CN206051913U - A kind of waste or used plastics are pyrolyzed dechlorination apparatus - Google Patents
A kind of waste or used plastics are pyrolyzed dechlorination apparatus Download PDFInfo
- Publication number
- CN206051913U CN206051913U CN201620802266.2U CN201620802266U CN206051913U CN 206051913 U CN206051913 U CN 206051913U CN 201620802266 U CN201620802266 U CN 201620802266U CN 206051913 U CN206051913 U CN 206051913U
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- China
- Prior art keywords
- waste
- used plastics
- boiler tube
- condenser
- pyrolyzed
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/141—Feedstock
- Y02P20/143—Feedstock the feedstock being recycled material, e.g. plastics
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Abstract
This utility model is related to technical field of environment protection equipment, more particularly to a kind of waste or used plastics pyrolysis dechlorination apparatus, including：At least two pyrolysis units, pyrolysis unit includes boiler tube, condenser, collecting means and the outer wall located at boiler tube the heating tube for heating to boiler tube, one end of condenser is connected with boiler tube by downtake pipe, and the other end of condenser is provided with waste discharge QI KOU, and collecting means are connected with condenser；Insulation shell, is provided with thermal insulation layer in insulation shell, the inner space of insulation shell is separated at least two soak zones being isolated from each other, and boiler tube is in soak zones；And electronics control, for regulating and controlling the heating-up temperature of heating tube.Waste or used plastics pyrolysis dechlorination apparatus of the present utility model can carry out temperature control respectively to multiple pyrolysis units, simultaneously different waste or used plastics can be carried out being pyrolyzed dechlorination experimentation, and also can same waste or used plastics be carried out with the pyrolysis dechlorination experiment of different temperatures.
Description
Technical field
This utility model is related to technical field of environment protection equipment, more particularly to a kind of waste or used plastics pyrolysis dechlorination apparatus.
Background technology
In waste rubbish, the process problem of waste or used plastics has become focus of attention in China's energy-saving and emission-reduction.At present, it is right
The process of waste rubbish it is general using burn or landfill by the way of.But with the extensive application of chloride organic articles, waste
Chloride organic waste materials in rubbish are also increasing.Due to the particularity of chloride containing article properties, burning disposal is carried out to which
Will produce with strong toxicity bioxin, serious secondary pollution can be caused in entering air, and is filled and is then difficult
Natural degradation, can cause the pollution to water and soil for a long time.
Someone's research in recent years carries out thermal cracking process to waste or used plastics so as to heated, fusing and condensation process step
Become crude oil, crude oil as fuel, can realize the chemical recovery of waste or used plastics.Due to often containing polrvinyl chloride in waste or used plastics
(PVC), generally, often needed first to carry out (230～350 DEG C) decomposition of low temperature before Pintsch process, to remove waste and old modeling
Expect the hydrogen chloride gas of heated generation, prevent hydrogen chloride gas from cracking apparatus are caused with corrosion.Therefore the solution to waste or used plastics
It is significant that dechlorination process carries out experimentation.Existing waste or used plastics pyrolysis installation scale is big, power consumption is high, and only has
One burner hearth for being used for pyrolytic reaction, filler are single, it is impossible to while carrying out experimentation to various different waste or used plastics, cause reality
Test program complicated.Therefore, existing waste or used plastics pyrolysis installation is not applied for experimentation.
Utility model content
(1) technical problem to be solved
The technical problems to be solved in the utility model is to solve existing waste or used plastics pyrolysis installation to meet while right
Various different waste or used plastics carry out the problem of experimentation.
(2) technical scheme
In order to solve above-mentioned technical problem, this utility model provides a kind of waste or used plastics and is pyrolyzed dechlorination apparatus, including：Extremely
Few two pyrolysis units, pyrolysis unit include boiler tube, condenser, collecting means and the outer wall located at boiler tube and for heating to boiler tube
Heating tube, one end of condenser connected with boiler tube by downtake pipe, and the other end of condenser is provided with waste discharge QI KOU, is collected
Part is connected with condenser；Insulation shell, is provided with thermal insulation layer in insulation shell, the inner space of insulation shell is separated at least
Two soak zones being isolated from each other, boiler tube is in soak zones；And electronics control, for regulating and controlling the heating temperature of heating tube
Degree.
According to this utility model, ceramic fibre in soak zones, is provided with.
