CN205424935U - Rubbish dechlorination device - Google Patents
Rubbish dechlorination device Download PDFInfo
- Publication number
- CN205424935U CN205424935U CN201620108522.8U CN201620108522U CN205424935U CN 205424935 U CN205424935 U CN 205424935U CN 201620108522 U CN201620108522 U CN 201620108522U CN 205424935 U CN205424935 U CN 205424935U
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- rubbish
- air
- drying kiln
- catalyst
- guipure
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Abstract
The utility model discloses a rubbish dechlorination device, including feed mechanism, drying kiln, hot supply mechanism, catalyst spray mechanism, tail gas treatment mechanism, the drying kiln includes the box casing, lie in the feed inlet at casing top, lie in the casing front end the air intake, lie in the casing tail end gas exhaust port, be fixed in shells inner wall multistage conveying mesh belt, be fixed in conveyer belt bottom the casing, be fixed in the microwave generator of casing outer wall, feed mechanism connects in feed inlet department, and hot supply mechanism connects in air intake department, and tail gas treatment mechanism connects the department in gas exhaust port, multistage conveying mesh belt's first order conveying mesh belt lies in the feed inlet under, and the conveyer belt lies in last one -level conveying mesh belt under, it is equipped with the discharge gate on the casing of end of the conveyor belt department to be located. The utility model discloses the device of chlorion in the compound such as PVC and polyurethane in can desorption rubbish to thoroughly root out the formation of msw incineration in -process dioxin.
Description
Technical field
This utility model belongs to field of environment protection equipment, is specifically related to a kind of rubbish dechlorination apparatus.
Background technology
At present, China is landfill and burning electricity generation to the main processing ways of domestic waste and flammable industrial refuse, and along with urban population is increasingly concentrated, the addressing of refuse landfill is the most more and more difficult.Burning electricity generation is the preferred road of a kind of minimizing and recycling, but the only daily output rubbish scale more than 400 tons just has investment value.Meanwhile, two Yingcheng Ben Taigao in the tail gas discharged after eliminating waste incineration, also constrain the popularization of this technology.By house refuse and flammable industrial refuse through sorting, broken, dry, molding and make shaped fuel (abroad claiming RDF5), be also the effective way of minimizing and recycling treatment, the method is the most universal in Japan, Korea S, Europe etc..But due to the material made containing macromolecular compounds such as substantial amounts of PVC, polyurethanes in China's house refuse, this material can discharge chloride ion and synthesize the severe toxicity carcinogen such as two English when burning, the most seriously constrains the popularization in China of this technology.
Chinese patent 201410020052.5 discloses one way of life refuse pyrolysis coalification processing method, the rubbish that with the addition of pyrolysis catalysts is knocked down in pyrolysis roller machine, the high temperature hot gas of incinerator gives pyrolysis roller machine outer wall heating, rubbish constantly rolls with the rotation of pyrolysis roller machine and moves forward lentamente, rubbish is constantly heated, successively through drying and dehydrating, the process of pyrolysis, in pyrolysis roller machine, the temperature of pyrolysis controls at about 200 degree, rubbish from pyrolysis coalification roller machine out after, process through dechlorination and become high-quality solid fuel, it is partly into incinerator to burn, heat is provided for pyrolysis roller machine, flap portion can be concentrated for high efficiency gas-to electricity.
Method used by this patent can not reach dechlorination effect, because wanting rubbish dechlorination, its temperature at least to reach 280 degree, and this is common knowledge.Secondly, using roller drying kiln, outside heat supply in this dechlorination equipment, the thermal efficiency is low, and cost is high.
Generally speaking, prior art does not also have a kind of can thoroughly remove the equipment of chlorine in rubbish.
Utility model content
For the problems referred to above, this utility model aims to provide a kind of chloride ion removing and containing in the compound such as PVC and polyurethane in rubbish, thus thoroughly eradicates the generation of two English, rubbish dechlorination apparatus in Refuse Incineration Process.
