CN107828440A - A kind of continuous carburetor of waste plastics - Google Patents
A kind of continuous carburetor of waste plastics Download PDFInfo
- Publication number
- CN107828440A CN107828440A CN201711305159.4A CN201711305159A CN107828440A CN 107828440 A CN107828440 A CN 107828440A CN 201711305159 A CN201711305159 A CN 201711305159A CN 107828440 A CN107828440 A CN 107828440A
- Authority
- CN
- China
- Prior art keywords
- kettle
- pipeline
- hydraulic packing
- waste plastics
- valve
- 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
- 239000004033 plastic Substances 0.000 title claims abstract description 43
- 229920003023 plastic Polymers 0.000 title claims abstract description 43
- 239000002699 waste material Substances 0.000 title claims abstract description 23
- 238000012856 packing Methods 0.000 claims abstract description 33
- 238000005336 cracking Methods 0.000 claims abstract description 19
- 238000006243 chemical reaction Methods 0.000 claims abstract description 18
- 238000006555 catalytic reaction Methods 0.000 claims abstract description 17
- 239000006229 carbon black Substances 0.000 claims abstract description 9
- 238000003860 storage Methods 0.000 claims abstract description 7
- 238000007599 discharging Methods 0.000 claims abstract description 5
- 239000010779 crude oil Substances 0.000 claims description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 5
- 239000002283 diesel fuel Substances 0.000 claims description 4
- 239000003502 gasoline Substances 0.000 claims description 4
- 238000011084 recovery Methods 0.000 claims description 4
- 238000010992 reflux Methods 0.000 claims description 4
- 239000007788 liquid Substances 0.000 claims description 3
- 239000002893 slag Substances 0.000 abstract description 13
- 239000000428 dust Substances 0.000 abstract description 5
- 230000000505 pernicious effect Effects 0.000 abstract description 5
- 238000004134 energy conservation Methods 0.000 abstract description 3
- 239000007789 gas Substances 0.000 description 19
- 239000003921 oil Substances 0.000 description 8
- 230000005611 electricity Effects 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 239000002737 fuel gas Substances 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 239000011449 brick Substances 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000686 essence Substances 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000005580 one pot reaction Methods 0.000 description 1
- 238000012946 outsourcing Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
- C10G1/002—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal in combination with oil conversion- or refining processes
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C1/00—Treatment of specific inorganic materials other than fibrous fillers; Preparation of carbon black
- C09C1/44—Carbon
- C09C1/48—Carbon black
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1003—Waste materials
-
- 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
- Y02P20/10—Process efficiency
Abstract
The invention belongs to carburetion equipment technical field, discloses a kind of continuous carburetor of waste plastics, is provided with funnel, and funnel is arranged at the spout of plastic extruders, and motor is arranged on the tail end of plastic extruders；Plastic extruders discharging opening is connected by hydraulic packing valve with cracking reaction kettle, cracking reaction kettle is connected by hydraulic packing valve with kettle of slagging tap, hydraulic packing valve is connected with quadric catalysis kettle, kettle of slagging tap is connected by hydraulic packing valve with quadric catalysis kettle, is connected by hydraulic packing valve with carbon black storage tank, quadric catalysis kettle connects through pipeline with condenser, condenser is between each other by pipeline UNICOM.The continuous carburetor of the waste plastics has been truly realized continuous feed, continuous discharging slag, has effectively utilized on-condensible gas, the purpose of energy-saving and emission-reduction；Itself heat energy is made full use of to reach the purpose of energy-conservation simultaneously；Whole system is under tiny structure and worked, and pernicious gas and dust have obtained effective control, effectively prevent pernicious gas (bioxin) and dust leak.
Description
Technical field
The invention belongs to carburetion equipment technical field, more particularly to a kind of continuous carburetor of waste plastics.
Background technology
There is not the continuous carburetor of waste plastics on a large scale to come into operation both at home and abroad, the country substantially uses small size back
Kettle is answered, is produced the kettle of a kettle one, can not both carry out high-temperature feeding, more can not carry out high temperature deslagging.Improved later,
Solve the problems, such as continuous feed, high temperature deslagging, still, still can not be fed within the previous hour of deslagging, at this
In hour, treat that oily wholeization in slag is complete, then slag it is drained after could feed again, be not in absolute sense it is continuous entering
Material, influences manufacturing schedule.
