CN105861018B - Waste plastics refining unit - Google Patents
Waste plastics refining unit Download PDFInfo
- Publication number
- CN105861018B CN105861018B CN201610313787.6A CN201610313787A CN105861018B CN 105861018 B CN105861018 B CN 105861018B CN 201610313787 A CN201610313787 A CN 201610313787A CN 105861018 B CN105861018 B CN 105861018B
- Authority
- CN
- China
- Prior art keywords
- reactor
- kettle
- interior kettle
- rotating disk
- layer
- 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.)
- Expired - Fee Related
Links
- 239000004033 plastic Substances 0.000 title claims abstract description 28
- 229920003023 plastic Polymers 0.000 title claims abstract description 28
- 238000007670 refining Methods 0.000 title claims abstract description 28
- 239000002699 waste material Substances 0.000 title claims abstract description 20
- 238000007599 discharging Methods 0.000 claims abstract description 21
- 238000010438 heat treatment Methods 0.000 claims abstract description 17
- 238000009413 insulation Methods 0.000 claims abstract description 16
- 238000005253 cladding Methods 0.000 claims abstract description 5
- 239000011810 insulating material Substances 0.000 claims abstract description 4
- 238000003756 stirring Methods 0.000 claims description 45
- 239000003921 oil Substances 0.000 description 37
- 238000007789 sealing Methods 0.000 description 9
- 239000011257 shell material Substances 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 238000012545 processing Methods 0.000 description 3
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 241000707825 Argyrosomus regius Species 0.000 description 1
- 241001062472 Stokellia anisodon Species 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009933 burial Methods 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000007233 catalytic pyrolysis Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 238000009940 knitting Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Classifications
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- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0006—Controlling or regulating processes
- B01J19/0013—Controlling the temperature of the process
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0053—Details of the reactor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0053—Details of the reactor
- B01J19/0066—Stirrers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J4/00—Feed or outlet devices; Feed or outlet control devices
- B01J4/001—Feed or outlet devices as such, e.g. feeding tubes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J6/00—Heat treatments such as Calcining; Fusing ; Pyrolysis
- B01J6/008—Pyrolysis reactions
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00087—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/0015—Controlling the temperature by thermal insulation means
-
- 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
Abstract
The invention discloses a kind of waste plastics refining unit, including feed arrangement, oil discharging device and reactor, feed arrangement and oil discharging device are connected with reactor, feed arrangement is arranged on the upper end of the reactor, the oil discharging device is arranged on the lower end of reactor, reactor is Double-layer vertical tank body, reactor includes interior kettle and external kettle body, one layer of heater of external kettle body outer cladding, heater includes shell, zone of heating and heat-insulation layer are provided with shell, one layer of insulating materials is coated on the contact surface of zone of heating and heat-insulation layer, heater is fixed on external kettle body outer wall；Some outages are uniformly placed with the wall of interior kettle, the upper end of interior kettle is connected with rotating disk, rotating disk center drives interior kettle to rotate after being provided with a through hole, rotating disk connection motor；Agitating device is installed with reactor, the oil refining apparatus is provided with rotatable, so as to save more resources, reduces cost.
Description
Technical field
The invention belongs to oil Refining Technologies field, it is related to a kind of oil refining apparatus, more particularly to a kind of refining for waste or used plastics
Oily device.
Background technology
In recent years, with the growth in the living standard of people, various plastic products use more and more；White pollution is more next
It is more serious, in China, waste plastic main source have plastic sheeting, plastic wire and knitting, foamed plastics, plastic package box and
Container, various daily plastic products, diversiform polybag and meagre agricultural mulching etc..The processing side of current plastic garbage
Method is mainly burial, burning, and these methods cause serious environmental pollution.Garbage as resource problem by extensive concern, why
Harmful Waste (waste or used plastics) are changed into efficient resource by sample, it has also become environmentalist, chemical industry expert, biological expert and economy
The popular problem of sociologist's research.
Current people have developed a variety of plastics refining equipments；Waste or used plastics can be smelt oil；Its original of waste plastic oil-refining
Reason is exactly the method for taking catalytic pyrolysis, is acted under the high temperature conditions through extraordinary catalytic pyrolyzing agent, makes the macromolecular chain rupture cracking be
The molecule of very little；I.e. waste plastics pyrolysis is exactly the inverse process that oil manufactures plastics for raw material.In the recovery profit of waste or used plastics
With in technology, the technology for refining fuel oil using cracking of waste plastics is approved by people, and it is gradually expanded come, it is but existing
Vertical tank reactor in technology waste plastic oil-refining equipment, its dischargeable capacity and heating surface area are limited, and temperature is unstable, heating effect
It is really poor, stir uneven, cause the oil yield of existing oil refining apparatus not high, and dregs of fat processing is complicated.