According to this utility model, also include：Shell, shell surround electronics control and insulation shell.
According to this utility model, boiler tube includes trocar sheath and the removably interior inner sleeve being placed in trocar sheath.
According to this utility model, condenser is provided with cooling medium flowing region, and cooling medium flows region near first row
One end of trachea is provided with air inlet, and which is provided with gas outlet away from the other end of downtake pipe.
According to this utility model, also include：Nitrogen feeder, nitrogen feeder are provided with appendix, and appendix is by ventilation
The one end of pipe with boiler tube away from condenser connects, and breather is provided with the first gas valve.
According to this utility model, appendix is provided with effusion meter.
According to this utility model, also include：Pump-down process case, pump-down process case are connected with waste discharge QI KOU by second exhaust pipe
Logical, pump-down process case includes at least two exhaust treatment regions that are mutually isolated and connecting with second exhaust pipe respectively, at aerofluxuss
Reason is provided with helical structure and treatment fluid in region, sets away from one end of second exhaust pipe in exhaust treatment region on pump-down process case
There is liquid titration detection mouth.
According to this utility model, also include：Aerofluxuss secondary filter treatment box, one end of aerofluxuss secondary filter treatment box pass through
The one end of 3rd exhaustor with pump-down process case away from second exhaust pipe connects, and the other end of aerofluxuss secondary filter treatment box is provided with
Air vent, is provided with porous media in aerofluxuss secondary filter treatment box.
(3) beneficial effect
Above-mentioned technical proposal of the present utility model has the advantage that：
Waste or used plastics pyrolysis dechlorination apparatus of the present utility model include at least two pyrolysis units, and each pyrolysis unit is wrapped
Boiler tube and condenser are included, different waste or used plastics in different boiler tubes, can be loaded, therefore can be while different at least two is useless
Old plastics carry out being pyrolyzed dechlorination process experimentation.Also, it is isolated from each other by thermal insulation layer between different boiler tubes, by electronics
Control is controlled to the heating-up temperature of the heating tube on different boiler tubes, and the temperature inside different boiler tubes can be caused different,
Thus the experiment of different temperatures can be carried out to different boiler tubes, so as to realize that same waste or used plastics are carried out under different temperatures
Pyrolysis dechlorination experimentation.
Description of the drawings
Fig. 1 is the structural representation that the waste or used plastics of this utility model embodiment are pyrolyzed dechlorination apparatus；
Fig. 2 is the cross-sectional schematic in Fig. 1 along A-A.
In figure：1：Boiler tube；101：Trocar sheath；102：Inner sleeve；103：Heating tube；2：Condenser；201：Air inlet；202：
Gas outlet；31：Downtake pipe；32：Second exhaust pipe；33：3rd exhaustor；4：Collecting means；5：Thermal insulation layer；6：Insulation cladding
Body；7：Soak zones；8：Electronics control；9：Shell；10：Flange；11：Bolt；12：Nitrogen feeder；13：Appendix；14：It is logical
Trachea；151：First gas valve；152：Second gas valve；16：Effusion meter；17：Multidirectional adpting flange；18：Pump-down process
Case；19：Liquid titrates detection mouth；20：Aerofluxuss secondary filter treatment box；21：Air vent.
Specific embodiment
It is to make purpose, technical scheme and the advantage of this utility model embodiment clearer, new below in conjunction with this practicality
Accompanying drawing in type embodiment, is clearly and completely described to the technical scheme in this utility model embodiment, it is clear that retouched
The embodiment stated is a part of embodiment of the present utility model, rather than the embodiment of whole.Based on the reality in this utility model
Apply example, the every other embodiment obtained on the premise of creative work is not made by those of ordinary skill in the art, all
Belong to the scope of this utility model protection.
