CN107192243A - A kind of house refuse drying device - Google Patents
A kind of house refuse drying device Download PDFInfo
- Publication number
- CN107192243A CN107192243A CN201710203529.7A CN201710203529A CN107192243A CN 107192243 A CN107192243 A CN 107192243A CN 201710203529 A CN201710203529 A CN 201710203529A CN 107192243 A CN107192243 A CN 107192243A
- Authority
- CN
- China
- Prior art keywords
- drying device
- house refuse
- dry
- dry channel
- rubbish
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 238000001035 drying Methods 0.000 title claims abstract description 46
- 239000010850 non-combustible waste Substances 0.000 claims abstract description 17
- 239000002699 waste material Substances 0.000 claims abstract description 12
- 238000010438 heat treatment Methods 0.000 claims abstract description 4
- 239000010813 municipal solid waste Substances 0.000 claims description 37
- 238000012545 processing Methods 0.000 abstract description 15
- 238000013461 design Methods 0.000 abstract description 4
- 239000002994 raw material Substances 0.000 abstract description 2
- 238000000197 pyrolysis Methods 0.000 description 25
- 239000007789 gas Substances 0.000 description 15
- 238000009434 installation Methods 0.000 description 10
- 239000000779 smoke Substances 0.000 description 10
- 239000010410 layer Substances 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 239000002910 solid waste Substances 0.000 description 7
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 239000003546 flue gas Substances 0.000 description 6
- 229910001220 stainless steel Inorganic materials 0.000 description 6
- 239000010935 stainless steel Substances 0.000 description 6
- 239000007791 liquid phase Substances 0.000 description 5
- 230000005415 magnetization Effects 0.000 description 5
- 102000004169 proteins and genes Human genes 0.000 description 5
- 108090000623 proteins and genes Proteins 0.000 description 5
- 210000000038 chest Anatomy 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 238000012544 monitoring process Methods 0.000 description 4
- 230000000505 pernicious effect Effects 0.000 description 4
- 239000012071 phase Substances 0.000 description 4
- 238000001179 sorption measurement Methods 0.000 description 4
- 229920000049 Carbon (fiber) Polymers 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 3
- 239000004917 carbon fiber Substances 0.000 description 3
- 230000003197 catalytic effect Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000011229 interlayer Substances 0.000 description 3
- 238000000751 protein extraction Methods 0.000 description 3
- 239000007921 spray Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000003818 cinder Substances 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 230000005399 magnetomechanical effect Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 239000002893 slag Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000013519 translation Methods 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 206010013786 Dry skin Diseases 0.000 description 1
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- 230000000712 assembly Effects 0.000 description 1
- 238000000429 assembly Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 230000001360 synchronised effect Effects 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B15/00—Machines or apparatus for drying objects with progressive movement; Machines or apparatus with progressive movement for drying batches of material in compact form
- F26B15/10—Machines or apparatus for drying objects with progressive movement; Machines or apparatus with progressive movement for drying batches of material in compact form with movement in a path composed of one or more straight lines, e.g. compound, the movement being in alternate horizontal and vertical directions
- F26B15/12—Machines or apparatus for drying objects with progressive movement; Machines or apparatus with progressive movement for drying batches of material in compact form with movement in a path composed of one or more straight lines, e.g. compound, the movement being in alternate horizontal and vertical directions the lines being all horizontal or slightly inclined
- F26B15/18—Machines or apparatus for drying objects with progressive movement; Machines or apparatus with progressive movement for drying batches of material in compact form with movement in a path composed of one or more straight lines, e.g. compound, the movement being in alternate horizontal and vertical directions the lines being all horizontal or slightly inclined the objects or batches of materials being carried by endless belts
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
- F26B25/001—Handling, e.g. loading or unloading arrangements
Abstract
The invention discloses a kind of house refuse drying device, including tunnel type roasting brickkiln, combustiblerefuse drying device and non-combustible waste drying device, the combustiblerefuse drying device and non-combustible waste drying device, all include waste conveyor and multiple dry channels, multiple dry channels are spaced laterally apart the top that brickkiln is calcined in tunnel type, dry channel is calcined the heat of brickkiln as heating source using tunnel type, in the presence of waste conveyor, house refuse passes sequentially through each dry channel.Due to the dry channel in house refuse drying equipment is located at into the top that tunnel type is calcined brickkiln, tunnel type roasting brickkiln is progress brickmaking by raw material of the house refuse of processing, the heat being calcined using tunnel type in brickkiln is thermally dried to the house refuse in dry channel, this design is not only laid out compacter, space is not take up, but also the heat for making tunnel type be calcined in brickkiln is fully used.