The content of the invention
The technical problem to be solved in the present invention is to provide a kind of scientific and reasonable for structure, operation and facilitates, is heated evenly, stirring
Uniformly, efficiency high and suitable for industrial mass production waste plastics refining unit.
In order to solve the above technical problems, the technical solution adopted by the present invention is：The waste plastics refining unit includes charging and filled
Put, oil discharging device and reactor, the feed arrangement and oil discharging device are connected with the reactor, and the feed arrangement is set
Put in the upper end of the reactor, the oil discharging device is arranged on the lower end of the reactor, the reactor is Double-layer vertical
Tank body, the reactor includes interior kettle and external kettle body, described one layer of heater of external kettle body outer cladding, the heater bag
Include and one layer of insulation of coating on zone of heating and heat-insulation layer, the contact surface of the zone of heating and heat-insulation layer is provided with shell, the shell
Material, the heater is fixed on external kettle body outer wall；Some outages are uniformly placed with the wall of the interior kettle, it is described
The upper end of interior kettle is connected with rotating disk, and the rotating disk center drives interior kettle after being provided with a through hole, the rotating disk connection motor
Rotate；Agitating device is installed with the reactor, the agitating device includes agitating paddle, and the agitating paddle includes vertical
Stirring main shaft, the upper end of the stirring main shaft is connected with motor, and the stirring main shaft is at the top of the interior kettle through described
Rotating disk through hole and interior kettle enter in the interior kettle, and positioned at the bottom of the interior kettle；The stirring main shaft is opened from bottom
The upward equi-spaced apart that begins is provided with multiple horizontal stirring rod.
Using above-mentioned technical proposal, rotated by interior kettle, oil can be discharged from the outage of interior kettle, and the dregs of fat are stayed
In interior kettle, it is directly realized and handles the dregs of fat in oil refining, reduce technique, so as to economize on resources, reduce cost；By
The outer wall of reactor, which is set in heater, heater, zone of heating and heat-insulation layer, can make being uniformly heated for reactor,
Convenient maintenance simultaneously；Temperature control is shown and temperature control device can control the temperature in reactor, is integrated into the kettle of reactor
Type set, temperature control device through kettle enter kettle in, using such structure can strengthen the reactor sealing property and
The thorough seal of kettle is realized, stirring main shaft adds mixing direction provided with multiple horizontal stirring rod in bottom, can improve and stir
Mix efficiency so that the stirring of whole kettle is evenly.
Further improvement is that, the bottom of the reactor is provided with dregs of fat storing unit, can increase the amount of storage of the dregs of fat.
Further improvement is that, the bottom of the stirring main shaft, which is extended downwardly, is transversely provided with baffle plate.Set baffle plate can be to prevent
Only the dregs of fat are deposited in reactor bottom, it is to avoid form accumulation dead angle, the dregs of fat can be helped to enter dregs of fat storing unit, further carried
Height oil refining efficiency.
Further improvement is that, the connection of the feed arrangement, oil discharging device and dregs of fat storing unit and the reactor
Sealing ring and insulation ring are provided with position.Such setting can improve the sealing property and heat conductivility of the oil refining apparatus,
So as to improve the efficiency of oil refining.
Further improvement is that, the stirring main shaft and the junction of the kettle are provided with sealing structure.It is such to set
The sealing property of reactor can preferably be improved.
Further improvement is that, the bottom of the dregs of fat storing unit can be with slide-open.Such setting can be cleared up
The dregs of fat of storage.
Further improvement is that, the end of the horizontal stirring rod is provided with scraper.Set scraper can oil refining when and
Grease on Shi Qingli oil refining cabinet walls, improves oil refining efficiency.
Further improvement is that, filter is provided with the oil discharging device.The purity of oil can further be improved.