As depicted in figs. 1 and 2, a kind of waste or used plastics of the present utility model are pyrolyzed one embodiment of dechlorination apparatus.Such as Fig. 1
Shown, the waste or used plastics pyrolysis dechlorination apparatus of the present embodiment include at least two pyrolysis units.Each pyrolysis unit includes stove
Pipe 1, condenser 2, collecting means 4 and the outer wall located at boiler tube 1 heating tube 103 for heating to boiler tube 1, the one of condenser 2
End is connected with boiler tube 1 by downtake pipe 31, and the other end of condenser 2 is provided with waste discharge QI KOU, collecting means 4 and 2 phase of condenser
Connection.The waste or used plastics pyrolysis dechlorination apparatus of the present embodiment also include insulation shell 6 and electronics control 8.It is provided with insulation shell 6
The inner space of insulation shell 6 is separated at least two soak zones 7 being isolated from each other, 1, boiler tube by thermal insulation layer 5, thermal insulation layer 5
In soak zones 7, i.e., thermal insulation layer 5 is between each boiler tube 1 and makes all of boiler tube 1 be isolated from each other.Electronics control 8 is used for
The heating-up temperature of regulation and control heating tube 103, electronics control 8 detect the temperature and pressure parameter value inside each boiler tube 1, and right accordingly
The heating-up temperature of the heating tube 103 on the outside of different boiler tubes 1 is regulated and controled respectively, so as to carry out to the temperature inside different boiler tubes 1
Precise control.
The above-mentioned waste or used plastics pyrolysis dechlorination apparatus of the present embodiment include at least two pyrolysis units, and each pyrolysis unit is equal
Including boiler tube 1 and condenser 2, different waste or used plastics can be loaded in different boiler tubes 1, carry out respectively being pyrolyzed dechlorination experiment,
Therefore, the waste or used plastics that the waste or used plastics pyrolysis dechlorination apparatus of the present embodiment can be simultaneously different at least two carry out pyrolysis dechlorination
Technological experiment is studied.Also, it is isolated from each other by thermal insulation layer 5 between different boiler tubes 1, and boiler tube 1 is carried out by soak zones 7
Insulation, is controlled by the heating-up temperature of the heating tube 103 on 8 pairs of different boiler tubes 1 of electronics control, can cause different boiler tubes 1
Internal temperature is different, the experiment of different temperatures thus can be carried out to different boiler tubes 1, so as to realize to same waste and old
Plastics carry out the pyrolysis dechlorination experimentation under different temperatures.Produce after waste or used plastics pyrolysis in the boiler tube 1 of the present embodiment
Gas enters condenser 2, and Jing is cooled into grease, the grease produced by collecting means 4 are collected.
As shown in Fig. 2 in the present embodiment, four pyrolysis units are provided with, each pyrolysis unit includes a boiler tube 1
With a condenser 2, four boiler tubes 1 are axially in parallel and arrange in an array manner.The outside of each boiler tube 1 is provided with four
With the axially in parallel heating tube 103 of boiler tube 1, heating tube 103 adopts siliconits.Heating tube 103 passes through heat radiation and conduction of heat
Mode being internally heated to boiler tube 1 so that the waste or used plastics being placed in boiler tube 1 are heated generation pyrolytic reaction.Four add
Heat pipe 103 is equally spaced along the circumference of boiler tube 1, thus can be made the temperature inside boiler tube 1 to heating inside boiler tube 1
Degree is evenly distributed, so that the waste or used plastics being placed in boiler tube 1 are heated evenly, react abundant.The thermal insulation layer 5 of the present embodiment is adopted
High-temperature heat-resistance ceramic layer, can play the thermal insulation effect between good each boiler tube 1.It should be noted that this utility model
The quantity of pyrolysis unit, the arrangement mode of boiler tube, the quantity of the set-up mode of heating tube and heating tube be not limited to this
Embodiment, can be designed according to actual needs.
Further, ceramic fibre is provided with the soak zones 7 of the present embodiment, can further strengthen heat insulating effect,
Ensure that the working condition of each boiler tube 1 is separate, make the temperature of each boiler tube 1 be independent of each other, it is same waste and old so as to ensure
The accuracy and reliability of plastics Pyrolysis Experiment at different temperatures.
Further, the waste or used plastics pyrolysis dechlorination apparatus of the present embodiment also include shell 9, and shell 9 surrounds 8 He of electronics control
Insulation shell 6, i.e. electronics control 8 and insulation shell 6 are respectively positioned in shell 9, and thus electronics control 8 can be protected.
