnetic air refuse disposal installation, includes from top to bottom feeding mechanism, charging successively
Warehouse, transition warehouse, pyrolysis warehouse and pedestal：
The feeding mechanism includes visiting at charging warehouse upper channel, under being located at charging warehouse lower channel
Door；
It visits including the upper door pivot at the top of charging warehouse, the door body of visiting being connect with upper door pivot is arranged, setting exists
Door body of visiting side is used for the fixed lock of door body that will visit, and the side for door body of visiting passes through cuts with scissors at the top of connecting rod and charging warehouse
It connects；
Xiamen is the double swing doors that can be opened downwards, including be arranged lower channel both sides by power plant driving and
The articulated shaft of rotation, the rotating bar being separately positioned on two articulated shafts, two pieces of lower door-plates are separately positioned on Xiamen board bottom portion
One end of Xiamen sliding slot with elongate holes, the rotating bar is slidably arranged in respectively in the elongate holes of Xiamen sliding slot,
When the articulated shaft is driven by power plant and rotated, drive lower door-plate in vertical direction and water by the driving effect of rotating bar
It square is moved between, two pieces of lower door-plates can play the role of closing lower channel when being horizontally oriented；
The transition warehouse, the outer wall of transition warehouse are used to be arranged the power plant of driving rotating bar rotation, are used for conduct
Accommodation space when rotating bar and lower door-plate rotate；
The pyrolysis warehouse inner top is provided with two agitating shafts being arranged in parallel in the horizontal direction, the pyrolysis warehouse
Inner bottom wall and madial wall are three layers of inner wall, and to form two layers of channel in bottom and side, it is first passage to be located inside, is located at
Outside is second channel, and the top for being pyrolyzed warehouse is two layers of inner wall, forms one layer of channel, and channel and the second channel at top connect
It is logical；
The inner bottom wall of pyrolysis warehouse is interior in the high V-arrangement in intermediate low both sides, and the halfpace positioned at V-arrangement centre position
The angle of bottom wall and horizontal plane is 40 ° -50 °, the bottom of inner bottom wall, the lower section of halfpace be collect warehouse, second channel with
Warehouse connection is collected, the second air inlet is evenly arranged on the innermost madial wall of the pyrolysis warehouse, has in top inner wall
There are gas outlet, dust and gas to enter in second channel by the gas outlet in top inner wall, and settled in second channel, is received
Collection warehouse bottom is provided with gas outlet joint, and pyrolysis gas is discharged through gas vent interface；
It is provided with several outlet towers in the pyrolysis warehouse, outlet tower includes hollow cylinder and the tool above cylinder
Have the tower body of four sides of pyramid shape, offer the first air inlet on four sides of tower body, the first air inlet it is big
Small to successively decrease with the increase of height, the cylinder side of the outlet tower is provided with the interface being connected to first passage, outlet tower
The bottom of cylinder be connected to first passage, after high temperature magnetic air enters outlet tower, a part of high temperature magnetic air is from tower body
On the first air inlet outflow, another part by first passage finally from the second air inlet flow out, outlet tower is on cross section
In being evenly arranged；
It collects warehouse bottom and is provided with gas outlet joint.
Preferably, low temperature magnetic air refuse disposal installation of the invention, the outlet tower are arranged high from center to both sides
Degree gradually increases, and the setting height of wherein the first air inlet on the outlet tower of lower height is not less than the outlet tower of high height
On the first air inlet setting height.
Preferably, low temperature magnetic air refuse disposal installation of the invention,
Outlet tower is in a row staggered, and the distance of a nearest outlet tower of outlet tower distance is 25-40cm.
Preferably, low temperature magnetic air refuse disposal installation of the invention,
First air inlet and the second air inlet go out mouth down.
Preferably, low temperature magnetic air refuse disposal installation of the invention,
The setting height of gas outlet is not less than the setting height of air inlet, and gas outlet is connected to first passage, the pyrolysis
Observation window is offered on side wall at the top of warehouse.