Description
Technical field
The present invention relates to a kind of field of garbage disposal, and in particular to a kind of house refuse drying device.
Background technology
State Intellectual Property Office disclosed Publication No. 103691731B on June 29th, 2016, and patent name is kitchen
The Patent Application Publication of refuse disposal system, it includes：Separator, Solid Waste processing unit, liquid phase refuse disposal installation
With oil phase refuse disposal installation；Wherein, separator is used to kitchen garbage being separated into Solid Waste, liquid phase rubbish and oil phase rubbish
Rubbish；Solid Waste processing unit is used to carry out bioprotein processing, the protein of acquisition to the Solid Waste of reception
It is used as feed addictive；Liquid phase refuse disposal installation is used to handle the liquid phase rubbish of reception；Oil phase garbage disposal
Device is used to handle the oil phase rubbish of reception；The Solid Waste processing unit includes the connected extruding of order
Portion, Protein Extraction processing department；Wherein press section is used to carry out extrusion dehydration processing to the Solid Waste, isolates solid
And liquid object；Protein Extraction processing department is used for the extraction for carrying out protein to the solid based on bioprotein extracting mode
And process, obtain the protein as feed addictive；The Solid Waste processing unit also adds including biological energy source product
The Ministry of worker, is connected with the Protein Extraction processing department, the processing for carrying out biological energy source product based on protein；The liquid
Phase refuse disposal installation includes：Homogeneous pond, anaerobic fermentation tank, sludge dewatering portion and the sewage disposal portion of sequential communication.Although on
When stating restaurant garbage treating system processing kitchen garbage, innoxious degree is high, can be avoided as much as secondary pollution and economy
Property is good.But there is following defect：One is the presence of substantial amounts of energy consumption, does not meet the standard of energy-conserving and environment-protective；Two be that rubbish is not obtained
Make full use of, it is to extract useful protein, rubbish generation is also had after extraction.The said equipment is not used drying and set
It is standby.
State Intellectual Property Office disclosed Publication No. 102679364B on July 23rd, 2014, and patent name is kitchen
The Patent Application Publication of refuse disposal system, it is characterized in that：Including magnetization pyrolysis installation, smoke eliminator, digital display monitoring control
Device processed；Wherein, magnetization pyrolysis installation includes：Feeding mouth, body of heater, pyrolysis chamber, shaftless screw batcher, the gradual sealing of strip
Automatic grate, scraper slag removing machine, power generator, time mouth, exhaust opening；Pyrolysis chamber, body of heater side are provided with described body of heater
Wall top is provided with feeding mouth, is fed by shaftless screw batcher；Bottom of furnace body, which is provided with, removes cinder notch；Sidewall of the furnace body bottom is installed by the energy
Generator, is supplied to needed for magnetization pyrolysis installation using magnetic energy translation function, magnetic resonance, magnetomechanical effect and magnetochemistry domino effect
Energy；Thorax thorax body in interlayer, pyrolysis chamber is provided between body of heater and pyrolysis chamber and is provided with back mouth；Body of heater center of top is provided with smoke evacuation
Mouthful, the flue gas of discharge is handled by smoke eliminator；Described body of heater is the domed cylinder in top, makes to enter in body of heater
Annular magnetic flexible and round kiln in thorax coincide；It is provided between described body of heater and pyrolysis chamber on the outside of interlayer, body of heater as one layer not
Become rusty ladle dress, adds refractory insulating layer on thorax thorax body in pyrolysis chamber, forms pyrolysis chamber's Si Bi three-deckers, makes to enter in stove
Magnetic air farthest improved；Described feeding mouth is located at furnace body outer wall from top to bottom at 1/3, by shaftless screw
Batcher is fed；The shaftless screw batcher is closed structure, is difficult to enter heat from feeding mouth from the air without being magnetized
Solve room；Described seals Automatic grate and scraper slag removing machine except cinder notch mounting bar shape is gradual, and during slagging-off, air can not be from slagging-off
Mouth enters pyrolysis chamber, it is ensured that the pyrolysis effect of pyrolysis chamber；Described power generator includes protected type stainless steel box body, stainless steel
Permanent magnet assembly is provided with box body, in the both sides of permanent magnet assembly provided with solidification foamed glue, for by power generator forever