Further, in the present embodiment, boiler tube 1 includes trocar sheath 101 and inner sleeve 102, and inner sleeve 102 is removably interior
It is placed in trocar sheath 101.Inner sleeve 102 and trocar sheath 101 are one end closing, and the other end is opened wide, wherein, inner sleeve 102 is opened
Stretch in trocar sheath 101 from one end that trocar sheath 101 is opened wide the one end opened.The boiler tube 1 of the present embodiment adopts inside and outside sleeve combination
Mode, greatly reduce the replacement difficulty of inner sleeve 102, it is convenient that extent of corrosion inspection and replacing are carried out to inner sleeve 102, prevent
Only inner sleeve 102 is corroded for a long time and damages.The trocar sheath 101 and inner sleeve 102 of the present embodiment is made using rustless steel.
In the present embodiment, one end that one end and inner sleeve 102 that trocar sheath 101 is opened wide is opened wide is connected with downtake pipe 31, and outward
The end that sleeve pipe 101 is connected with downtake pipe 31 is provided with flange 10 and bolt 11, and inner sleeve 102 is being connected with downtake pipe 31
Logical end is provided with bolt hole, and bolt 11 is inserted in the bolt hole of inner sleeve 102, to fix inner sleeve 102.Trocar sheath 101
Connected with downtake pipe 31 by flange 10, good sealing effectiveness can be played.
Further, in the present embodiment, condenser 2 is provided with cooling medium flowing region, and cooling medium flowing region is close
One end of downtake pipe 31 is provided with air inlet 201, and cooling medium flowing region is provided with away from the other end of downtake pipe 31
Gas outlet 202.Cooling medium enters cooling medium flowing region by air inlet 201, and is discharged by gas outlet 202, thus to Jing
The gas for crossing condenser 2 is cooled down.The cooling medium of the present embodiment is air, and air is blown into by air inlet 201, from gas outlet
202 discharge, and form cooling wind by its flowing, the gas through condenser 2 is cooled down.It is cold through the gas Jing of condenser 2
But grease is formed, is collected by collecting means 4.The collecting means 4 of the present embodiment are connected with the bottom of condenser 2, and collecting means 4 are located at
Near the position of gas outlet 202.The collecting means 4 of the present embodiment are receiving flask.
Further, the waste or used plastics pyrolysis dechlorination apparatus of the present embodiment also include nitrogen feeder 12, nitrogen feeder 12
Appendix 13 is provided with, appendix 13 is connected by the one end of breather 14 with boiler tube 1 away from condenser 2, and breather 14 is provided with
First gas valve 151.Nitrogen is filled with by nitrogen feeder 12 into boiler tube 1, the oxygen in boiler tube 1 can be discharged, and in reality
Keep nitrogen purging being carried out to boiler tube 1 during testing, to ensure in boiler tube 1 as oxygen-free environment, can also make the waste and old modeling in boiler tube 1
The gas that material pyrolysis is produced is discharged in time, is conducive to waste or used plastics pyrolytic reaction abundant.In the present embodiment, on four boiler tubes 1
Breather 14 is equipped with, the first gas valve 151 on each breather 14, is designed with, four breathers 14 are connected with appendix 13
It is logical, may choose whether nitrogen purging to be carried out to its corresponding boiler tube 1 by the opening and closing of the first gas valve 151, make
Obtain actual experiment easy to operate feasible.The end of the appendix 13 of the present embodiment is provided with multidirectional adpting flange 17, multidirectional connection method
Blue 17 are connected with four breathers 14 respectively.The appendix 13 of the present embodiment is provided with the second gas valve 152 and effusion meter 16,
The uninterrupted of nitrogen can control by the second gas valve 152, effusion meter 16 is then used for measuring nitrogen flow parameter value.
Further, the waste or used plastics pyrolysis dechlorination apparatus of the present embodiment also include pump-down process case 18, pump-down process case 18
Connected with the waste discharge QI KOU of condenser 2 by second exhaust pipe 32, pump-down process case 18 include at least two it is mutually isolated and point
The exhaust treatment region not connected with second exhaust pipe 32.The pump-down process case 18 of the present embodiment includes four pump-down process areas
Domain, four exhaust treatment regions are connected by the second comb 32 with four condensers 2 respectively.It is all provided with each exhaust treatment region
The treatment fluid for having helical structure and treatment fluid, the present embodiment adopts distilled water, can absorb hydrogen chloride gas.On pump-down process case 18
One end away from second exhaust pipe 32 in each exhaust treatment region is equipped with liquid titration detection mouth 19, to aerofluxuss
Distilled water in reason region is sampled analysis, can calculate the content of wherein hydrogen chloride.Four exhaust treatment regions mutually every
From, can individually to the 1 interior-heat solution dechlorination of different boiler tubes test produce gas be processed and sample analysis.
