CN106047395A - Equipment for turning waste plastics into oil and process flow of equipment - Google Patents
Equipment for turning waste plastics into oil and process flow of equipment Download PDFInfo
- Publication number
- CN106047395A CN106047395A CN201610581958.3A CN201610581958A CN106047395A CN 106047395 A CN106047395 A CN 106047395A CN 201610581958 A CN201610581958 A CN 201610581958A CN 106047395 A CN106047395 A CN 106047395A
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- China
- Prior art keywords
- oil
- tower
- fixed bed
- catalytic cracking
- bed catalytic
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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
- 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
- C10G1/008—Controlling or regulating of liquefaction processes
-
- 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
-
- 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
- C10G2300/40—Characteristics of the process deviating from typical ways of processing
- C10G2300/4006—Temperature
-
- 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
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/02—Gasoline
-
- 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
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/04—Diesel oil
Abstract
The invention discloses equipment for turning waste plastics into oil and a process flow of the equipment. The equipment comprises a feeding mechanism, a heating furnace, a fixed bed catalytic cracking tower and a separating column, wherein the feeding mechanism is connected with the heating furnace; the heating furnace is connected with the fixed bed catalytic cracking tower through an oil pump, and the upper portion of the fixed bed catalytic cracking tower is connected with the separating column through a conveying pipeline; a condensing cooler is connected to the upper portion of the separating column, a solvent oil tank and a stripping tower are respectively connected to one side of the separating column, and the lower portion of the separating column is connected with reduced fuel oil tank through the oil pump. Oil of different qualities is obtained through melting by the heating furnace, the pyrolysis by the fixed bed catalytic cracking tower and the separation by the separating column. Compared with the prior art, the equipment is high in automation level, low in manpower cost, capable of achieving continuous production, capable increasing the treatment efficiency of the waste plastics, capable of avoiding secondary pollution and significant to resource utilization and environment protection at the present stage.
Description
Technical field
The present invention relates to petrochemical equipment technical field, be specifically related to a kind of waste or used plastics liquefying apparatus and technique stream thereof
Journey.
Background technology
Currently, the white plastic bag producing in commercial production and daily life and abandoning gets more and more, and white pollution is with regard to this
Sample creates, and the most visible nondegradable plastic refuse is for the pollution of environment, and it mainly includes plastic bag, plastics bag
Dress, disposable polypropylene mess-tin, plastic tableware cup dish and electrical equipment filling foaming wadding, plastic beverage bottle, equipment for prepn. of yoghurt, snow
Cake skin etc..Additionally paper mill is used as raw material by some waste and old paper, remaining substantial amounts of plastics after using, although some papermaking
Factory is progressively closing down, but how solving these plastics carried over is still a problem.The domestic recovery to waste or used plastics,
Again making thin film, plastic bag etc. after utilizing and processing employing pelletize mostly, some, as its heat energy of fuel recovery, has
With rubbish by buried underground.Utilizing waste or used plastics to carry out oiling, to become the technique of combustion oil, equipment the simplest
Easy and backward, manual operation, it is interrupted and produces, secondary pollution is serious, and oil quality does not has standard.If the work of advanced person can be explored
These Plastic products are cracked, again refine into oil by skill and equipment again, and free from environmental pollution, and this will be for resource profit
With significant with environmental conservation.
Summary of the invention
For solving drawbacks described above, it is an object of the invention to provide a kind of waste or used plastics liquefying apparatus, reasonable in design, design is skilful
Wonderful, automatization level is higher, it is possible to long periodicity produces continuously, the high-quality weight recovery of oil not only produced after waste or used plastics oiling
Rate is up to more than 95%, and environment does not results in secondary pollution, does not leave over the pollutant such as waste gas, waste water and waste residue after oiling.
It is a further object of the present invention to provide the technological process of a kind of waste or used plastics liquefying apparatus.