In summary, the problem of prior art is present be：Existing reaction unit can not carry out high temperature deslagging, deslagging it
Can not be fed in previous hour, in this hour, treat that the oily wholeization in slag is complete, then slag it is drained after could again
Charging, is not the continuous feed in absolute sense, influences manufacturing schedule.
The content of the invention
The problem of existing for prior art, the invention provides a kind of continuous carburetor of waste plastics.
The present invention is achieved in that a kind of continuous carburetor of waste plastics is provided with funnel, and funnel squeezes installed in plastics
At the spout of press, motor is arranged on the tail end of plastic extruders；Plastic extruders discharging opening by hydraulic packing valve with
The connection of cracking reaction kettle, cracking reaction kettle are connected by hydraulic packing valve with kettle of slagging tap, and hydraulic packing valve connects with quadric catalysis kettle
Connect, kettle of slagging tap is connected by hydraulic packing valve with quadric catalysis kettle, is connected by hydraulic packing valve with carbon black storage tank, quadric catalysis
Kettle connects through pipeline with condenser, condenser passes through pipeline UNICOM between each other；Top is connected by pipeline with top, and bottom leads to
Piping is connected with peephole with crude oil tank, and crude oil tank is connected through pipeline with roots blower, roots blower stores up through pipeline and high pressure
Gas tank connection, high pressure tank is connected through pipeline with jet dynamic control, crude oil tank is connected through crude oil pump with rectifying column, rectifying column
Be connected through pipeline with condenser, condenser is connected by pipeline between each other, condenser is connected through pipeline with finished product pans, into
Product pans are through pipeline and reflux pump and gasoline finished pot diesel oil finished pot is connected, finished product pans pass through on-condensible gas recovery valve
It is connected with roots blower.
Further, the power of the motor is 37KW, and the power of the intermediate frequency power supply is 40KW.
Further, the plastic extruders are 200mm bores, length 2800mm；The a diameter of 1000mm of cracking reaction kettle, it is long
Spend for 3000mm；Kettle of slagging tap a diameter of 1000mm, length 3000mm；Quadric catalysis kettle a diameter of 800mm, height 1000mm.
Further, a diameter of 300mm of the hydraulic packing valve, valve body thickness 200mm, the valve body and lock of hydraulic packing valve
Plate is ground using accurate boring.
Further, the crude oil tank internal negative pressure keeps 1000mm-2000mm water columns.
Further, the heating-up temperature of the intermediate frequency power supply can set regulation.
Advantages of the present invention and good effect are：The continuous carburetor of the waste plastics has been truly realized continuous feed, continuous
Deslagging, effectively utilize on-condensible gas, the purpose of energy-saving and emission-reduction；Itself heat energy is made full use of to reach the purpose of energy-conservation simultaneously；It is whole
Individual system is under tiny structure and worked, and pernicious gas and dust have obtained effective control, effectively prevent pernicious gas (bis- Evil
English) and dust leak, keep production plant area cleaning it is clean.
Brief description of the drawings
Fig. 1 is the structural representation of the continuous carburetor of waste plastics provided in an embodiment of the present invention；
In figure：1st, funnel；2nd, motor；3rd, plastic extruders；4th, intermediate frequency power supply；5th, hydraulic packing valve；6th, cracking reaction
Kettle；7th, slag tap kettle；8th, quadric catalysis kettle；9th, carbon black storage tank；10th, condenser；11st, peephole；12nd, crude oil tank；13rd, Luo Cifeng
Machine；14th, high pressure tank；15th, jet dynamic control；16th, crude oil pump；17th, reflux pump；18th, on-condensible gas recovery valve；19th, into
Product pans.
Embodiment
In order to make the purpose , technical scheme and advantage of the present invention be clearer, with reference to embodiments, to the present invention
It is further elaborated.It should be appreciated that the specific embodiments described herein are merely illustrative of the present invention, it is not used to
Limit the present invention.
