CN101912758B - V-shaped reaction kettle - Google Patents
V-shaped reaction kettle Download PDFInfo
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- CN101912758B CN101912758B CN201010243437XA CN201010243437A CN101912758B CN 101912758 B CN101912758 B CN 101912758B CN 201010243437X A CN201010243437X A CN 201010243437XA CN 201010243437 A CN201010243437 A CN 201010243437A CN 101912758 B CN101912758 B CN 101912758B
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- conversion zone
- deferent segment
- type reactor
- reaction kettle
- mass percent
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Abstract
The invention discloses a device for separating aluminum and plastics, and particularly discloses a V-shaped reaction kettle. The V-shaped reaction kettle is characterized by comprising a V-shaped body mounted on a bracket, wherein the V-shaped body consists of a reaction section and an output section, the upper end of the reaction section is provided with a feed inlet and a liquid inlet, the reaction section contains liquid medicine and is equipped with a heat-insulation layer, the top end of the output section is provided with a discharge port and is internally provided with an emptying auger connected with a motor and a speed reducer, and a cooling layer is installed on the output section. By the V-shaped reaction kettle, aluminum-plastic composite material is separated through reaction, so that plastic film and aluminum foil can be completely separated, and recycled plastic after sorting can be produced into plastic particles which have wide purpose, the aluminum foil also can be reutilized, meanwhile, the daily treatment amount is big, and is increased to 100 ton from the current 30 ton, and the V-shaped reaction kettle has the advantages of energy conservation, low noise and convenient maintenance.
Description
(1) technical field
The present invention relates to a kind of aluminum-plastic separation device, particularly a kind of V-type reactor.
(2) background technology
development along with society, the plastic-aluminum product is because its superior performance and good quality, be favourably welcome, little packing box to milk, packing of capsule etc., large to door and window and engineering plastic-steel support, but in a single day the product of these plastic-aluminums is scrapped, be difficult to recycle, such as, milk package box, all disposable, if can not recycle, not only waste resource, and discarded object is difficult to decompose, process by approach such as burnings and also do not meet environmental requirement, present aluminum-plastic separation equipment can be processed at most 30 tons of useless bags every day, also do not reach the requirement of processing far away, so some aluminum-plastic separation enterprise increasing existing equipment treating capacities blindly, improve workman's working time, strengthen workman's workload, not only affect workman's physical and mental health, and existing equipment is damaged serious, and it is totally not thorough to cause plastic foil to separate with aluminium foil.
(3) summary of the invention
The present invention provides a kind for the treatment of capacity large V-type reactor in order to make up the defective of prior art.
The present invention is achieved through the following technical solutions:
A kind of V-type reactor is characterized in that: comprise rack-mount V-type body, the V-type body comprises conversion zone and deferent segment, and the conversion zone upper end is provided with charging aperture and inlet, fills liquid in conversion zone, and heat-insulation layer is installed on conversion zone; The top of deferent segment is provided with discharging opening, is provided with the emptying auger that is connected with motor and reductor in deferent segment, and cooling layer is installed on deferent segment.
This V-type reactor, the angle of conversion zone and horizontal plane are 30 °, and the angle of deferent segment and horizontal plane is 60 °; Charging aperture place, top is equipped with feeding machine in conversion zone, and deferent segment top discharging opening downside is provided with liquid spill-way, and the junction of deferent segment bottom and conversion zone is provided with sewage draining exit; Described liquid comprises that mass percent is that 85% formic acid, mass percent are 95% carrene and water, and in described liquid, the shared ratio of each composition is:
Mass percent is that 85% formic acid is 12%～15%;
Mass percent is that 95% carrene is 2%～4%;
Water is 81%～86%.
The invention has the beneficial effects as follows: this V-type reactor, aluminium plastic composite material is broken away from through reaction, plastic foil is thoroughly separated with aluminium foil, the plastics that reclaim after sorting can produce plastic grain, regenerated granule is had many uses, and aluminium foil also can regeneration, and day output is large simultaneously, by being converted to 100 tons 30 tons of existing every days, and have advantages of energy-conservation, noise is low, easy to maintenance.
(4) description of drawings
The present invention is further illustrated below in conjunction with accompanying drawing.
Accompanying drawing 1 is the structural representation of V-type reactor of the present invention.
In figure, 1 charging aperture, 2V type body, 3 discharging openings, 4 supports, 5 emptying augers, 6 feeding machines, 7 motors and reductor, 8 liquid spill-ways, 9 sewage draining exits, 10 inlets, 11 heat-insulation layers, 12 cooling layers, 13 conversion zones, 14 deferent segments.
(5) specific embodiment
Embodiment 1:
Accompanying drawing is a kind of specific embodiment of the present invention.This V-type reactor is characterized in that: comprise the V-type body 2 that is arranged on support 4, V-type body 2 comprises conversion zone 13 and deferent segment 14, and conversion zone 13 upper ends are provided with charging aperture 1 and inlet 10, fill liquid in conversion zone 13, and heat-insulation layer 11 is installed on conversion zone 13; The top of deferent segment 14 is provided with discharging opening 3, is provided with the emptying auger 5 that is connected with motor and reductor 7 in deferent segment 14, and cooling layer 12 is installed on deferent segment 14.Conversion zone 13 is 30 ° with the angle of horizontal plane, and deferent segment 14 is 60 ° with the angle of horizontal plane; Charging aperture 1 place, the interior top of conversion zone 13 is equipped with feeding machine 6, and deferent segment 14 top discharging opening 3 downsides are provided with liquid spill-way 8, and the junction of deferent segment 14 bottoms and conversion zone 13 is provided with sewage draining exit 9; Described liquid comprises that mass percent is that 85% formic acid, mass percent are 95% carrene and water, and in described liquid, the shared ratio of each composition is: mass percent is that 85% formic acid is 12%; Mass percent is that 95% carrene is 2%; Water is 86%.