For reaching above-mentioned purpose, the technical solution used in the present invention is: a kind of waste or used plastics liquefying apparatus, including feeder
Structure, heating furnace, fixed bed catalytic cracking tower and knockout tower, described feed mechanism is connected with described heating furnace, and described feeder
Being provided with the first autocontrol valve between structure and described heating furnace, described first autocontrol valve is automatically switched off when stopping charging；
Described heating furnace is connected with described fixed bed catalytic cracking tower by oil pump, by conveying above described fixed bed catalytic cracking tower
Pipeline is connected with described knockout tower, and lower section is connected by oil pump a reduced fuel oil tank, and described fixed bed catalytic cracking tower and institute
State and between reduced fuel oil tank, be additionally provided with the first cooling bath；Described knockout tower is connected above condensate cooler, described condensate cooler
One end connects circulating water tower, and lower section connects has oil water separator, described oil water separator bottom to be provided with water storage bag, and described
Oil water separator is connected with gasoline cistern and described knockout tower top respectively by oil pump, is also associated with above described oil water separator
Water sealed tank, described knockout tower side has been also respectively connected with solvent oil tank and stripper, and described stripper is connected with described diesel fuel tank,
It is connected with described reduced fuel oil tank also by oil pump below described knockout tower.
Preferably, described fixed bed catalytic cracking tower, described knockout tower and described oil water separator side are equipped with liquid
Level sensor, and described fixed bed catalytic cracking tower, described knockout tower and described oil water separator be all provided with when being connected with oil pump
There are the second autocontrol valve, described second autocontrol valve to receive the height of liquid level signal of described liquid level sensor and control oil plant stream
The speed of speed.
It is provided with the second cooling bath between described knockout tower and described solvent oil tank.
Described oil pump is all set to double group pump.
Described fixed bed catalytic cracking tower outer wall is provided with catalyst and adds entrance.
Described water sealed tank is connected with described heating furnace, and is provided with flame-retardant device between described water sealed tank and described heating furnace.
Described fixed bed catalytic cracking tower is connected with the coil pipe being provided with inside described knockout tower by oil pump, and described coil pipe exists
It is connected with described first cooling bath outside described splitter column.
The technological process of a kind of waste or used plastics liquefying apparatus, it is characterised in that comprise the following steps:
1) waste or used plastics pretreatment: sorting-broken-clean-dry；
2) heating: the waste or used plastics processed in step 1) is sent into by feed mechanism and obtains height after adding heat fusing in heating furnace
Geothermal liquid, described heating furnace internal temperature in heating process is maintained between 450 DEG C～480 DEG C, if conveying mechanism stop into
When material or workman leave, described first autocontrol valve cuts out transfer passage, and in preventing heating furnace, high-temp liquid flows backwards；
3) vaporization and catalytic pyrolysis: by step 2) in the high-temp liquid that obtains be conveyed into fixed bed catalytic cracking tower by oil pump
In, described fixed bed catalytic cracking tower adds catalyst, is vaporized liquid, catalytic pyrolysis, and the gas after cracking passes through institute
Stating and enter in knockout tower above fixed bed catalytic cracking tower, the liquid stayed after cracking is reduced fuel oil, and reduced fuel oil is by oil
Transport pump, to the coil pipe within described knockout tower, enters described first cooling bath after heat exchange, is finally delivered to reduced fuel oil
Tank；
4) cracked gas separates: described knockout tower receives after the cracked gas of described fixed bed catalytic cracking tower, to cracking
Gas separates, and the lightweight component above described knockout tower is carried out condensation process by described condensate cooler of leading up to, and
Processed by circulating water tower cooler, then the process through oil water separator, isolated moisture is discharged by water storage bag, separates
The gasoline part gone out is sent directly into gasoline cistern by oil pump, and another part is delivered to above described knockout tower, by gasoline
Temperature controls described separation column temperature, and the isolated condensed gas that is difficult to enters water sealed tank, eventually enters into heating furnace mist
It is turned into fuel；After the isolated solvent naphtha in another road makes full use of heat exchange resource, enter molten after being cooled down by the second cooling bath
Agent oil tank；The process by stripper of 3rd tunnel, withdraws lightweight component, and by oil pump, the diesel oil obtained is conveyed into diesel fuel tank；
4th tunnel directly carries diesel oil to described diesel fuel tank by oil pump below described knockout tower, and the internal temperature of described knockout tower is protected
Hold between 300 DEG C～400 DEG C.
Preferably, the catalyst described in step 3) can be alumina silicate catalyst.
The present invention passes through technique scheme, by the fuel oil that waste or used plastics catalytic pyrolysis is different quality, can be applicable to very
Multi-field, and the fuel oil response rate is high, and automaticity is effective, and input cost is relatively low, not only solves waste or used plastics to ring
The pollution in border and current waste or used plastics problems and disadvantages present in the oiling process, and bring huge economic benefit.