Below in conjunction with the accompanying drawings and specific embodiment is further described to the application principle of the present invention.
The continuous carburetor of the waste plastics includes funnel 1, and funnel 1 is arranged at the spout of plastic extruders 3, motor
2 are arranged on the tail end of plastic extruders 3, and power is provided for plastic extruders 3；The discharging opening of plastic extruders 3 passes through hydraulic packing
Valve 5 is connected with cracking reaction kettle 6, cracking reaction kettle 6 is connected with kettle 7 of slagging tap by hydraulic packing valve 5, and passes through hydraulic packing valve
5 are connected with quadric catalysis kettle 8, and kettle 7 of slagging tap is connected by hydraulic packing valve 5 with quadric catalysis kettle 8, and passes through hydraulic packing valve 5
It is connected with carbon black storage tank 9, quadric catalysis kettle 8 is connected through pipeline with condenser 10, condenser 10 is condensed by pipeline and next stage
Device UNICOM, top are connected by pipeline with top, and bottom is connected by pipeline with peephole 11 with crude oil tank 12, and crude oil tank 12 passes through
Pipeline is connected with roots blower 13, roots blower 13 is connected through pipeline with high pressure tank 14, high pressure tank 14 through pipeline with
Jet dynamic control 15 is connected, crude oil tank 12 is connected through crude oil pump 16 with rectifying column, rectifying column is connected through pipeline with condenser 10,
Condenser 10 is connected by pipeline with condenser 10, and condenser 10 is connected through pipeline with finished product pans 19, finished product pans 19
Be connected through pipeline with reflux pump 17 and gasoline finished pot diesel oil finished pot, finished product pans 19 by on-condensible gas recovery valve 18 with
Roots blower 13 connects.
The power of the motor 2 is 37KW.The power of the intermediate frequency power supply 4 is 40KW.
Operation principle：In order to ensure yield, waste plastics is pre-processed first, water is first crossed and crushes, remove iron block silt, drag for
After material, dehydration, waste plastics is subjected to feeding from funnel 1, plastic extruders 3 carry out pre-add thermoplastification and addition Cracking catalyst,
Intermediate frequency power supply 4 is set as 250 DEG C, so far by Treatment of Waste Plastics into 250 DEG C or so of molten condition, by hydraulic packing valve 5 simultaneously
Cracking reaction kettle 6 is fed into by pipeline, now the hydraulic packing valve 5 of slag dumping is closed mode；The plastics of molten condition, which enter, to be split
After changing reactor 6, because the temperature of cracking reaction kettle 6 is maintained at 400 DEG C or so, the plastics of molten condition oil and gas at once,
And quadric catalysis kettle 8 is entered by oil gas vent and the hydraulic packing valve 5 of normally open, oil gas passes through quadric catalysis herein,
Quality is further enhanced, and afterwards into condenser 10, the oil gas after condensation is changed into liquid and enters crude oil tank 12, no
Solidifying oil gas body then rests on the top of crude oil tank 12, is pumped into high pressure gas holder by roots blower 13, then be supplied to by high pressure gas holder
Jet dynamic control 15 is used for generating electricity, and the power of the enough whole systems of this power supply and heating are used.Liquid oil in crude oil tank 12,
Got to through crude oil pump 16 in rectifying column, the tower reactor of the tower is also heated using intermediate frequency power supply, controls tower reactor and tower top temperature herein
Degree, you can to obtain qualified gasoline and diesel oil.Cracking reaction kettle 6 and slag tap kettle 7 and plastics extruding with insulation outer layer
Machine 3 uses Electromagnetic Heating, and Electromagnetic Heating power supply is then provided by intermediate frequency power supply, and institute is dynamic in intermediate frequency power supply and system
Power supply is then provided by jet dynamic control 15,, can Xian Yong cities because on-condensible gas is not enough to generate electricity when just having started production
Electricity, after treating that system on-condensible gas generates electricity enough, the electric power sent using jet dynamic control 15 is changed at once.Herein, institute
There is power consumption to be produced by on-condensible gas, reached maximum energy-saving effect！Cracking reaction kettle 6, the volume for kettle 7 of slagging tap are 2.5