This utility model solves the technical scheme of problem: a kind of rubbish dechlorination apparatus, including feeding mechanism, the drying kiln being connected with feeding mechanism, the hot organization of supply of heat energy is provided to drying kiln, the catalyst spraying mechanism being connected with feeding mechanism, the tail gas processing mechanism being connected with drying kiln outfan, described drying kiln includes box housing, it is positioned at the charging aperture of case top, it is positioned at the air inlet of housing forward end, it is positioned at the exhaust port of housing tail end, it is fixed on the multistage transmission guipure of inner walls, it is fixed on the conveyer belt of housing inner bottom part, it is fixed on the microwave generator of housing exterior walls；
Described housing exterior walls is installed and is had through hole at microwave generator, and microwave generator sends microwave by through hole in drying kiln；
Described feeding mechanism is connected at charging aperture, and hot organization of supply is connected to air inlet, and tail gas processing mechanism is connected at exhaust port；
The first order of described multistage transmission guipure transmits guipure and is positioned at the underface of charging aperture, and described conveyer belt is positioned at afterbody and transmits the underface of guipure；
The described housing being positioned at conveyer belt end is provided with discharging opening.
In such scheme, conveyer belt relies on the motor outside drying kiln and drives.Microwave generator, except heat in supplementary kiln, maintains outside temperature stabilization, also can accelerate catalytic action.
In a kind of preferably scheme, every one-level of described multistage transmission guipure is all in tilted layout, and is divided into upper and lower two rows to put in drying kiln, and upper row and lower row are that specular is arranged with the axis of drying kiln for axis of symmetry；The tail end that every one-level transmits guipure is respectively positioned on its adjacent next stage and transmits the surface of guipure head end, and the head end that every one-level transmits guipure is equipped with to prevent the baffle plate of rubbish landing；
Described multistage transmission guipure relies on the transmission guipure driving means outside drying kiln and drives.
Described transmission guipure driving means includes drive bearing, driving chain and motor, drives lower driving chain to drive the motion of every primary transmission guipure at motor.
In order to grasp the temperature in drying kiln in time, described drying kiln is interior and exhaust port is provided with kiln temperature sensor.
Concrete, described hot organization of supply includes aerator, the air stove being connected with aerator, the air-introduced machine that is connected with air stove by the first pipeline, described air-introduced machine is connected with the air inlet of drying kiln by warm-air pipe, and described warm-air pipe is provided with hot blast temperature sensor；
Offer air intake on described first pipeline, air filter and regulation valve are installed at this air intake.
Further, it is additionally provided with metal bellows between described air-introduced machine and warm-air pipe, described warm-air pipe is arranged right below go-cart, this go-cart is provided with and the adjusting screw rod being connected bottom warm-air pipe, described warm-air pipe can moving horizontally and regulate the degree of depth inserted in drying kiln with go-cart, warm-air pipe can regulate oneself height with the lifting of adjusting screw rod.
In such scheme, the purpose controlling warm-air pipe insertion depth is to control front portion or the temperature at rear portion in drying kiln, as deep in inserted by warm-air pipe, by caudal temperature height in the drying kiln of side, low near anterior temperature；Otherwise, high near anterior temperature, low by caudal temperature.
Further, also include for controlling aerator, regulation valve, microwave generator action, and detection hot blast temperature sensor and the switch board of kiln temperature sensor.
Concrete, described feeding mechanism includes feed hopper, conveying worm and drives the motor of conveying worm.
Described catalyst spraying mechanism includes the catalyst shower nozzle that the catalyst water pump that catalyst regulation container, the agitator being positioned at catalyst regulation container and motor thereof are connected by pipeline is connected with catalyst water pump outfan with catalyst regulation container, and this catalyst shower nozzle is arranged at drying kiln charging aperture.
Described tail gas processing mechanism includes the water scrubber that the one cyclonic cleaner unit being sequentially connected connects with second cyclone dust extractor with second cyclone dust extractor, this water scrubber top is connected by pipeline Photolytic deodorization device, and water scrubber bottom is connected by drain pipe multistage filtering tank；Installing multiple screw spraying heads in described water scrubber, be additionally provided with water circulating pump between multistage filtering tank and water scrubber, this water circulating pump connects with screw spraying head；
The outfan of described Photolytic deodorization device is connected by pipeline aerofluxus air-introduced machine, and this aerofluxus air-introduced machine outfan connects chimney.