Preferably, low temperature magnetic air refuse disposal installation of the invention,
If being additionally provided with dry temperature sensor in the pyrolysis warehouse, for monitoring the temperature in pyrolysis warehouse.
Preferably, low temperature magnetic air refuse disposal installation of the invention,
The pedestal is provided with foundation bolt, for fixing on the ground.
Preferably, low temperature magnetic air refuse disposal installation of the invention,
Two pieces of opposite sides of lower door-plate are provided with sheet rubber to play the role of better seal.
Preferably, low temperature magnetic air refuse disposal installation of the invention,
The charging warehouse has funnelform square inner wall
Preferably, low temperature magnetic air refuse disposal installation of the invention,
Wherein one two opposite inner walls extend at the top of charging warehouse, and the angle α of two inner walls is 64-68 °, another opposite
Two inner walls extend in the middle part of charging warehouse, the angle β of two inner walls is 58-62 °.
The beneficial effects of the invention are as follows：The low temperature magnetic air refuse disposal installation of the present invention, pyrolysis warehouse have two layers
Inner wall is pyrolyzed on the innermost madial wall of warehouse and is evenly arranged with the second air inlet, has gas outlet, dust in top inner wall
Entered in second channel by the gas outlet in top inner wall with gas, and settled in second channel, passes through second channel pair
Air-flow slows down effect, and the dust in final second channel can be slipped in collecting bin room.Two formed by three layers of inner wall
Layer channel, since hotter air enters the second channel positioned at outside from top, hotter air is after side wall and bottom wall
It is discharged from the discharge coupling of bottom, is equivalent to and has carried out primary heating along entire pyrolysis warehouse surrounding, while will be hot
Solution warehouse is isolated with outside, is reduced temperature drop, is improved heat utilization rate, the temperature of pyrolysis warehouse is made to be more uniformly distributed, and
Temperature rise is more rapid when work being made just to proceed by.
Description of the drawings
Present invention will be further explained below with reference to the attached drawings and examples.
Fig. 1 is the three-dimensional view of low temperature magnetic air refuse disposal installation in the embodiment of the present invention；
Fig. 2 is the side view of feeding mechanism in the embodiment of the present invention；
Fig. 3 a are the longitudinal section views that a direction at warehouse is fed in the embodiment of the present invention；
Fig. 3 b are the longitudinal section views that another direction at warehouse is fed in the embodiment of the present invention；
Fig. 4 a are sectional views when Xiamen is opened in transition warehouse in the embodiment of the present invention；
Fig. 4 b are sectional views when Xiamen is closed in transition warehouse in the embodiment of the present invention；
Fig. 5 is the side view of transition warehouse in the embodiment of the present invention；
Fig. 6 a are the longitudinal section views that one direction of warehouse is pyrolyzed in the embodiment of the present invention；
Fig. 6 b are the longitudinal section views that another direction of warehouse is pyrolyzed in the embodiment of the present invention；
Fig. 6 c are the longitudinal section views of outlet tower in the embodiment of the present invention；
Fig. 7 is the longitudinal section view of low temperature magnetic air refuse disposal installation in the embodiment of the present invention；.
Specific implementation mode
In conjunction with the accompanying drawings, the present invention is further explained in detail.These attached drawings are simplified schematic diagram, only with
Illustration illustrates the basic structure of the present invention, therefore it only shows the composition relevant to the invention.
In the description of the present application, it is to be understood that term "center", " longitudinal direction ", " transverse direction ", "upper", "lower",
The orientation or positional relationship of the instructions such as "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outside" is
It is based on the orientation or positional relationship shown in the drawings, is merely for convenience of description the application and simplifies to describe, rather than instruction or dark
Show that signified device or element must have a particular orientation, with specific azimuth configuration and operation, therefore should not be understood as pair
The limitation of the application protection domain.In addition, term " first ", " second " etc. are used for description purposes only, and should not be understood as indicating
Or it implies relative importance or implicitly indicates the quantity of indicated technical characteristic." first ", " second " etc. are defined as a result,
Feature can explicitly or implicitly include one or more this feature.In the description of the invention, unless separately
It is described, the meaning of " plurality " is two or more.