Cubic meter, minimum 500 kilograms of one-pot production capacity/per hour, therefore the device daily at least can 20 tons for the treatment of of waste plastics.By 15%
Slag rate, cracking reaction kettle 6 was mutually staggered and slagged tap once to kettle 7 of slagging tap every 3 hours, each half an hour, now, only need to open
Corresponding hydraulic packing valve 5 of slagging tap, after slagging tap every time, hydraulic packing valve 5 of slagging tap accordingly will close immediately.Cracking is anti-
Kettle 6 is answered to continue to feed during slag tap and continue oil gas, within half an hour of slagging tap, if with not changed oily raw material
Enter within kettle 7 of slagging tap, can also continue to carburetion.Slag tap after all having changed oil in kettle 7, that is, close the hydraulic packing of oil-out
Valve 5, hydraulic packing valve 5 of slagging tap is opened, carbon black is discharged to carbon black storage tank 9.Afterwards, hydraulic packing valve 5 of slagging tap is closed, is opened fuel-displaced
Oral fluid means of press seals valve 5.Such cycle repeats above-mentioned action.
Kettle 7 slag tap as cracking reaction kettle 6, is both provided with screw feeder in kettle so that material is heated evenly, and avoids kettle
Wall coking；Inlet and outlet are provided with hydraulic packing valve 5, effectively prevent air from entering in reactor, it is possible to achieve high temperature is slagged tap, and is had
Effect avoid burning, explosion accident produce, both safe and can continuous feed, continuously slag tap, reached purpose of design.
Calorific value of the carbon black of carbon black storage tank 9 still containing 5000 kilocalories, it can directly be sold to common brick factory and be used as fuel.
The system day handles 20 tons of waste plastics, wherein producing 15% not solidifying fuel gas, this fuel gas is by de-
Water warfare, high pressure tank 14 is pressed into by the roots blower 13 of frequency control, for jet dynamic control 15.Theoretical calculation, 3 tons
Fuel gas can send 15000kw/h electricity, and enough the system links heating and power are used, it is not necessary to which outsourcing is fired
Material, embody the purpose of design of efficient energy-conservation.
Above-mentioned carburetion system is kept the tiny structure of 1200pa water columns by the roots blower 13 of adjustable speed.The reality of this function
Existing, ensure that whole system be under tiny structure and work, effectively prevent pernicious gas (bioxin) and dust leak, holding
The cleaning for producing plant area is clean.
The foregoing is merely illustrative of the preferred embodiments of the present invention, is not intended to limit the invention, all essences in the present invention
All any modification, equivalent and improvement made within refreshing and principle etc., should be included in the scope of the protection.
Claims (6)
1. a kind of continuous carburetor of waste plastics, it is characterised in that the continuous carburetor of the waste plastics is provided with funnel, funnel peace
At the spout of plastic extruders, motor is arranged on the tail end of plastic extruders；Plastic extruders discharging opening passes through liquid
Means of press seals valve is connected with cracking reaction kettle, cracking reaction kettle is connected by hydraulic packing valve with kettle of slagging tap, hydraulic packing valve and two
Secondary catalysis kettle connection, kettle of slagging tap are connected with quadric catalysis kettle by hydraulic packing valve, connected by hydraulic packing valve and carbon black storage tank
Connect, quadric catalysis kettle connects through pipeline with condenser, condenser is between each other by pipeline UNICOM；Top passes through pipeline and top
Connection, bottom is connected by pipeline with peephole with crude oil tank, crude oil tank top is connected through pipeline with roots blower, roots blower
It is connected through pipeline with high pressure tank, high pressure tank is connected through pipeline with jet dynamic control, crude oil tank is through crude oil pump and essence
Evaporate tower connection, rectifying column is connected through pipeline with condenser, condenser is connected by pipeline between each other, condenser through pipeline and into
The connection of product pans, finished product pans are connected, on finished product pans through pipeline with reflux pump and gasoline finished pot diesel oil finished pot
Portion is connected by on-condensible gas recovery valve with roots blower.