Operation principle of the present utility model is:
(a) by switch board open aerator, air stove produce hot blast and from air filter enter air mixing after, entered in drying kiln by air-introduced machine, metal bellows, warm-air pipe；
B () regulates warm-air pipe respectively by go-cart and adjusting screw rod and inserts the degree of depth and the height of drying kiln；
C () is by measuring the temperature of hot blast temperature sensor and kiln temperature sensing, utilize the frequency of switch board regulation aerator and the aperture of regulation valve to regulate hot blast temperature and to control dynamic equilibrium, control kiln temperature by the power of regulation microwave generator again, make kiln temperature reach at least 280 degree；
D () rubbish after sorting, crush, extracting enters into conveying worm from feed hopper, be transported in drying kiln by rubbish under motor drives；
What e () and step (d) were carried out simultaneously also puts in catalyst regulation container by various catalyst raw materials, utilize motor to drive agitator by catalyst material dissolution and to stir evenly, then by catalyst water pump and catalyst shower nozzle, catalyst mixed solution is sprayed onto garbage table face；
F () surface speckles with on the transmission guipure that the rubbish of catalyst mixed solution enters in drying kiln, falling on conveyer belt transmitting under guipure drives after multistage many backhauls overturn and perturb, this process stops the time of more than 30 minutes at a temperature of at least 280 DEG C；Under catalyst action, the chloride ion contained in PVC and polyurethane materials in rubbish is spun off and is reduced generation hydrogen chloride gas；
G () conveyer belt is transported to discharging opening by drying the rubbish with dechlorination and by under driven by motor conveying worm, rubbish is discharged drying kiln；
H the mixed gas such as water vapour, hydrogen chloride gas and dust in () drying kiln are drawn into one cyclonic cleaner unit under aerofluxus air-introduced machine effect and second cyclone dust extractor carries out dust removal process, carry out dedusting then into water scrubber and deacidification processes, enter back into and Photolytic deodorization device carries out deodorization process, then discharged by chimney；
(i) the sewage containing dust and hydrochloric acid is flowed in multistage filtering tank, added with calcium hydroxide alkaline solution in tank, hydrochloric acid in reactive tank and calcium hydroxide generation chemical reaction and generate calcium chloride salt, calcium chloride salt is deposited in multistage filtering bottom of gullet, and the clean water through precipitation is extracted into water scrubber repetitive cycling under water circulating pump effect and uses.
Remarkable result of the present utility model is: devise in a set of brand-new removing rubbish the device of chloride ion in the compound such as PVC and polyurethane, the more important thing is the design of drying kiln, enable to rubbish ceaselessly overturn and perturb continuously under driving at guipure, hydrous matter in rubbish is oven-dried and fully dechlorination, thus thoroughly eradicate the generation of two English in Refuse Incineration Process, realize directly burning or the gasification, and combustion of house refuse and flammable industrial refuse, promote waste incineration and generating electricity or the popularization of molding derivatived fuel technology.
Accompanying drawing explanation
The utility model is described in further detail below in conjunction with the accompanying drawings.
Fig. 1 is this utility model apparatus structure schematic diagram.
In figure: 1-air stove；2-aerator；3-air-introduced machine；4-regulates valve；5-air filter；6-switch board；7-metal bellow；8-go-cart；9-adjusting screw rod；10-hot blast temperature sensor；11-feed hopper；12-conveying worm；13-motor；14-drying kiln；15-Multi-stage transmission guipure；16-plate washer；17-conveyer belt；18-kiln temperature sensor；19-motor；20-driving chain；21-drive bearing；22-motor；23-conveying worm；24 motors；25-catalyst regulation container；26-agitator；27-motor；28-catalyst water pump；29-one cyclonic cleaner unit；30-second cyclone dust extractor；31-water scrubber；32-screw spraying head；33-water circulating pump；34-multistage filtering tank；35-drain pipe；36-Photolytic deodorization device；37-aerofluxus air-introduced machine；38-chimney；39-catalyst shower nozzle；40-microwave generator；41-warm-air pipe；42-housing；43-the first pipeline.
Detailed description of the invention
As shown in Figure 1, a kind of rubbish dechlorination apparatus, the tail gas processing mechanism that the catalyst spraying mechanism that the drying kiln 14 being connected with feeding mechanism including feeding mechanism, the hot organization of supply providing heat energy to drying kiln 14 are connected with feeding mechanism is connected with drying kiln 14 outfan.Described drying kiln 14 includes box housing 42, the charging aperture being positioned at housing 42 top, is positioned at the air inlet of housing 42 front end, is positioned at the exhaust port of housing 42 tail end, is fixed on the multistage transmission guipure 15 of housing 42 inwall, is fixed on the conveyer belt 17 of housing 42 inner bottom part, is fixed on the microwave generator 40 of housing 42 outer wall.