Compared with prior art, the equipment used in the present invention and technics comparing are advanced, and automaticity is high, need artificial
Operate less, reduce human cost, it is possible to produce continuously, improve the treatment effeciency of waste or used plastics, after cracking of waste plastics
The different material obtained processes proper, does not results in secondary pollution, has important for the present stage utilization of resources and environmental conservation
Meaning.
Accompanying drawing explanation
Below in conjunction with the accompanying drawings and embodiment, inventive feature is further described.
Fig. 1 is the square frame principle schematic diagram of the present invention.
Detailed description of the invention
Referring in accompanying drawing 1, a kind of waste or used plastics liquefying apparatus, including feed mechanism, heating furnace, fixed bed catalytic cracking tower
And knockout tower, described feed mechanism is connected with described heating furnace, and is provided with first between described feed mechanism and described heating furnace
Autocontrol valve, described first autocontrol valve is automatically switched off when leaving in stopping charging or workman, prevents liquid from flowing backwards；Institute
State heating furnace to be connected with described fixed bed catalytic cracking tower by oil pump, managed by conveying above described fixed bed catalytic cracking tower
Road is connected with described knockout tower, and lower section is connected by oil pump reduced fuel oil tank, and described fixed bed catalytic cracking tower is with described
Being additionally provided with the first cooling bath between reduced fuel oil tank, described fixed bed catalytic cracking tower outer wall is provided with catalyst and adds entrance；Described point
Being connected above condensate cooler from tower, described condensate cooler one end connects circulating water tower, and lower section connects has profit to divide
From device, described oil water separator bottom is provided with water storage bag, and described oil water separator by oil pump respectively with gasoline cistern and described
Knockout tower top is connected, and is also associated with water sealed tank above described oil water separator, and described water sealed tank is connected with described heating furnace,
And it is provided with flame-retardant device between described water sealed tank and described heating furnace；Described knockout tower side has been also respectively connected with solvent oil tank and vapour
Stripper, is provided with the second cooling bath between described knockout tower and described solvent oil tank, described stripper is connected with described diesel fuel tank, institute
State and be connected with described reduced fuel oil tank also by oil pump below knockout tower；Described oil pump is all set to double group pump.
Preferably, described fixed bed catalytic cracking tower, described knockout tower and described oil water separator side are equipped with liquid
Level sensor, and described fixed bed catalytic cracking tower, described knockout tower and described oil water separator be all provided with when being connected with oil pump
There are the second autocontrol valve, described second autocontrol valve to receive the height of liquid level signal of described liquid level sensor and control oil plant stream
The speed of speed.
Described fixed bed catalytic cracking tower is connected with the coil pipe being provided with inside described knockout tower by oil pump, and described coil pipe exists
It is connected with described first cooling bath outside described splitter column.
The present invention is realized by following steps in use:
1) waste or used plastics pretreatment: sorting-broken-clean-dry；2) heating: the waste or used plastics processed in step 1) is led to
Crossing and obtain high-temp liquid after adding heat fusing in feed mechanism feeding heating furnace, described heating furnace internal temperature in heating process is protected
Holding between 450 DEG C～480 DEG C, if conveying mechanism stopping charging or workman leave, described first autocontrol valve cuts out defeated
Sending passage, in preventing heating furnace, high-temp liquid flows backwards；3) vaporization and catalytic pyrolysis: by step 2) in the high-temp liquid that obtains pass through
Oil pump is conveyed in fixed bed catalytic cracking tower, and described fixed bed catalytic cracking tower adds catalyst, is vaporized liquid, urges
Change cracking, the gas after cracking by above described fixed bed catalytic cracking tower entrance knockout tower in, the liquid stayed after cracking
For reduced fuel oil, reduced fuel oil is delivered to the coil pipe within described knockout tower by oil pump, enters described first after heat exchange
Cooling bath, is finally delivered to reduced fuel oil tank；4) cracked gas separates: described knockout tower receives and splits from described fixed-bed catalytic
After changing the cracked gas of tower, cracked gas is separated, leads up to described condensate cooler by above described knockout tower
Lightweight component carries out condensation process, and is processed by circulating water tower cooler, then the process through oil water separator, isolated
Moisture is discharged by water storage bag, and an isolated gasoline part is sent directly into gasoline cistern by oil pump, and another part is delivered to institute
Stating above knockout tower, control described separation column temperature by the temperature of gasoline, the isolated condensed gas that is difficult to enters
Water sealed tank, eventually enters into heating furnace atomization and makees fuel；After the isolated solvent naphtha in another road makes full use of heat exchange resource, pass through
Solvent naphtha tank is entered after second cooling bath cooling；The process by stripper of 3rd tunnel, withdraws lightweight component, the diesel oil that will obtain
It is conveyed into diesel fuel tank by oil pump；4th tunnel directly carries diesel oil to described diesel fuel tank by oil pump below described knockout tower,
The internal temperature of described knockout tower is maintained between 300 DEG C～400 DEG C.