Compared with the prior art, the invention has the advantages that：Interior kettle is set to rotatable and at it by the oil refining apparatus
It is upper to be provided with outage, so as to the direct oil extraction side processing dregs of fat in oil refining, more resources are saved, cost are reduced, together
When its reactor good heat conductivity, the thermal efficiency is high, environment friendly and pollution-free can be in close contact with heating object；Heating is more equal
Even, device for simultaneous heating more facilitates maintenance, increases the service life；Stirring main shaft is in bottom provided with multiple horizontal stirring rod increases
Mixing direction, can improve stirring efficiency so that the stirring of whole kettle is evenly.
Brief description of the drawings
It is further described below in conjunction with the accompanying drawings with embodiments of the present invention：
Fig. 1 is the structural representation of waste plastics refining unit of the present invention；
Wherein：1- reactors；Kettle in 101-；1011- outages；102- external kettle bodies；2- heaters；201- shells；
202- zones of heating；203- heat-insulation layers；3- agitating devices；301- stirring main shafts；302- transverse direction stirring rod；303- scrapers；4- motors；
5- temperature controls are shown；6- baffle plates；7- feed arrangements；8- oil discharging devices；9- dregs of fat storing units；10 rotating disks.
Embodiment
Embodiment one：The waste plastics refining unit includes feed arrangement 7, oil discharging device 8 and reactor 1, the He of feed arrangement 7
Oil discharging device 8 is connected with reactor 1, and feed arrangement 7 is arranged on the upper end of reactor 1, and oil discharging device 8 is arranged on reactor
1 lower end, reactor 1 is vertical tank body, and reactor 1 includes interior kettle 101 and external kettle body 102, one layer of 102 outer cladding of external kettle body
Heater 2, heater 2 includes shell 201, is provided with zone of heating 202 and heat-insulation layer 203 in shell 201, zone of heating 202 with
One layer of insulating materials is coated on the contact surface of heat-insulation layer 203, heater 2 is fixed on the outer wall of external kettle body 102；Interior kettle
Outage 1011 uniformly is placed with 101 wall, the upper end of interior kettle 101 is connected with rotating disk 10, the center of rotating disk 10 is provided with one
Kettle 101 is rotated in being driven after through hole, the connection motor 4 of rotating disk 10；Agitating device 3, agitating device are installed with reactor 1
3 include agitating paddle, and agitating paddle includes vertical stirring main shaft 301, and the upper end of stirring main shaft 301 is connected with motor 4 and temperature control is aobvious
Show 5, stirring main shaft 301 enters in interior kettle 101 from the interior top of kettle 101 through the through hole and interior kettle 101 of rotating disk 10, and position
In the bottom of interior kettle 101；The upward equi-spaced apart since bottom of stirring main shaft 301 is provided with 5 horizontal stirring rod 302；Temperature control
Display 5 is connected with temperature control device；Temperature control device is located in stirring main shaft；The company of oil feeding device 7 and oil discharging device 8 and reactor 1
Connect and sealing ring and insulation ring are provided with position；Stirring main shaft 301 and the junction of kettle are provided with sealing structure；Horizontal stirring rod
302 end is provided with scraper 303；The bottom of stirring main shaft 301, which is extended downwardly, is transversely provided with baffle plate 6；It is provided with oil discharging device 8
Filter.