Magnet assemblies are fixed in stainless steel box body；There is a circular hole in stainless steel box body center；Tube at one end passes perpendicularly through stainless steel box body
Central circular hole is connected with permanent magnet assembly, to dredge magnetic field flow direction；The conduit mouth for the side that conduit is connected with pyrolysis chamber is
Inclined-plane, and angle of inclination is 68 degree；The conduit other end is provided with junction button, for being docked with device；Equipped with boiling in stainless steel box body
Stone, plays heat-blocking action；Baffle plate is provided between permanent magnet assembly and conduit, prevents zeolite from revealing；Described permanent magnet assembly is
The permanent magnet assembly being arranged in order in conduit interior orientation；Described power generator is correspondingly arranged many in body of heater lateral wall bottom
Layer；The top and middle part of thorax thorax body are provided with back mouth in described pyrolysis chamber；During described exhaust opening is arranged at the top of body of heater
Position is entreated, exhaust opening is connected by smoke exhaust pipe with pyrolysis chamber and interlayer, make the flue gas produced in device sufficient to greatest extent
Smoke eliminator is discharged into after pyrolysis；The smoke eliminator includes water scrubber, catalytic tower, reduction tower, adsorption tower level Four；Its
The middle setting first order is water scrubber；The water scrubber uses turbogrid tray formula tower cooling system, plays a part of dedusting and cooling；Should
Turbogrid tray formula pyramidal structure is that flue gas is entered by bottom, and water is sprayed from the superiors' turbogrid tray, arrangement one in water scrubber
The hole of multiple geometries is drilled with layer or multilayer turbogrid tray, turbogrid tray, and the area of every layer of turbogrid tray is accumulated more than the tower section
1/2, the straight portion of turbogrid tray is designed to flow-stopping plate so that turbogrid tray baffle plate part while aperture leakage forms excessive
Waterfall is flowed, also through the waterfall of overflow formation while gas flow in the curtain of rain of keyhole formation, the liquid of gas and tower is allowed
Sufficiently contacted；The smoke eliminator sets the second level to be catalytic tower；The catalytic tower using vortex spray washing and
Spiral board separation method；I.e. gas is discharged from tower bottom into top, and tower top is provided with multiple vortex nozzles, makes to form rain in tower
Curtain, the curtain of rain makes drop fully be contacted again with gas, cleans pernicious gas and dust in flue gas；Shower nozzle top is equipped with eddy flow
Plate, is rotated at a high speed by the gas of spiral board in tower, under the influence of centrifugal force the drop in gas be thrown in tower wall with
Gas is separated, so that gas is further purified；The smoke eliminator sets the third level to be reduction tower；The reduction
While tower uses spray washing, two layers of active carbon fiber felt being equipped with tower on column plate is adsorbed to pernicious gas, described
Reduction tower structure is that flue gas enters into upper strata active carbon fiber felt after baffling twice, and in the mistake of baffling twice from bottom
Three Water sprays are carried out in journey by shower to purify, purified gas enters the NACF carpet veneer on top to being harmful to gas
Body carries out activated carbon absorption, absorbs the active carbon fiber felt of pernicious gas at least with two layers to ensure to absorb cleaner；It is described
Smoke eliminator sets the fourth stage to be adsorption tower；The adsorption tower is specially carried out further with NACF to pernicious gas
Absorption, its structure is to be discharged after gas is passed into the activated carbon fiber layers absorption of multilayer by top from the adsorption tower bottom；
Digital display monitors control device, for monitored over time refuse pyrolysis processing procedure, after house refuse is ignited, and opens digital display monitoring control
Temperature in installation's power source switch processed, pyrolysis chamber is shown on digital display monitoring control device display screen；When pyrolysis indoor temperature reaches
During to 850 DEG C, air-introduced machine control is automatically turned on, and smoke eliminator is started working；During digital display monitoring control device setting pan feeding
Between, the pan feeding time one arrives, shaftless screw batcher automatic start, meanwhile, the gradual sealing Automatic grate of strip and scraper plate slagging-off
Machine starts, and pan feeding is synchronous with slagging-off to be carried out, when house refuse is filled to 2/3 height of pyrolysis chamber, and pan feeding stops simultaneously with slagging-off.