Described housing 42 outer wall is installed and is had through hole at microwave generator 40, and microwave generator 40 sends microwave by through hole in drying kiln 14.
Described feeding mechanism is connected at charging aperture, and hot organization of supply is connected to air inlet, and tail gas processing mechanism is connected at exhaust port.
The first order of described multistage transmission guipure 15 transmits guipure and is positioned at the underface of charging aperture, and described conveyer belt 17 is positioned at afterbody and transmits the underface of guipure.
The described housing 42 being positioned at conveyer belt 17 end is provided with discharging opening.The motor 22 that conveyer belt 17 relies on outside drying kiln 14 drives.
Every one-level of described multistage transmission guipure 15 is all in tilted layout, and is divided into upper and lower two rows to put in drying kiln 14, and upper row and lower row are that specular is arranged with the axis of drying kiln for axis of symmetry.The tail end that every one-level transmits guipure is respectively positioned on its adjacent next stage and transmits the surface of guipure head end, and the head end that every one-level transmits guipure is equipped with to prevent the baffle plate 16 of rubbish landing.
Described multistage transmission guipure 15 relies on the transmission guipure driving means outside drying kiln 14 and drives.Described transmission guipure driving means includes drive bearing 21, driving chain 20 and motor 19, drives lower driving chain 20 to drive every primary transmission guipure to move at motor 19.
Described drying kiln 14 is interior and exhaust port is provided with kiln temperature sensor 18.
Described hot organization of supply includes aerator 2, the air stove 1 being connected with aerator 2, passes through, with air stove 1, the air-introduced machine 3 that the first pipeline 43 is connected.Described air-introduced machine 3 is connected with the air inlet of drying kiln 14 by warm-air pipe 41, and described warm-air pipe 41 is provided with hot blast temperature sensor 10.Offer air intake on described first pipeline 43, air filter 5 and regulation valve 4 are installed at this air intake.
It is additionally provided with metal bellows 7 between described air-introduced machine 3 and warm-air pipe 41.Described warm-air pipe 41 is arranged right below go-cart 8, this go-cart 8 is provided with and the adjusting screw rod 9 being connected bottom warm-air pipe 41, described warm-air pipe 41 can moving horizontally and regulate the degree of depth inserted in drying kiln 14 with go-cart 8, warm-air pipe 41 can regulate oneself height with the lifting of adjusting screw rod 9.
Further, also include for controlling aerator 2, regulation valve 4, microwave generator 40 action, and detection hot blast temperature sensor 10 and the switch board 6 of kiln temperature sensor 18.
Described feeding mechanism includes feed hopper 11, conveying worm 12 and drives the motor 13 of conveying worm 12.
Described catalyst spraying mechanism includes the catalyst shower nozzle 39 that the catalyst water pump 28 that catalyst regulation container 25, the agitator 26 being positioned at catalyst regulation container 25 and motor 27 thereof are connected by pipeline is connected with catalyst water pump 28 outfan with catalyst regulation container 25, and this catalyst shower nozzle 39 is arranged at drying kiln 14 charging aperture.
Described tail gas processing mechanism includes the water scrubber 31 that the one cyclonic cleaner unit 29 being sequentially connected connects with second cyclone dust extractor 30 with second cyclone dust extractor 30, this water scrubber 31 top is connected by pipeline Photolytic deodorization device 36, and water scrubber 31 bottom is connected by drain pipe 35 multistage filtering tank 34.Installing multiple screw spraying heads 32 in described water scrubber 31, be additionally provided with water circulating pump 33 between multistage filtering tank 34 and water scrubber 31, this water circulating pump 33 connects with screw spraying head 32.
The outfan of described Photolytic deodorization device 36 is connected by pipeline aerofluxus air-introduced machine 37, and this aerofluxus air-introduced machine 37 outfan connects chimney 38.
