CN103739874B - A kind of waste or used plastics extracts Tissuemat E system - Google Patents
A kind of waste or used plastics extracts Tissuemat E system Download PDFInfo
- Publication number
- CN103739874B CN103739874B CN201310744724.2A CN201310744724A CN103739874B CN 103739874 B CN103739874 B CN 103739874B CN 201310744724 A CN201310744724 A CN 201310744724A CN 103739874 B CN103739874 B CN 103739874B
- Authority
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- China
- Prior art keywords
- section
- extruder
- waste
- tissuemat
- extracts
- 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
- 239000002699 waste material Substances 0.000 title claims abstract description 20
- 239000004033 plastic Substances 0.000 title claims abstract description 15
- 229920003023 plastic Polymers 0.000 title claims abstract description 15
- 239000000284 extract Substances 0.000 title claims abstract description 9
- 238000001816 cooling Methods 0.000 claims abstract description 22
- 238000002156 mixing Methods 0.000 claims abstract description 20
- 238000010438 heat treatment Methods 0.000 claims abstract description 9
- 238000002485 combustion reaction Methods 0.000 claims abstract description 7
- 238000007789 sealing Methods 0.000 claims abstract description 6
- 239000003054 catalyst Substances 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 230000009466 transformation Effects 0.000 abstract description 2
- 239000000047 product Substances 0.000 description 5
- 238000003912 environmental pollution Methods 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000001993 wax Substances 0.000 description 3
- 239000004698 Polyethylene Substances 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000001125 extrusion Methods 0.000 description 2
- -1 polyethylene Polymers 0.000 description 2
- 229920000573 polyethylene Polymers 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 239000003502 gasoline Substances 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- 239000003348 petrochemical agent Substances 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 239000013502 plastic waste Substances 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000012744 reinforcing agent Substances 0.000 description 1
- 230000000192 social effect Effects 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
Classifications
-
- 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
Landscapes
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
A kind of waste or used plastics extracts Tissuemat E system, including: extruder, described extruder is connected with cooling system, caisson by sealing pipeline, described extruder is divided into feed zone, the first transportation section, the first mixing section, the second transportation section, the second mixing section, first exhaust section, the 3rd mixing section, second exhaust section, the 3rd transportation section, deslagging section, described extruder is double screw extruder, and described double screw extruder outer layer is provided with combustion heating layer.The transformation efficiency of Tissuemat E can be improved owing to present invention uses this structure, reduce thermal waste, reduce production cost.
Description
Technical field
The present invention relates to a kind of technics of reclaim of plastic waste and utilize system, particularly relate to a kind of waste or used plastics and extract Tissuemat E system.
Background technology
Tissuemat E is petrochemicals, is widely used as lubricant and the reinforcing agent of rubber, the pigment dispersing agent in plastic processing and brightener, and paper industry is used for improving the anti-stick page purposes of paper surface gloss, hardness, and paper.Utilize preparing polyethylene wax from waste plastic for the waste and old utilization of resources, eliminate white pollution, environmental protection there is important economy, social effect.
Tissuemat E has nontoxic, non-corrosiveness, hardness compared with feature big, that softening point is high, melting viscosity is low.There is good moisture resistance, chemical-resistant, electric property and antiwear heat resisting performance at normal temperatures.And lubricity, dispersiveness, good fluidity.Purposes is quite varied, particularly after micronization processes.Yield at China's polyethylene wax micro mist can not meet far away the needs in market at present, and substantial amounts of import can only be relied on to supplement, and its price is the highest.
It is " batch reactor " that the waste or used plastics that existing market is popular extracts the process equipment great majority of Tissuemat E, and thermal waste is serious, and conversion ratio is low, and product is uncontrollable, and cost is high.Due to open-sky technique, environmental pollution is serious, the most disabled.
Summary of the invention
The present invention provides a kind of waste or used plastics to extract Tissuemat E system, can improve the transformation efficiency of Tissuemat E, reduce thermal waste, reduce production cost.
The present invention is achieved by the following technical solutions:
A kind of waste or used plastics extracts Tissuemat E system, including: extruder, described extruder is connected with cooling system, caisson by sealing pipeline, and described extruder is divided into feed zone, the first transportation section, the first mixing section, the second transportation section, the second mixing section, first exhaust section, the 3rd mixing, second exhaust section, the 3rd transportation section, deslagging section；Described extruder is double screw extruder, and described double screw extruder outer layer is provided with combustion heating layer；
Described extruder at least includes 3 mixing sections；
If described cooling system includes pipeline and the dry cooling tower being arranged side by side being connected with pipeline, in described cooling tower, it is provided with the condenser pipe of cross-helicity structure；
Described cooling tower is 4；
Described extruder is arranged over catalyst change device.
In sum, the twin-screw extrusion equipment that employs of the invention thoroughly instead of old-fashioned batch reactor, make mixing more abundant, described cooling tower interior condenser tube is because have employed cross-helicity structure, the effect of cooling is more preferable, reduce the volume of cooling tower, decrease use space.After the waste gas burning produced, its heat can recycle, and decreases environmental pollution, has saved the energy.Additionally present configuration is simple, easily produces, invests little, saves operation fund.Produce Tissuemat E with waste or used plastics for raw material simultaneously, can solve domestic with polyvinyl resin for raw material to produce the problem that Tissuemat E technical costs is high.
Accompanying drawing explanation
Fig. 1 is present configuration simplified schematic diagram
Fig. 2 is extruder structure sketch of the present invention
In figure: 1, feed zone；2, the first transportation section；3, the first mixing section；4, the second transportation section；5, the second mixing section；6 first exhaust sections；7, the 3rd mixing section；8, second exhaust section；9, the 3rd transportation section；10, deslagging section 11, combustion heating layer 12, sealing pipeline 13, catalyst change device 14, cooling tower 15, condenser 16, vavuum pump 17, caisson 18, extruder 19 spout 20, cooling system.