Further, the waste or used plastics pyrolysis dechlorination apparatus of the present embodiment also include aerofluxuss secondary filter treatment box 20, aerofluxuss
One end of secondary filter treatment box 20 is connected by the one end of the 3rd exhaustor 33 with pump-down process case 18 away from the second comb 32,
The other end of aerofluxuss secondary filter treatment box 20 is provided with air vent 21.In the present embodiment, through pump-down process case 18 not by
The gas that distilled water in its exhaust treatment region absorbs then enters aerofluxuss secondary filter treatment box 20 by the 3rd exhaustor 33
In, and be discharged in air by air vent 21.A small amount of hydrogen chloride gas, aerofluxuss may also be contained in these remaining gases
Porous media is provided with secondary filter treatment box 20, the porous media of the present embodiment is solid basic oxide, can be fully absorbed
Hydrogen chloride gas in the residual gas of aerofluxuss secondary filter treatment box 20, so as to ensure by aerofluxuss secondary filter treatment box
Not gas containing hydrogen chloride in 20 21 expellant gas of air vent, prevents air pollution.
Waste or used plastics when in use, are first loaded in inner sleeve 102, so by the waste or used plastics pyrolysis dechlorination apparatus of the present embodiment
Inner sleeve 102 is fixed by bolt 11 afterwards, and inner sleeve 102 and trocar sheath 101 is sealed by flange 10.Waste or used plastics
After loading is finished, the second gas valve 152 and the first gas valve 151 are opened, nitrogen purging is carried out to inner sleeve 102, discharged
Oxygen in inner sleeve 102.Operator opens electronics control 8, and control heating tube 103 begins to warm up, and according to practical situation pair
The heating-up temperature of the heating tube 103 on different boiler tubes 1 is regulated and controled, and heating tube 103 is internal in the way of heat radiation, conduction of heat
Sleeve pipe 102 is internally heated, and waste or used plastics are heated generation pyrolysis, and the gas of generation is through condenser 2, a portion Jing
Grease is cooled into, is collected by collecting means 4；Another part is uncolled into grease gas then enter pump-down process case 18.
Absorb into the most of distilled water by pump-down process case 18 of hydrogen chloride gas in the gas of pump-down process case 18, Shao Liangwei
Absorbed hydrogen chloride gas are then entered in aerofluxuss secondary filter treatment box 20, by aerofluxuss secondary filter treatment box 20 in consolidate
Body basic anhydride absorb so that hydrogen chloride gas are not contained from 21 expellant gas of air vent of aerofluxuss secondary filter treatment box 20
Body.
In sum, the waste or used plastics pyrolysis dechlorination apparatus of the present embodiment can enter trip temperature respectively to multiple pyrolysis units
Different waste or used plastics can be carried out being pyrolyzed dechlorination experimentation, also can carry out difference to same waste or used plastics by control simultaneously
The pyrolysis dechlorination experiment of temperature.The waste or used plastics pyrolysis dechlorination apparatus are pyrolysis dechlorination integrated apparatus, compact conformation, scale
Little, power consumption less, reliability it is high.
Finally it should be noted that：Above example only to illustrate the technical solution of the utility model, rather than a limitation；
Although being described in detail to this utility model with reference to the foregoing embodiments, it will be understood by those within the art that：
Which still can be modified to the technical scheme described in foregoing embodiments, or which part technical characteristic is carried out etc.
With replacement；And these modifications or replacement, do not make the essence of appropriate technical solution depart from each embodiment technology of this utility model
The spirit and scope of scheme.
Claims (9)
1. a kind of waste or used plastics are pyrolyzed dechlorination apparatus, it is characterised in that include：
At least two pyrolysis units, the pyrolysis unit include boiler tube, condenser, collecting means and located at the boiler tube outer wall simultaneously
For the heating tube to boiler tube heating, one end of the condenser is connected with the boiler tube by downtake pipe, described
The other end of condenser is provided with waste discharge QI KOU, and the collecting means are connected with the condenser；
Insulation shell, is provided with thermal insulation layer in the insulation shell, and the inner space of the insulation shell is separated at least two
The soak zones being isolated from each other, the boiler tube is in the soak zones；And
Electronics control, for regulating and controlling the heating-up temperature of the heating tube.