Operation principle of the present utility model is:
A () opens aerator 2 by switch board 6, hot blast that air stove 1 produces and after the air mixing that air filter 5 enters, and is entered in drying kiln 14 by air-introduced machine 3, metal bellows 7, warm-air pipe 41；
B () regulates warm-air pipe respectively by go-cart 8 and adjusting screw rod 9 and inserts the degree of depth and the height of drying kiln 14；
C () is by measuring the temperature of hot blast temperature sensor 10 and kiln temperature sensing 18, switch board 6 is utilized to regulate the frequency of aerator 2 and the aperture of regulation valve 5 to regulate hot blast temperature and to control dynamic equilibrium, control kiln temperature by the power of regulation microwave generator 40 again, make kiln temperature reach at least 280 degree；
D () rubbish after sorting, crush, extracting enters into conveying worm 12 from feed hopper 11, be transported in drying kiln 14 by rubbish under motor 13 drives；
What e () and step (d) were carried out simultaneously also puts in catalyst regulation container 25 by various catalyst raw materials, utilize motor 27 to drive agitator 26 by catalyst material dissolution and to stir evenly, then by catalyst water pump 28 and catalyst shower nozzle 39, catalyst mixed solution is sprayed onto garbage table face；
F () surface speckles with on the transmission guipure 15 that the rubbish of catalyst mixed solution enters in drying kiln 14, falling on conveyer belt 17 transmitting under guipure drives after multistage many backhauls overturn and perturb, this process stops the time of more than 30 minutes at a temperature of at least 280 DEG C；Under catalyst action, the chloride ion contained in PVC and polyurethane materials in rubbish is spun off and is reduced generation hydrogen chloride gas；
G () conveyer belt 17 will be dried and the rubbish of dechlorination is transported to discharging opening and is driven conveying worm 23 times that rubbish is discharged drying kiln 14 by motor 24；
H the mixed gas such as water vapour, hydrogen chloride gas and dust in () drying kiln 14 are drawn into one cyclonic cleaner unit 29 under aerofluxus air-introduced machine 37 acts on and second cyclone dust extractor 30 carries out dust removal process, carry out dedusting then into water scrubber 31 and deacidification processes, enter back into and Photolytic deodorization device 36 carries out deodorization process, then discharged by chimney 38；
(i) the sewage containing dust and hydrochloric acid is flowed in multistage filtering tank 34, added with calcium hydroxide alkaline solution in tank, hydrochloric acid in reactive tank and calcium hydroxide generation chemical reaction and generate calcium chloride salt, calcium chloride salt is deposited in bottom multistage filtering tank 34, and the clean water through precipitation is extracted into water scrubber 31 repetitive cycling under water circulating pump 33 acts on and uses.
Claims (10)
1. a rubbish dechlorination apparatus, including feeding mechanism, the drying kiln (14) being connected with feeding mechanism, the hot organization of supply of heat energy is provided to drying kiln (14), the catalyst spraying mechanism being connected with feeding mechanism, the tail gas processing mechanism being connected with drying kiln (14) outfan, it is characterized in that: described drying kiln (14) includes box housing (42), it is positioned at the charging aperture at housing (42) top, it is positioned at the air inlet of housing (42) front end, it is positioned at the exhaust port of housing (42) tail end, it is fixed on the multistage transmission guipure (15) of housing (42) inwall, it is fixed on the conveyer belt (17) of housing (42) inner bottom part, it is fixed on the microwave generator (40) of housing (42) outer wall；
Described housing (42) outer wall is installed microwave generator (40) place and is had through hole, and microwave generator (40) sends microwave by through hole in drying kiln (14)；
Described feeding mechanism is connected at charging aperture, and hot organization of supply is connected to air inlet, and tail gas processing mechanism is connected at exhaust port；
The first order of described multistage transmission guipure (15) transmits guipure and is positioned at the underface of charging aperture, and described conveyer belt (17) is positioned at afterbody and transmits the underface of guipure；
The described housing (42) being positioned at conveyer belt (17) end is provided with discharging opening.
Rubbish dechlorination apparatus the most according to claim 1, it is characterized in that: every one-level of described multistage transmission guipure (15) is all in tilted layout, it is divided into upper and lower two rows to put in drying kiln (14), and upper row and lower row are that specular is arranged with the axis of drying kiln for axis of symmetry；The tail end that every one-level transmits guipure is respectively positioned on its adjacent next stage and transmits the surface of guipure head end, and the head end that every one-level transmits guipure is equipped with to prevent the baffle plate (16) of rubbish landing；
Described multistage transmission guipure (15) relies on drying kiln (14) transmission guipure driving means outward and drives.