Above-mentioned technology is to be supplied to magnetization pyrolysis installation using magnetic energy translation function, magnetic resonance, magnetomechanical effect and magnetochemistry domino effect
Required energy, so as to carry out pyrolysis processing to rubbish.Above-mentioned technical proposal, is not divided house refuse and non-house refuse
Class, is sent directly into magnetization pyrolysis installation and is handled, pyrolysis effect is bad, and energy consumption is big, and also to discharge substantial amounts of flue gas, difficult
Exempt to pollute the environment.
Above-mentioned refuse treatment plant does not use drying equipment due to not classifying using water to house refuse,
This patent is designed on the basis of being classified using water to house refuse.
The content of the invention
It is laid out what heat that is compacter and can making garbage disposal was fully used it is an object of the invention to provide a kind of
House refuse drying device.
To achieve the above object, the technical solution adopted in the present invention is：
A kind of house refuse drying device, including tunnel type roasting brickkiln, combustiblerefuse drying device and non-combustible waste are dried
Device, the combustiblerefuse drying device and non-combustible waste drying device are all logical including waste conveyor and multiple dryings
Road, multiple dry channels are spaced laterally apart the top that brickkiln is calcined in tunnel type, and dry channel is calcined brickkiln with tunnel type
Heat is heating source, in the presence of waste conveyor, and house refuse passes sequentially through each dry channel and forms dry life
Rubbish.
Further, the waste conveyor, including rubbish infeed conveyor belt, multiple propulsion spirals and multiple gap bridges are defeated
Send to be provided between described propulsion spiral, two adjacent dry channels in machine, described dry channel and be provided with described gap bridge
Conveyer, house refuse sends into dry channel through rubbish infeed conveyor belt, and in the presence of spiral is promoted, house refuse is in drying
Pushed ahead in passage, adjacent dry channel is sent into through gap bridge conveyer after dry channel discharge, house refuse is successively
Pass through each dry channel.
Further, the waste conveyor in combustiblerefuse drying device, in addition to rubbish output conveyer belt and rubbish
Disintegrating machine, dries house refuse through rubbish output conveyer belt feeding refuse grinder.
Further, the temperature of the multiple dry channel is different, for combustiblerefuse drying device, and combustiblerefuse is from temperature
Highest dry channel is spent to enter, from the dry channel discharge that temperature is minimum, because this drying mode from high to low, for
Combustiblerefuse effect is best；For non-combustible waste drying device, non-combustible waste enters from the low high dry channel of temperature, from
Temperature highest dry channel is discharged, similarly, through testing, this drying mode from low to high, to non-combustible waste effect most
It is good.
Beneficial effects of the present invention：Due to the dry channel in house refuse drying equipment is located at into tunnel type roasting brickkiln
Top, tunnel type roasting brickkiln be by raw material of the house refuse of processing progress brickmaking, using tunnel type roasting brickkiln in
Heat the house refuse in dry channel is thermally dried, this design is not only laid out compacter, is not take up space,
But also the heat for making tunnel type be calcined in brickkiln is fully used.