Embodiment two：As shown in figure 1, being with the difference of embodiment one, the waste plastics refining unit also includes the dregs of fat
Storing unit；Specific as follows, the waste plastics refining unit includes feed arrangement 7, oil discharging device 8 and reactor 1, feed arrangement 7
It is connected with oil discharging device 8 with reactor 1, feed arrangement 7 is arranged on the upper end of reactor 1, oil discharging device 8 is arranged on reaction
The lower end of kettle 1, reactor 1 is vertical tank body, and reactor 1 includes interior kettle 101 and external kettle body 102, the outer cladding one of external kettle body 102
Layer heater 2, heater 2 includes being provided with zone of heating 202 and heat-insulation layer 203, zone of heating 202 in shell 201, shell 201
With coating one layer of insulating materials on the contact surface of heat-insulation layer 203, heater 2 is fixed on the outer wall of external kettle body 102；Interior kettle
Outage 1011 uniformly is placed with 101 wall, the upper end of interior kettle 101 is connected with rotating disk 10, the center of rotating disk 10 is provided with one
Kettle 101 is rotated in being driven after through hole, the connection motor 4 of rotating disk 10；Agitating device 3, agitating device are installed with reactor 1
3 include agitating paddle, and agitating paddle includes vertical stirring main shaft 301, and the upper end of stirring main shaft 301 is connected with motor 4 and temperature control is aobvious
Show 5, stirring main shaft 301 enters in interior kettle 101 from the interior top of kettle 101 through the through hole and interior kettle 101 of rotating disk 10, and position
In the bottom of interior kettle 101；The upward equi-spaced apart since bottom of stirring main shaft 301 is provided with 5 horizontal stirring rod 302；Temperature control
Display 5 is connected with temperature control device；Temperature control device is located in stirring main shaft；The bottom of reactor 1 is provided with dregs of fat storing unit 9；Oil
Slag storing unit 9 is beaten with being only connected with interior kettle 101, and provided with its connection of switch control when needing connection by switch
The bottom of interior kettle 101 is opened, dregs of fat storing unit 9 is connected with interior kettle 101；The bottom of dregs of fat storing unit 9 can be with
Slide-open, when dregs of fat storing unit 9 is filled with the dregs of fat, then the bottom that can open dregs of fat storing unit 9 is cleared up；Oil-feed is filled
7, oil discharging device 8 and dregs of fat storing unit 9 are put with being provided with sealing ring and insulation ring at the link position of reactor 1；Stirring main shaft
301 are provided with sealing structure with the junction of kettle；The end of horizontal stirring rod 302 is provided with scraper 303；Stirring main shaft 301
Bottom, which is extended downwardly, is transversely provided with baffle plate 6；Filter is provided with oil discharging device 8.
In the present invention when needing internal kettle 101 to be rotated, just rotating disk 10 is connected simultaneously with motor 4, oil extraction
Hole 1011 is provided with guard；It can play a role in filtering.
Particular embodiments described above, has been carried out further in detail to the purpose of the present invention, technical scheme and beneficial effect
Describe in detail it is bright, should be understood that the foregoing is only the present invention specific embodiment, be not intended to limit the invention；It is all
Within the spirit and principles in the present invention, any modification, equivalent substitution and improvements done etc., should be included in the guarantor of the present invention
Within the scope of shield.
Claims (1)
1. a kind of waste plastics refining unit, including feed arrangement, oil discharging device and reactor, it is characterised in that the charging dress
Put and be connected with oil discharging device with the reactor, the feed arrangement is arranged on the upper end of the reactor, described fuel-displaced
Device is arranged on the lower end of the reactor, and the reactor is Double-layer vertical tank body, and the reactor includes interior kettle and outer
Kettle, described one layer of heater of external kettle body outer cladding, the heater includes shell, in the shell provided with zone of heating and
One layer of insulating materials is coated on heat-insulation layer, the contact surface of the zone of heating and heat-insulation layer, the heater is fixed on external kettle body
On outer wall；Some outages are uniformly placed with the wall of the interior kettle, the upper end of the interior kettle is connected with rotating disk, described turn
Disk center drives interior kettle to rotate after being provided with a through hole, the rotating disk connection motor；Stirring is installed with the reactor
Device, the agitating device includes agitating paddle, and the agitating paddle includes vertical stirring main shaft, and the upper end of the stirring main shaft connects