2. the continuous carburetor of waste plastics as claimed in claim 1, it is characterised in that the power of the motor is 37KW,
The power of the intermediate frequency power supply is 40KW.
3. the continuous carburetor of waste plastics as claimed in claim 1, it is characterised in that the plastic extruders are 200mm mouths
Footpath, length 2800mm；Cracking reaction kettle a diameter of 1000mm, length 3000mm；The a diameter of 1000mm of kettle of slagging tap, length
3000mm；Quadric catalysis kettle a diameter of 800mm, height 1000mm.
4. the continuous carburetor of waste plastics as claimed in claim 1, it is characterised in that the hydraulic packing valve it is a diameter of
300mm, valve body thickness 200mm, the valve body and flashboard of hydraulic packing valve are ground using accurate boring.
5. the continuous carburetor of waste plastics as claimed in claim 1, it is characterised in that the crude oil tank internal negative pressure is kept
1000mm-2000mm water columns.
6. the continuous carburetor of waste plastics as claimed in claim 1, it is characterised in that the heating-up temperature of the intermediate frequency power supply is equal
Regulation can be set.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711305159.4A CN107828440A (en) | 2017-12-11 | 2017-12-11 | A kind of continuous carburetor of waste plastics |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711305159.4A CN107828440A (en) | 2017-12-11 | 2017-12-11 | A kind of continuous carburetor of waste plastics |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107828440A true CN107828440A (en) | 2018-03-23 |
Family
ID=61642232
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711305159.4A Pending CN107828440A (en) | 2017-12-11 | 2017-12-11 | A kind of continuous carburetor of waste plastics |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107828440A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114015467A (en) * | 2021-12-16 | 2022-02-08 | 广西海鸥能源装备有限公司 | Waste organic matter energy conversion device |
| CN114032116A (en) * | 2021-12-22 | 2022-02-11 | 广西海鸥能源装备有限公司 | Large-scale and continuous waste organic matter energy conversion device |
| CN114106866A (en) * | 2021-12-16 | 2022-03-01 | 广西海鸥能源装备有限公司 | Novel conversion of abandonment organic matter energy device |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103059897A (en) * | 2013-01-16 | 2013-04-24 | 欧卓木 | Continuous waste-plastic carburation device and production method |
| CN104293368A (en) * | 2014-10-29 | 2015-01-21 | 烟台荣盛压力容器制造有限公司 | Waste plastics oil refining device |
| CN106281396A (en) * | 2016-08-31 | 2017-01-04 | 蓝德环保科技集团股份有限公司 | Waste plastic cracking equipment and method |
| CN207775148U (en) * | 2017-12-11 | 2018-08-28 | 广西锟德能源科技有限公司 | A kind of continuous carburetor of waste plastics |
-
2017
- 2017-12-11 CN CN201711305159.4A patent/CN107828440A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103059897A (en) * | 2013-01-16 | 2013-04-24 | 欧卓木 | Continuous waste-plastic carburation device and production method |
| CN104293368A (en) * | 2014-10-29 | 2015-01-21 | 烟台荣盛压力容器制造有限公司 | Waste plastics oil refining device |
| CN106281396A (en) * | 2016-08-31 | 2017-01-04 | 蓝德环保科技集团股份有限公司 | Waste plastic cracking equipment and method |
| CN207775148U (en) * | 2017-12-11 | 2018-08-28 | 广西锟德能源科技有限公司 | A kind of continuous carburetor of waste plastics |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114015467A (en) * | 2021-12-16 | 2022-02-08 | 广西海鸥能源装备有限公司 | Waste organic matter energy conversion device |
| CN114106866A (en) * | 2021-12-16 | 2022-03-01 | 广西海鸥能源装备有限公司 | Novel conversion of abandonment organic matter energy device |
| CN114032116A (en) * | 2021-12-22 | 2022-02-11 | 广西海鸥能源装备有限公司 | Large-scale and continuous waste organic matter energy conversion device |
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| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
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Application publication date: 20180323 |