Rubbish dechlorination apparatus the most according to claim 2, it is characterized in that: described transmission guipure driving means includes drive bearing (21), driving chain (20) and motor (19), drive lower driving chain (20) to drive every primary transmission guipure to move at motor (19).
Rubbish dechlorination apparatus the most according to claim 1, it is characterised in that: described drying kiln (14) is interior and exhaust port is provided with kiln temperature sensor (18).
Rubbish dechlorination apparatus the most according to claim 4, it is characterized in that: described hot organization of supply includes the air-introduced machine (3) that the air stove (1) that aerator (2) is connected is connected by the first pipeline (43) with air stove (1) with aerator (2), described air-introduced machine (3) is connected with the air inlet of drying kiln (14) by warm-air pipe (41), and described warm-air pipe (41) is provided with hot blast temperature sensor (10)；
Offer air intake on described first pipeline (43), air filter (5) and regulation valve (4) are installed at this air intake.
Rubbish dechlorination apparatus the most according to claim 5, it is characterized in that: between described air-introduced machine (3) and warm-air pipe (41), be additionally provided with metal bellows (7), described warm-air pipe (41) is arranged right below go-cart (8), this go-cart (8) is provided with the adjusting screw rod (9) being connected with warm-air pipe (41) bottom, described warm-air pipe (41) can moving horizontally and regulate the degree of depth inserted in drying kiln (14) with go-cart (8), warm-air pipe (41) can regulate oneself height with the lifting of adjusting screw rod (9).
Rubbish dechlorination apparatus the most according to claim 5, it is characterized in that: also include for controlling aerator (2), regulation valve (4), microwave generator (40) action, and detection hot blast temperature sensor (10) and the switch board (6) of kiln temperature sensor (18).
Rubbish dechlorination apparatus the most according to claim 1, it is characterised in that: described feeding mechanism includes feed hopper (11), conveying worm (12) and drives the motor (13) of conveying worm (12).
Rubbish dechlorination apparatus the most according to claim 1, it is characterized in that: described catalyst spraying mechanism includes the catalyst shower nozzle (39) that the catalyst water pump (28) that catalyst regulation container (25), the agitator (26) being positioned at catalyst regulation container (25) and motor (27) thereof are connected by pipeline is connected with catalyst water pump (28) outfan with catalyst regulation container (25), and this catalyst shower nozzle (39) is arranged at drying kiln (14) charging aperture.
Rubbish dechlorination apparatus the most according to claim 1, it is characterized in that: described tail gas processing mechanism includes the water scrubber (31) that the one cyclonic cleaner unit (29) being sequentially connected connects with second cyclone dust extractor (30) with second cyclone dust extractor (30), this water scrubber (31) top is connected by pipeline Photolytic deodorization device (36), and water scrubber (31) bottom is connected by drain pipe (35) multistage filtering tank (34)；Installing multiple screw spraying heads (32) in described water scrubber (31), be additionally provided with water circulating pump (33) between multistage filtering tank (34) and water scrubber (31), this water circulating pump (33) connects with screw spraying head (32)；
The outfan of described Photolytic deodorization device (36) is connected by pipeline aerofluxus air-introduced machine (37), and this aerofluxus air-introduced machine (37) outfan connects chimney (38).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620108522.8U CN205424935U (en) | 2016-02-03 | 2016-02-03 | Rubbish dechlorination device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620108522.8U CN205424935U (en) | 2016-02-03 | 2016-02-03 | Rubbish dechlorination device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205424935U true CN205424935U (en) | 2016-08-03 |
Family
ID=56540814
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620108522.8U Withdrawn - After Issue CN205424935U (en) | 2016-02-03 | 2016-02-03 | Rubbish dechlorination device |
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| Country | Link |
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| CN (1) | CN205424935U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105546549A (en) * | 2016-02-03 | 2016-05-04 | 湖南鹞翔环保能源科技有限公司 | Trash dechlorination device and method |
-
2016
- 2016-02-03 CN CN201620108522.8U patent/CN205424935U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105546549A (en) * | 2016-02-03 | 2016-05-04 | 湖南鹞翔环保能源科技有限公司 | Trash dechlorination device and method |
| CN105546549B (en) * | 2016-02-03 | 2017-11-21 | 湖南鹞翔环保能源科技有限公司 | A kind of rubbish dechlorination apparatus and its dechlorination method |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20160803 Effective date of abandoning: 20171121 |
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| AV01 | Patent right actively abandoned |