In the description of the present application, it should be noted that unless otherwise clearly defined and limited, term " installation ", " phase
Even ", " connection " shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or be integrally connected；It can
Can also be electrical connection to be mechanical connection；It can be directly connected, can also indirectly connected through an intermediary, Ke Yishi
Connection inside two elements.For the ordinary skill in the art, above-mentioned term can be understood by concrete condition
Concrete meaning in this application.
The technical solution of the application is described in detail below with reference to the accompanying drawings and in conjunction with the embodiments.
Embodiment 1
The present embodiment provides a kind of low temperature magnetic air refuse disposal installations, as shown in Figure 1, include successively from top to bottom into
Expect mechanism 1, charging warehouse 2, transition warehouse 3, pyrolysis warehouse 4 and pedestal 5：
The feeding mechanism 1 includes visiting 11 at charging 2 upper channel of warehouse, is located at charging 2 lower channel of warehouse
Xiamen 13；
11 are visited including the upper door pivot 111 at 2 top of charging warehouse, the door of visiting being connect with upper door pivot 111 is arranged
Body 112 is arranged in 112 side of door body of visiting for the fixed lock 113 of the door body 112 that will visit, the side of door body of visiting 112
It is hinged by connecting rod 114 and 2 top of charging warehouse；
Xiamen 12 is the double swing doors that can be opened downwards, including is arranged and is driven by power plant 31 in lower channel both sides
Dynamic and rotation articulated shaft 121, the rotating bar 122 being separately positioned on two articulated shafts 121, two pieces of lower door-plates 123 are set respectively
The Xiamen sliding slot 124 with elongate holes in 123 bottom of lower door-plate is set, one end of the rotating bar 122 is slidably set respectively
It sets in the elongate holes of Xiamen sliding slot 124, when the articulated shaft 121 is driven by power plant and rotated, passes through rotating bar 122
Driving effect drive lower door-plate 123 to be moved between vertically and horizontally, two pieces of lower door-plates 123 are horizontally oriented
When can play the role of close lower channel, two pieces of opposite sides of lower door-plate 123 be provided with sheet rubber 125 with play preferably
Sealing function.The upper top surface of lower door-plate 123 is smooth flat.
The charging warehouse 2 has inclined square inner wall, wherein the inner wall towards 11 direction of rotation of visiting extends to
2 top of warehouse is fed, the angle α of two inner walls is 64-68 °, and the inner wall for 11 direction of rotation both sides of visiting extends in charging warehouse 2
Between, the angle β of two inner walls is 58-62 °, and inner wall surface is smooth；
The transition warehouse 3, the outer wall of transition warehouse 3 are used to be arranged the power plant 31 that driving rotating bar 122 rotates, use
Accommodation space when as rotating bar 122 and the rotation of lower door-plate 123,3 side of transition warehouse is additionally provided with cleaning window 32；
The pyrolysis warehouse 4, including two agitating shafts being arranged in parallel in the horizontal direction at 4 top of pyrolysis warehouse are set
41, it is three layers of inner wall to be pyrolyzed the inner bottom wall of warehouse 4 and madial wall, to form two layers of channel in bottom and side, is located inside
It is second channel 42 positioned at outside for first passage 43, the top of pyrolysis warehouse 4 is two layers of inner wall, forms one layer of channel, top
The channel in portion is connected to second channel 42；
It can be flowed down with the innermost layer in three layers of inner wall after vapor and oil gas condensation；
The inner bottom wall of warehouse 4 is pyrolyzed in the high V-arrangement in intermediate low both sides, and the halfpace 44 positioned at V-arrangement centre position,