2. waste or used plastics according to claim 1 are pyrolyzed dechlorination apparatus, it is characterised in that pottery is provided with the soak zones
Porcelain fiber.
3. waste or used plastics according to claim 1 are pyrolyzed dechlorination apparatus, it is characterised in that also include：Shell, the shell
Surround the electronics control and the insulation shell.
4. waste or used plastics according to claim 1 are pyrolyzed dechlorination apparatus, it is characterised in that the boiler tube include trocar sheath and
The removably interior inner sleeve being placed in the trocar sheath.
5. waste or used plastics according to claim 1 are pyrolyzed dechlorination apparatus, it is characterised in that the condenser is provided with cooling and is situated between
Matter flow region, the cooling medium flowing region are provided with air inlet near one end of the downtake pipe, and which is away from described
The other end of downtake pipe is provided with gas outlet.
6. waste or used plastics according to claim 1 are pyrolyzed dechlorination apparatus, it is characterised in that also include：Nitrogen feeder, institute
State nitrogen feeder and be provided with appendix, the one end of the appendix by breather with the boiler tube away from the condenser connects
Logical, the breather is provided with the first gas valve.
7. waste or used plastics according to claim 6 are pyrolyzed dechlorination apparatus, it is characterised in that the appendix is provided with flow
Meter.
8. waste or used plastics according to claim 1 are pyrolyzed dechlorination apparatus, it is characterised in that also include：Pump-down process case, institute
State pump-down process case to connect with the waste discharge QI KOU by second exhaust pipe, the pump-down process case include at least two mutually every
From and the exhaust treatment region that connects with the second exhaust pipe respectively, helical structure and place are provided with the exhaust treatment region
Reason liquid, is provided with liquid titration inspection away from one end of the second exhaust pipe in the exhaust treatment region on the pump-down process case
Survey mouth.
9. waste or used plastics according to claim 8 are pyrolyzed dechlorination apparatus, it is characterised in that also include：Aerofluxuss secondary filter
Treatment box, one end of the aerofluxuss secondary filter treatment box is by the 3rd exhaustor and the pump-down process case away from described second
One end connection of exhaustor, the other end of the aerofluxuss secondary filter treatment box is provided with air vent, at the aerofluxuss secondary filter
Porous media is provided with reason case.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620802266.2U CN206051913U (en) | 2016-07-27 | 2016-07-27 | A kind of waste or used plastics are pyrolyzed dechlorination apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620802266.2U CN206051913U (en) | 2016-07-27 | 2016-07-27 | A kind of waste or used plastics are pyrolyzed dechlorination apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206051913U true CN206051913U (en) | 2017-03-29 |
Family
ID=58379415
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620802266.2U Expired - Fee Related CN206051913U (en) | 2016-07-27 | 2016-07-27 | A kind of waste or used plastics are pyrolyzed dechlorination apparatus |
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| Country | Link |
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| CN (1) | CN206051913U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110951498A (en) * | 2019-10-12 | 2020-04-03 | 无锡市泰新环保科技有限公司 | Synchronous cracking device for various plastic wastes |
| CN112300835A (en) * | 2020-09-27 | 2021-02-02 | 南京工业大学 | Combined recycling method and device for waste crop straws and agricultural films |
| CN112760099A (en) * | 2021-02-01 | 2021-05-07 | 刘元生 | Pollution-free coking furnace capable of realizing continuous production |
| CN116064064A (en) * | 2021-10-29 | 2023-05-05 | 中国石油化工股份有限公司 | Method and system for recycling waste plastics through pyrolysis |
-
2016
- 2016-07-27 CN CN201620802266.2U patent/CN206051913U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110951498A (en) * | 2019-10-12 | 2020-04-03 | 无锡市泰新环保科技有限公司 | Synchronous cracking device for various plastic wastes |
| CN112300835A (en) * | 2020-09-27 | 2021-02-02 | 南京工业大学 | Combined recycling method and device for waste crop straws and agricultural films |
| CN112760099A (en) * | 2021-02-01 | 2021-05-07 | 刘元生 | Pollution-free coking furnace capable of realizing continuous production |
| CN116064064A (en) * | 2021-10-29 | 2023-05-05 | 中国石油化工股份有限公司 | Method and system for recycling waste plastics through pyrolysis |
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