Detailed description of the invention
As shown in Figure 1 and Figure 2, a kind of waste or used plastics extracts Tissuemat E system, including: extruder 18, described extruder 18 is connected with cooling system 20, caisson 17 by sealing pipeline 12.Described extruder 18 is divided into the 2, first mixing section the 3, second transportation section, feed zone the 1, first transportation section the 4, second mixing section 5, first exhaust section the 6, the 3rd mixing section 7, second exhaust section the 8, the 3rd transportation section 9, deslagging section 10；Described extruder 18 is double screw extruder, and described double screw extruder outer layer is provided with combustion heating layer 11；
Described extruder at least includes 3 mixing sections；
If described cooling system includes pipeline and the dry cooling tower 14 being arranged side by side being connected with pipeline, described cooling tower 14 interior condenser tube 15 is cross-helicity structure；
Described cooling tower 14 is 4；
Described extruder 18 is arranged over catalyst change device 13.
Waste or used plastics is entered extruder 18 by spout 20, waste or used plastics passes through three mixing sections in extruder 18, mixing, crack in extruder 18 exhaust ports moment after heating, the waste residue that can not crack is discharged to deslagging section 10 by Screw Extrusion, after being catalyzed by catalyst-assembly after gasification, the different product of generation is progressively cooled down such as: Tissuemat E by sealing pipeline entrance cooling tower 14, soft wax, dissolved oil etc., residual air generates liquefied gas after being entered air storage chamber by vavuum pump 16, liquefied gas is pipelined to the combustion heating layer of leading portion double screw extruder to its combustion heating, recycle.
The present invention can produce saving heating energy source continuously, moment cracking reduces equipment occupation space, system is totally-enclosed, non-environmental-pollution.Material 100 converts, and produces without the three wastes.And can be selected for corresponding catalyst, orientation cracking is converted into the product of the applicable market demand.I.e. in the products such as paraffin, diesel oil, gasoline and liquefied gas, orientation expands the proportion of certain product artificially.
Claims (2)
1. a waste or used plastics extracts Tissuemat E system, including: extruder, it is characterized in that, described extruder is connected with cooling system, caisson by sealing pipeline, described extruder is divided into feed zone, the first transportation section, the first mixing section, the second transportation section, the second mixing section, first exhaust section, the 3rd mixing section, second exhaust section, the 3rd transportation section, deslagging section, described extruder is double screw extruder, and described double screw extruder outer layer is provided with combustion heating layer；If described cooling system includes pipeline and the dry cooling tower being arranged side by side being connected with pipeline, in described cooling tower, it is provided with the condenser pipe of cross-helicity structure；Described extruder is arranged over catalyst change device.
A kind of waste or used plastics the most according to claim 1 extracts Tissuemat E system, and described cooling tower is 4.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310744724.2A CN103739874B (en) | 2013-12-31 | 2013-12-31 | A kind of waste or used plastics extracts Tissuemat E system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310744724.2A CN103739874B (en) | 2013-12-31 | 2013-12-31 | A kind of waste or used plastics extracts Tissuemat E system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103739874A CN103739874A (en) | 2014-04-23 |
| CN103739874B true CN103739874B (en) | 2016-08-24 |
Family
ID=50496951
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310744724.2A Expired - Fee Related CN103739874B (en) | 2013-12-31 | 2013-12-31 | A kind of waste or used plastics extracts Tissuemat E system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103739874B (en) |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102205620A (en) * | 2011-04-15 | 2011-10-05 | 北京化工大学 | Differential-speed conical twin-screw extruder |
| CN203668288U (en) * | 2013-12-31 | 2014-06-25 | 青岛大有电力环保设备有限公司 | System for extracting polyethylene wax from waste plastic |
-
2013
- 2013-12-31 CN CN201310744724.2A patent/CN103739874B/en not_active Expired - Fee Related
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102205620A (en) * | 2011-04-15 | 2011-10-05 | 北京化工大学 | Differential-speed conical twin-screw extruder |
| CN203668288U (en) * | 2013-12-31 | 2014-06-25 | 青岛大有电力环保设备有限公司 | System for extracting polyethylene wax from waste plastic |
Also Published As
| Publication number | Publication date |
|---|---|
| CN103739874A (en) | 2014-04-23 |
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| Date | Code | Title | Description |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| CB03 | Change of inventor or designer information |
Inventor after: Chen Zhaokun Inventor before: Han Fengwen |
|
| COR | Change of bibliographic data | ||
| GR01 | Patent grant | ||
| TA01 | Transfer of patent application right |
Effective date of registration: 20160801 Address after: 266300 Shandong, Qingdao, Jiaozhou, No. 39, Tong Jie Street Applicant after: Wu Huiliang Address before: 266300 Jiaozhou City, Shandong, Qingdao Applicant before: QINGDAO DAYOU POWER ENVIRONMENTAL PROTECTION EQUIPMENT CO.,LTD. |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20170719 Address after: 266300, Shandong, Qingdao province Jiaozhou glue North Street Office East Yong Village Patentee after: Qingdao Bao Zhi plastic material Co.,Ltd. Address before: 266300 Shandong, Qingdao, Jiaozhou, No. 39, Tong Jie Street Patentee before: Wu Huiliang |
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| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190902 Address after: Take the door street in Jiaozhou City, Shandong province 266300 Qingdao City No. 39 Patentee after: Wu Huiliang Address before: 266300 Dongyong Village, Jiaobei Street Office, Qingdao City, Shandong Province Patentee before: Qingdao Bao Zhi plastic material Co.,Ltd. |
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| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160824 Termination date: 20211231 |