Preferably, the catalyst described in step 3) can be alumina silicate catalyst.
Described fixed bed catalytic cracking tower in use, is provided with standby fixed bed catalytic cracking tower, can be used alternatingly；Institute
State oil pump and use double group pump, as standby when that a fault or flow being bigger wherein.
The present invention passes through technique scheme, by the fuel oil that waste or used plastics catalytic pyrolysis is different quality, can be applicable to very
Multi-field, and the fuel oil response rate is high, and automaticity is effective, and input cost is relatively low, needs manual operation less, reduces
Human cost, it is possible to produce continuously, improves the treatment effeciency of waste or used plastics, not only solves the waste or used plastics pollution to environment
With current waste or used plastics problems and disadvantages present in the oiling process, and bring huge economic benefit.
In actual production, for weight fuel oil collection rate after raising waste or used plastics oiling, should lay particular stress on when collecting waste or used plastics
A certain waste or used plastics addition because PE PP PS ABS PET every kind waste or used plastics fuel-displaced be different.
As a example by 1 ton of alumina silicate catalyst, 600t oil can be catalyzed out, and this 600t oil is by 1200t cracking of waste plastics
Forming, cleavage rate reaches 50%, and the cost of 1t waste or used plastics is the lowest, but goes out 0.6 ton of oil plant by cleavable of the present invention, band
The economic benefit come is well imagined.
Described above is only presently preferred embodiments of the present invention, and above-mentioned specific embodiment is not limitation of the present invention,
Retouching, amendment or the equivalent that all those of ordinary skill in the art are made as described above, belongs to the guarantor of the present invention
Protect scope.
Claims (9)
1. a waste or used plastics liquefying apparatus, it is characterised in that: include feed mechanism, heating furnace, fixed bed catalytic cracking tower and
Knockout tower, described feed mechanism is connected with described heating furnace, and is provided with first between described feed mechanism and described heating furnace certainly
Brake control valve, described first autocontrol valve is automatically switched off when stopping charging；Described heating furnace is fixing with described by oil pump
Bed catalytic cracking tower is connected, and is connected with described knockout tower by conveyance conduit above described fixed bed catalytic cracking tower, lower square tube
Cross oil pump to connect and have between reduced fuel oil tank, and described fixed bed catalytic cracking tower and described reduced fuel oil tank and be additionally provided with the first cooling
Groove；Described knockout tower is connected above condensate cooler, and described condensate cooler one end connects circulating water tower, and lower section connects
Have oil water separator, described oil water separator bottom to be provided with water storage bag, and described oil water separator by oil pump respectively with gasoline
Tank is connected with described knockout tower top, is also associated with water sealed tank above described oil water separator, and described knockout tower side is also distinguished
Connecting has solvent oil tank and stripper, described stripper to be connected with described diesel fuel tank, below described knockout tower also by oil pump and
Described reduced fuel oil tank is connected.
Waste or used plastics liquefying apparatus the most according to claim 1, it is characterised in that: described fixed bed catalytic cracking tower, institute
State knockout tower and described oil water separator side is equipped with liquid level sensor, and described fixed bed catalytic cracking tower, described separation
Tower and described oil water separator are equipped with the second autocontrol valve with oil pump when being connected, and described second autocontrol valve receives institute
The height of liquid level signal stating liquid level sensor controls the speed of oil plant flow velocity.
Waste or used plastics liquefying apparatus the most according to claim 1, it is characterised in that: described knockout tower and described solvent oil tank
Between be provided with the second cooling bath.
Waste or used plastics liquefying apparatus the most according to claim 1, it is characterised in that: described oil pump is all set to double group pump.
Waste or used plastics liquefying apparatus the most according to claim 1, it is characterised in that: described fixed bed catalytic cracking tower outer wall
It is provided with catalyst and adds entrance.
Waste or used plastics liquefying apparatus the most according to claim 1, it is characterised in that: described water sealed tank and described heating furnace phase
Connection, and it is provided with flame-retardant device between described water sealed tank and described heating furnace.