The angle of inner bottom wall and horizontal plane is 40 ° -50 °, and the bottom of inner bottom wall, the lower section of halfpace 44 are to collect warehouse 40, second
Channel 42 is connected to warehouse 40 is collected, and the second air inlet is evenly arranged on the innermost madial wall of the pyrolysis warehouse 4
452, there is gas outlet, dust and gas to enter in second channel 42 by the gas outlet in top inner wall in top inner wall, and
Sedimentation, the effect that slows down by second channel 42 to air-flow, the dust in final second channel 42 can in second channel 42
It is slipped to and collects in warehouse 40.Collecting door by opening can clear up, and collect 40 bottom of warehouse and be provided with gas outlet joint
453, pyrolysis gas is discharged through gas vent interface 453, and can connect eliminating malodours from gases equipment after gas vent interface 453 is discharged into sky again
In gas；
Second channel 42 is interconnected at collection warehouse 40；Two layers of the channel formed by three layers of inner wall, due to hotter
Air from top enter positioned at outside second channel 42, hotter air is after side wall and bottom wall from going out positioned at bottom
Be discharged at mouthful interface 453, be equivalent to and carried out primary heating along entire pyrolysis 4 surrounding of warehouse, at the same will pyrolysis warehouse 4 with it is outer
Portion is isolated, and reduces temperature drop, improves heat utilization rate, so that the temperature of pyrolysis warehouse 4 is more uniformly distributed, and work is made just to open
Temperature rise is more rapid when beginning to carry out.
Several outlet towers 45 are provided in the pyrolysis warehouse 4, outlet tower 45 is including hollow cylinder and on cylinder
The tower body of four with the pyramid shape side of side, offers the first air inlet 451 on four sides of tower body, first into
The size of gas port 451 is successively decreased with the increase of height, and the cylinder side of the outlet tower 45 is provided with to be connected with first passage 43
The bottom of logical interface 454, the cylinder of outlet tower 45 is connected to first passage 43, after high temperature magnetic air enters outlet tower 45,
A part of high temperature magnetic air is from the first air inlet 451 outflow on tower body, and another part is by first passage 43 finally from the
Two air inlets 452 flow out, and are flowed out from multiple directions by high temperature magnetic air, keep the high temperature magnetization being passed through in pyrolysis warehouse 4 empty
Gas is more uniform；Outlet tower 45 is in be evenly arranged, and outlet tower 45 is gradual from center to both sides setting height on cross section
Increase, wherein the setting height of the air inlet 451 on the outlet tower 45 of lower height is not less than on the outlet tower 45 of high height
The first air inlet 451 setting height；
Outlet tower 45 is in a row staggered, and distance of the outlet tower 45 apart from a nearest outlet tower 45 is 25-40cm；
Outlet door 48 is provided at halfpace 44, opening outlet door 48 can be clear by the rubbish after pyrolysis processing
It removes；
First air inlet 451 and the second air inlet 452 go out mouth down, to prevent rubbish from entering.
The air through Magnetizing heating that magnetic air generates equipment enters through outlet tower 45 in pyrolysis warehouse 4, heating pyrolysis
Rubbish in warehouse 4；
The setting height of second air inlet 452 is not less than the setting height of the first air inlet 451, passes through the first air inlet
451 and 452 height of the second air inlet setting make high temperature magnetization gas keep uniform in the height direction.It is pyrolyzed 4 top of warehouse
Side wall on offer observation window 46.
If being additionally provided with dry temperature sensor 47 in the pyrolysis warehouse 4, for monitoring the temperature in pyrolysis warehouse 4.
The pedestal 5 is provided with foundation bolt, for fixing on the ground.