Brief description of the drawings
Using accompanying drawing, the invention will be further described, but the embodiment in accompanying drawing does not constitute any limit to the present invention
System, for one of ordinary skill in the art, on the premise of not paying creative work, can also be obtained according to the following drawings
Other accompanying drawings：
The structural representation that Fig. 1 overlooks for the present invention；
Fig. 2 is the side view shown in Fig. 1.
In figure：1st, tunnel type roasting brickkiln；2nd, dry channel；3rd, rubbish infeed conveyor belt；4th, spiral is promoted；5th, mistake
Bridge conveyer；6th, rubbish output conveyer belt；7th, refuse grinder；8th, combustiblerefuse drying device；9th, non-combustible waste is dried
Device.
Embodiment
In order that those skilled in the art more fully understands technical scheme, it is below in conjunction with the accompanying drawings and specific real
Apply example the present invention is described in further detail, it is necessary to explanation, in the case where not conflicting, embodiments herein and
Feature in embodiment can be mutually combined.
As shown in figure 1, a kind of house refuse drying device, including tunnel type roasting brickkiln 1, combustiblerefuse drying device 8
With non-combustible waste drying device 9, the combustiblerefuse drying device 8 and non-combustible waste drying device 9 are all defeated including rubbish
Device and multiple dry channels 2 are sent, multiple dry channels 2 are spaced laterally apart the top that brickkiln 1 is calcined in tunnel type, dry logical
Road 2 is using the heat of tunnel type roasting brickkiln as heating source, and in the presence of waste conveyor, house refuse passes sequentially through each
Dry channel forms dry house refuse.
Further, waste conveyor, including rubbish infeed conveyor belt 3, multiple propulsion spirals 4 and multiple conveyings of passing a bridge
It is provided with machine 5, described dry channel 2 between described propulsion spiral 4, two adjacent dry channels 2 and is provided with described mistake
Bridge conveyer 5, house refuse sends into dry channel 2 through rubbish infeed conveyor belt 3, in the presence of spiral 4 is promoted, house refuse
Pushed ahead in dry channel 2, adjacent dry channel is sent into through gap bridge conveyer 5 after dry channel discharge, is lived
Rubbish passes sequentially through each dry channel 2.
Further, the waste conveyor in combustiblerefuse drying device, in addition to the rubbish output He of conveyer belt 6
Refuse grinder 7, dry house refuse is through the rubbish output feeding refuse grinder 7 of conveyer belt 6.
Further, the temperature of the multiple dry channel 2 is different, when house refuse is combustiblerefuse, combustiblerefuse
Enter from temperature highest dry channel, from the dry channel discharge that temperature is minimum；When house refuse is non-combustible waste, no
Combustiblerefuse enters from the low high dry channel of temperature, from the discharge of temperature highest dry channel.
Operation principle：House refuse is divided into combustiblerefuse and non-combustible waste, and by combustiblerefuse drying device and
They are dried respectively for non-combustible waste drying device；In combustiblerefuse drying device and non-combustible waste drying device
Dry channel is located at the top that tunnel type is calcined brickkiln, using the heat in tunnel type roasting brickkiln to the life in dry channel
Rubbish is thermally dried this design and is not only laid out compacter, is not take up space, but also tunnel type is calcined in brickkiln
Heat be fully used.
Implementation recited above is only that embodiment of the present invention is described, not to the spirit and scope of the present invention
It is defined, under the premise of design of the present invention is not departed from, technology of the ordinary skill technical staff to the present invention in this area
The equivalent structure that scheme the is made technical field related to being directly or indirectly used in, all should fall into protection scope of the present invention.