Waste or used plastics liquefying apparatus the most according to claim 1, it is characterised in that: described fixed bed catalytic cracking tower passes through
Oil pump is connected with the coil pipe being provided with inside described knockout tower, and described coil pipe is in described splitter column outside and described first cooling bath phase
Even.
8. the technological process of a waste or used plastics liquefying apparatus, it is characterised in that comprise the following steps:
1) waste or used plastics pretreatment: sorting-broken-clean-dry；
2) heating: the waste or used plastics processed in step 1) is sent into by feed mechanism and obtains height after adding heat fusing in heating furnace
Geothermal liquid, described heating furnace internal temperature in heating process is maintained between 450 DEG C～480 DEG C, if conveying mechanism stop into
When material or workman leave, described first autocontrol valve cuts out transfer passage, and in preventing heating furnace, high-temp liquid flows backwards；
3) vaporization and catalytic pyrolysis: by step 2) in the high-temp liquid that obtains be conveyed into fixed bed catalytic cracking tower by oil pump
In, described fixed bed catalytic cracking tower adds catalyst, is vaporized liquid, catalytic pyrolysis, and the gas after cracking passes through institute
Stating and enter in knockout tower above fixed bed catalytic cracking tower, the liquid stayed after cracking is reduced fuel oil, and reduced fuel oil is by oil
Transport pump, to the coil pipe within described knockout tower, enters described first cooling bath after heat exchange, is finally delivered to reduced fuel oil
Tank；
4) cracked gas separates: described knockout tower receives after the cracked gas of described fixed bed catalytic cracking tower, to cracking
Gas separates, and the lightweight component above described knockout tower is carried out condensation process by described condensate cooler of leading up to, and
Processed by circulating water tower cooler, then the process through oil water separator, isolated moisture is discharged by water storage bag, separates
The gasoline part gone out is sent directly into gasoline cistern by oil pump, and another part is delivered to above described knockout tower, by gasoline
Temperature controls described separation column temperature, and the isolated condensed gas that is difficult to enters water sealed tank, eventually enters into heating furnace mist
It is turned into fuel；After the isolated solvent naphtha in another road makes full use of heat exchange resource, enter molten after being cooled down by the second cooling bath
Agent oil tank；The process by stripper of 3rd tunnel, withdraws lightweight component, and by oil pump, the diesel oil obtained is conveyed into diesel fuel tank；
4th tunnel directly carries diesel oil to described diesel fuel tank by oil pump below described knockout tower, and the internal temperature of described knockout tower is protected
Hold between 300 DEG C～400 DEG C.
The technological process of waste or used plastics liquefying apparatus the most according to claim 8, it is characterised in that: described in step 3)
Catalyst can be alumina silicate catalyst.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610581958.3A CN106047395A (en) | 2016-07-22 | 2016-07-22 | Equipment for turning waste plastics into oil and process flow of equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610581958.3A CN106047395A (en) | 2016-07-22 | 2016-07-22 | Equipment for turning waste plastics into oil and process flow of equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106047395A true CN106047395A (en) | 2016-10-26 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610581958.3A Pending CN106047395A (en) | 2016-07-22 | 2016-07-22 | Equipment for turning waste plastics into oil and process flow of equipment |
Country Status (1)
| Country | Link |
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| CN (1) | CN106047395A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111750358A (en) * | 2020-05-29 | 2020-10-09 | 浙江科茂环境科技有限公司 | Waste plastic green oiling technology embedded garbage incineration method |
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| CN1077479A (en) * | 1993-05-12 | 1993-10-20 | 杨先春 | Method with making hydrocarbon oil from waste polyolefine plastics |
| CN1306071A (en) * | 2000-01-17 | 2001-08-01 | 时瑞兴 | Equipment and method for preparing gasoline and diesel oil from waste plastics |
| CN201634634U (en) * | 2010-03-22 | 2010-11-17 | 景卫东 | Device for producing oil products and carbon black from scrap tires by one-step catalytic pyrolysis |
| WO2016107324A1 (en) * | 2014-12-31 | 2016-07-07 | 李伟波 | Rubber cracking and refining equipment and method |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111750358A (en) * | 2020-05-29 | 2020-10-09 | 浙江科茂环境科技有限公司 | Waste plastic green oiling technology embedded garbage incineration method |
| CN111750358B (en) * | 2020-05-29 | 2021-09-10 | 浙江科茂环境科技有限公司 | Waste plastic green oiling technology embedded garbage incineration method |
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