Motor is connected to, the stirring main shaft is originated at the top of the interior kettle and entered through the rotating disk through hole in interior kettle, stirring
Main the tip of the axis extends to the bottom of the interior kettle；The stirring main shaft upward equi-spaced apart since bottom is provided with multiple horizontal strokes
To stirring rod；Outage is provided with guard；The bottom of the reactor is provided with dregs of fat storing unit.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610313787.6A CN105861018B (en) | 2015-06-07 | 2015-06-07 | Waste plastics refining unit |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610313787.6A CN105861018B (en) | 2015-06-07 | 2015-06-07 | Waste plastics refining unit |
| CN201510303190.9A CN104862001B (en) | 2015-06-07 | 2015-06-07 | Waste plastics refining unit |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510303190.9A Division CN104862001B (en) | 2015-06-07 | 2015-06-07 | Waste plastics refining unit |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105861018A CN105861018A (en) | 2016-08-17 |
| CN105861018B true CN105861018B (en) | 2017-08-01 |
Family
ID=53908191
Family Applications (5)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510303190.9A Active CN104862001B (en) | 2015-06-07 | 2015-06-07 | Waste plastics refining unit |
| CN201610313784.2A Active CN105861016B (en) | 2015-06-07 | 2015-06-07 | Waste plastics refining unit |
| CN201610313786.1A Expired - Fee Related CN105861017B (en) | 2015-06-07 | 2015-06-07 | Waste plastics refining unit |
| CN201610313787.6A Expired - Fee Related CN105861018B (en) | 2015-06-07 | 2015-06-07 | Waste plastics refining unit |
| CN201610313785.7A Pending CN105885908A (en) | 2015-06-07 | 2015-06-07 | Waste plastic oil refining device |
Family Applications Before (3)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510303190.9A Active CN104862001B (en) | 2015-06-07 | 2015-06-07 | Waste plastics refining unit |
| CN201610313784.2A Active CN105861016B (en) | 2015-06-07 | 2015-06-07 | Waste plastics refining unit |
| CN201610313786.1A Expired - Fee Related CN105861017B (en) | 2015-06-07 | 2015-06-07 | Waste plastics refining unit |
Family Applications After (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610313785.7A Pending CN105885908A (en) | 2015-06-07 | 2015-06-07 | Waste plastic oil refining device |
Country Status (1)
| Country | Link |
|---|---|
| CN (5) | CN104862001B (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105251415A (en) * | 2015-09-18 | 2016-01-20 | 丹阳市助剂化工厂有限公司 | Esterification apparatus |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20110306808A1 (en) * | 2003-03-28 | 2011-12-15 | Ab-Cwt, Llc | Process For Conversion of Organic, Waste, or Low-Value Materials Into Useful Products |
| CN203582810U (en) * | 2013-09-10 | 2014-05-07 | 扬中市金元化工电力设备厂 | Waste plastic oil refining device |
Family Cites Families (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH08170081A (en) * | 1994-12-20 | 1996-07-02 | Toshiba Eng & Constr Co Ltd | Processing unit for converting waste plastic material into oil and conversion into oil |
| CN1070526C (en) * | 1997-10-13 | 2001-09-05 | 刘和生 | Wet oil refining process utilizing waste plastics and its vaporizer |
| CN2506643Y (en) * | 2001-09-06 | 2002-08-21 | 四川大学 | Oil refining equipment from waste and used plastics |
| CN2579895Y (en) * | 2002-11-07 | 2003-10-15 | 马军 | High temperature slag discharge device for waste plastic electric heating cracking oil |
| CN2666914Y (en) * | 2004-01-09 | 2004-12-29 | 严绥 | Apparatus for cracking waste plastics to produce oil products |
| CN201116299Y (en) * | 2007-09-13 | 2008-09-17 | 党德润 | Industrialization waste plastic oil refining reaction still |
| KR20120080158A (en) * | 2009-06-19 | 2012-07-16 | 이노베이티브 에너지 솔루션즈 인코포레이티드 | Thermo-catalytic cracking for conversion of higher hydrocarbons into lower hydrocarbons |
| CN103468297A (en) * | 2013-09-10 | 2013-12-25 | 扬中市金元化工电力设备厂 | Waste plastic oil refining device |
| CN204752622U (en) * | 2015-06-07 | 2015-11-11 | 浙江海洋学院 | Waste plastic oil refining device |
-
2015
- 2015-06-07 CN CN201510303190.9A patent/CN104862001B/en active Active
- 2015-06-07 CN CN201610313784.2A patent/CN105861016B/en active Active
- 2015-06-07 CN CN201610313786.1A patent/CN105861017B/en not_active Expired - Fee Related
- 2015-06-07 CN CN201610313787.6A patent/CN105861018B/en not_active Expired - Fee Related
- 2015-06-07 CN CN201610313785.7A patent/CN105885908A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20110306808A1 (en) * | 2003-03-28 | 2011-12-15 | Ab-Cwt, Llc | Process For Conversion of Organic, Waste, or Low-Value Materials Into Useful Products |
| CN203582810U (en) * | 2013-09-10 | 2014-05-07 | 扬中市金元化工电力设备厂 | Waste plastic oil refining device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105861017A (en) | 2016-08-17 |
| CN104862001A (en) | 2015-08-26 |
| CN105861017B (en) | 2017-10-20 |
| CN104862001B (en) | 2016-08-17 |
| CN105861016A (en) | 2016-08-17 |
| CN105861016B (en) | 2018-01-16 |
| CN105885908A (en) | 2016-08-24 |
| CN105861018A (en) | 2016-08-17 |
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