Embodiment 2
The present embodiment provides a kind of methods that magnetic air handles organic waste, are magnetized using low temperature described in embodiment 1
Air refuse disposal installation, includes the following steps；
S1：Opening, which is visited, 11 pending rubbish to be added, and is added to visit after pending rubbish and 11 be shut；
S2：So that agitating shaft 41 is rotated, open Xiamen 12, pending rubbish is made to fall into pyrolysis warehouse 4；
S3：The temperature of the air being passed through into pyrolysis warehouse 4 after Magnetizing heating, air is 300-450 DEG C；
S4：It is kept stirring the rotation of axis 41, after handling 2-5h, outlet door 48 is opened and removes residue；
When needing that rubbish is added, then in the case where closing Xiamen 12, opening, which is visited, 11 pending rubbish to be added, addition
Afterwards, 11 opening Xiamen 12 of visiting are turned off.
Visit 11 and 12 liang of Xiamen sect are set, when may be implemented that rubbish is added in processing procedure, keep whole device
It is closed, prevent because open door but be pyrolyzed warehouse 4 in gas leakage, cause environmental pollution.
It is enlightenment with above-mentioned desirable embodiment according to the present invention, through the above description, relevant staff is complete
Various changes and amendments can be carried out without departing from the scope of the technological thought of the present invention' entirely.The technology of this invention
Property range is not limited to the contents of the specification, it is necessary to determine its technical scope according to right.
Claims (10)
1. a kind of low temperature magnetic air refuse disposal installation, which is characterized in that from top to bottom successively include feeding mechanism (1), into
Stock bin body (2), transition warehouse (3), pyrolysis warehouse (4) and pedestal (5)：
The feeding mechanism (1), including it is located at visiting (11) at charging warehouse (2) upper channel, it is located under charging warehouse (2) and leads to
Xiamen (13) at road；
(11) are visited including the upper door pivot (111) at the top of charging warehouse (2) is arranged, are connect with upper door pivot (111) upper
Door door body (112) is arranged in door body of visiting (112) side for the fixed lock (113) of door body (112) that will visit, visits
The side of door body (112) at the top of connecting rod (114) and charging warehouse (2) by being hinged；
Xiamen (12) is the double swing doors that can be opened downwards, including is arranged and is driven by power plant (31) in lower channel both sides
Dynamic and rotation articulated shaft (121), the rotating bar (122) being separately positioned on two articulated shafts (121), two pieces of lower door-plates
(123), the Xiamen sliding slot (124) with elongate holes of lower door-plate (123) bottom, the rotating bar (122) are separately positioned on
One end be slidably arranged in respectively in the elongate holes of Xiamen sliding slot (124), the articulated shaft (121) is driven by power plant
And when rotating, drive lower door-plate (123) to be transported between vertically and horizontally by the driving effect of rotating bar (122)
Dynamic, two pieces of lower door-plates (123) can play the role of closing lower channel when being horizontally oriented；
The transition warehouse (3), the outer wall of transition warehouse (3) are used to be arranged the power plant that driving rotating bar (122) rotates
(31), accommodation space when being used to rotate as rotating bar (122) and lower door-plate (123)；
Pyrolysis warehouse (4) inner top is provided with two agitating shafts being arranged in parallel in the horizontal direction (41), the pyrolysis storehouse
The inner bottom wall and madial wall of body (4) are three layers of inner wall, and to form two layers of channel in bottom and side, it is first logical to be located inside
Road (43) is second channel (42) positioned at outside, and the top of pyrolysis warehouse (4) is two layers of inner wall, forms one layer of channel, top
Channel be connected to second channel (42)；
The inner bottom wall of warehouse (4) is pyrolyzed in the high V-arrangement in intermediate low both sides, and the halfpace (44) positioned at V-arrangement centre position,
The angle of inner bottom wall and horizontal plane is 40 ° -50 °, and the bottom of inner bottom wall, the lower section of halfpace (44) are to collect warehouse (40),
Second channel (42) be connected to warehouse (40) is collected, and described be pyrolyzed on the innermost madial wall of warehouse (4) is evenly arranged with the
Two air inlets (452) there is in top inner wall gas outlet, dust and gas by the gas outlet in top inner wall to enter second logical
In road (42), and the sedimentation in second channel (42), it collects warehouse (40) bottom and is provided with gas outlet joint (453), be pyrolyzed
Gas is discharged through gas vent interface (453)；
It is provided with several outlet towers (45) in the pyrolysis warehouse (4), outlet tower (45) includes hollow cylinder and is located at cylinder
The tower body of four with the pyramid shape side of top offers the first air inlet (451) on four sides of tower body, and
The size of one air inlet (451) is successively decreased with the increase of height, and the cylinder side of the outlet tower (45) is provided with and first
The interface (454) of channel (43) connection, the bottom of the cylinder of outlet tower (45) are connected to first passage (43), high temperature magnetic air
Into after outlet tower (45), a part of high temperature magnetic air passes through from the first air inlet (451) outflow on tower body, another part
First passage (43) is finally flowed out from the second air inlet (452), and outlet tower (45) is in be evenly arranged on cross section；
It collects warehouse (40) bottom and is provided with gas outlet joint (453).