Claims (4)
1. a kind of house refuse drying device, it is characterised in that：Including tunnel type roasting brickkiln, combustiblerefuse drying device and not
Combustiblerefuse drying device, the combustiblerefuse drying device and non-combustible waste drying device, all including waste conveyor
With multiple dry channels, multiple dry channels are spaced laterally apart the top that brickkiln is calcined in tunnel type, and dry channel is with tunnel
The heat of formula roasting brickkiln is heating source, and in the presence of waste conveyor, house refuse passes sequentially through each dry channel.
2. house refuse drying device according to claim 1, it is characterised in that：The waste conveyor, including rubbish
Described propulsion spiral is provided with rubbish infeed conveyor belt, multiple propulsion spirals and multiple gap bridge conveyers, described dry channel,
Described gap bridge conveyer is provided between two adjacent dry channels, house refuse is dried logical through rubbish infeed conveyor belt feeding
Road, in the presence of spiral is promoted, house refuse is pushed ahead in dry channel, defeated through passing a bridge after dry channel discharge
Machine is sent to send into adjacent dry channel, house refuse passes sequentially through each dry channel and forms dry house refuse.
3. house refuse drying device according to claim 2, it is characterised in that：Rubbish in combustiblerefuse drying device
Conveying device, in addition to rubbish output conveyer belt and refuse grinder, dry house refuse through rubbish output conveyer belt feeding rubbish
Rubbish disintegrating machine.
4. house refuse drying device according to claim 1, it is characterised in that：The temperature of the multiple dry channel is not
Together, for combustiblerefuse drying device, combustiblerefuse enters from temperature highest dry channel, from the dry channel that temperature is minimum
Discharge；For non-combustible waste drying device, non-combustible waste enters from the low high dry channel of temperature, dry from temperature highest
Dry passage discharge.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710203529.7A CN107192243A (en) | 2017-03-30 | 2017-03-30 | A kind of house refuse drying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710203529.7A CN107192243A (en) | 2017-03-30 | 2017-03-30 | A kind of house refuse drying device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107192243A true CN107192243A (en) | 2017-09-22 |
Family
ID=59871772
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710203529.7A Pending CN107192243A (en) | 2017-03-30 | 2017-03-30 | A kind of house refuse drying device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107192243A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111351325A (en) * | 2018-06-25 | 2020-06-30 | 马勇 | Public raincoat drying equipment and drying method |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202350457U (en) * | 2011-11-25 | 2012-07-25 | 天津市国民制药机械有限公司 | Tunnel dryer of high temperature heat pump |
| CN103100552A (en) * | 2013-01-22 | 2013-05-15 | 蒲仁建 | Method and system for carrying out thermal treatment on household garbage by using brick kiln |
| CN203642680U (en) * | 2013-12-16 | 2014-06-11 | 郑州真金耐火材料有限责任公司 | Tunnel kiln waste heat using system |
| CN207214733U (en) * | 2017-03-30 | 2018-04-10 | 练其辉 | A kind of house refuse drying device |
-
2017
- 2017-03-30 CN CN201710203529.7A patent/CN107192243A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202350457U (en) * | 2011-11-25 | 2012-07-25 | 天津市国民制药机械有限公司 | Tunnel dryer of high temperature heat pump |
| CN103100552A (en) * | 2013-01-22 | 2013-05-15 | 蒲仁建 | Method and system for carrying out thermal treatment on household garbage by using brick kiln |
| CN203642680U (en) * | 2013-12-16 | 2014-06-11 | 郑州真金耐火材料有限责任公司 | Tunnel kiln waste heat using system |
| CN207214733U (en) * | 2017-03-30 | 2018-04-10 | 练其辉 | A kind of house refuse drying device |
Non-Patent Citations (1)
| Title |
|---|
| 黄波: "《选煤厂工艺设计与建设》", 31 August 2014, 冶金工业出版社 * |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111351325A (en) * | 2018-06-25 | 2020-06-30 | 马勇 | Public raincoat drying equipment and drying method |
| CN111351325B (en) * | 2018-06-25 | 2021-06-25 | 安徽科瑞户外用品科技有限公司 | Public raincoat drying equipment and drying method |
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