2. low temperature magnetic air refuse disposal installation according to claim 1, which is characterized in that the outlet tower (45) from
Center is gradually increased to both sides setting height, the wherein setting of the first air inlet (451) on the outlet tower (45) of lower height
Setting height of the height not less than the first air inlet (451) on the outlet tower (45) of high height.
3. low temperature magnetic air refuse disposal installation according to claim 1, which is characterized in that
Outlet tower (45) is in a row staggered, and the distance of a nearest outlet tower (45) of outlet tower (45) distance is 25-40cm.
4. low temperature magnetic air refuse disposal installation according to claim 1, which is characterized in that
First air inlet (451) and the second air inlet (452) go out mouth down.
5. low temperature magnetic air refuse disposal installation according to claim 1, which is characterized in that
The setting height of gas outlet (452) is not less than the setting height of air inlet (451), gas outlet (452) and first passage
(43) it is connected to, observation window (46) is offered on the side wall at the top of the pyrolysis warehouse (4).
6. low temperature magnetic air refuse disposal installation according to claim 1, which is characterized in that
The pyrolysis warehouse (4) is if interior be additionally provided with dry temperature sensor (47), for monitoring the temperature in pyrolysis warehouse (4).
7. according to claim 1-6 any one of them low temperature magnetic air refuse disposal installations, which is characterized in that
The pedestal (5) is provided with foundation bolt, for fixing on the ground.
8. according to claim 1-7 any one of them low temperature magnetic air refuse disposal installations, which is characterized in that
Two pieces of opposite sides of lower door-plate (123) are provided with sheet rubber (125) to play the role of better seal.
9. according to claim 1-8 any one of them low temperature magnetic air refuse disposal installations, which is characterized in that
The charging warehouse (2) has funnelform square inner wall.
10. low temperature magnetic air refuse disposal installation according to claim 9, which is characterized in that
Wherein one two opposite inner walls extend at the top of charging warehouse (1), and the angle α of two inner walls is 64-68 °, another opposite
Two inner walls extend in the middle part of charging warehouse (1), the angle β of two inner walls is 58-62 °.
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| CN201810854457.7A CN108758644B (en) | 2018-07-30 | 2018-07-30 | Low-temperature magnetized air garbage treatment device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810854457.7A CN108758644B (en) | 2018-07-30 | 2018-07-30 | Low-temperature magnetized air garbage treatment device |
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| CN108758644B CN108758644B (en) | 2024-04-05 |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN110238169A (en) * | 2019-07-08 | 2019-09-17 | 深圳市思索科技有限公司 | A kind of low temperature thermal decomposition device decomposing environmentally friendly organic matter using nature magnetic force |
| CN112126450A (en) * | 2020-09-29 | 2020-12-25 | 华中科技大学 | Light-gathering pyrolysis catalytic reforming system and method based on spectrum splitting |
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| CN112126450A (en) * | 2020-09-29 | 2020-12-25 | 华中科技大学 | Light-gathering pyrolysis catalytic reforming system and method based on spectrum splitting |
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| CN108758644B (en) | 2024-04-05 |
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