This V-type reactor, during use, in charging aperture 1 was sent into the conversion zone 13 of V-type reactor, charging aperture 1 place was equipped with feeding machine 6 with aluminum-plastic composite membrane, add the liquid that configures from inlet 10 to conversion zone in 13, and by heat-insulation layer 11, its maintenance is carried out at a certain temperature.Aluminum-plastic composite membrane moves downward from charging aperture 1 along reactor with certain speed at the bottom of the still under the action of gravitation of self.Aluminum-plastic composite membrane can be separated fully in its motion process.Then starter motor and reductor 7 drive emptying auger 5 and at the bottom of still, completely reacted material are transported to subsequent processing from discharging opening 3, can carry out cooling by the material that deferent segment 14 internal reactions are good by cooling layer 12.
Embodiment 2:
Get that in described liquid, the shared ratio of each composition is: mass percent is that 85% formic acid is 13%; Mass percent is that 95% carrene is 2%; Water is 85% to react, and other is identical with embodiment 1.
Embodiment 3:
Get that in described liquid, the shared ratio of each composition is: mass percent is that 85% formic acid is 14%; Mass percent is that 95% carrene is 3%; Water is 83% to react, and other is identical with embodiment 1.
Embodiment 4:
Get that in described liquid, the shared ratio of each composition is: mass percent is that 85% formic acid is 15%; Mass percent is that 95% carrene is 4%; Water is 81% to react, and other is identical with embodiment 1.
This V-type reactor, equipment profile are " V " shape, and volume is about 50m
3, day output has been converted to 100 tons by 30 tons of existing every days, and raw material is completed by the Action of Gravity Field of himself fully in the motion of conversion zone 13, thereby has reduced power, has saved energy consumption, and each parts can adopt superfine high-quality stainless steel to make, with corrosion-resistant.
Claims (6)
1. V-type reactor, it is characterized in that: comprise the V-type body (2) that is arranged on support (4), V-type body (2) comprises conversion zone (13) and deferent segment (14), conversion zone (13) upper end is provided with charging aperture (1) and inlet (10), conversion zone fills liquid in (13), and heat-insulation layer (11) is installed on conversion zone (13); The top of deferent segment (14) is provided with discharging opening (3), is provided with the emptying auger (5) that is connected with motor and reductor (7) in deferent segment (14), and cooling layer (12) is installed on deferent segment (14); Conversion zone (13) is 30 ° with the angle of horizontal plane, and deferent segment (14) is 60 ° with the angle of horizontal plane.
2. V-type reactor according to claim 1, it is characterized in that: conversion zone (13) interior top charging aperture (1) locates to be equipped with feeding machine (6).
3. V-type reactor according to claim 1, it is characterized in that: deferent segment (14) top discharging opening (3) downside is provided with liquid spill-way (8).
4. V-type reactor according to claim 3, it is characterized in that: the junction of deferent segment (14) bottom and conversion zone (13) is provided with sewage draining exit (9).
5. V-type reactor according to claim 1 is characterized in that: described liquid comprises that mass percent is that 85% formic acid, mass percent are 95% carrene and water.
6. V-type reactor according to claim 1 or 5, it is characterized in that: in described liquid, the shared ratio of each composition is:
Mass percent is that 85% formic acid is 12%～15%;
Mass percent is that 95% carrene is 2%～4%;
Water is 81%～86%.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201010243437XA CN101912758B (en) | 2010-08-03 | 2010-08-03 | V-shaped reaction kettle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201010243437XA CN101912758B (en) | 2010-08-03 | 2010-08-03 | V-shaped reaction kettle |
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| Publication Number | Publication Date |
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| CN101912758A CN101912758A (en) | 2010-12-15 |
| CN101912758B true CN101912758B (en) | 2013-11-06 |
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| CN201010243437XA Active CN101912758B (en) | 2010-08-03 | 2010-08-03 | V-shaped reaction kettle |
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Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN104669467A (en) * | 2015-03-06 | 2015-06-03 | 徐超 | Separating agent for medical waste aluminium-plastic packaging materials and preparation method of separating agent |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0228724A2 (en) * | 1985-12-19 | 1987-07-15 | DANECO DANIELI ECOLOGIA SpA | Separator for aggregate |
| EP1038581A1 (en) * | 1999-03-22 | 2000-09-27 | Eco-Bat S.p.A. | Equipment and process to make separations and reactions among solids in aqueous suspensions and/or among liquids and solids |
| CN1600439A (en) * | 2003-09-22 | 2005-03-30 | 汉斯·胡贝尔机械设备制造股份公司 | Apparatus for separating organic material from inorganic material |
| CN2820306Y (en) * | 2005-09-20 | 2006-09-27 | 常州市荣创自动化设备厂 | Screw type solid material continuous stirrer |
| CN101165084A (en) * | 2007-09-20 | 2008-04-23 | 曹光军 | Plastic-aluminum separating agent and plastic-aluminum separating method |
| CN101759868A (en) * | 2009-12-15 | 2010-06-30 | 巨锋 | Decomposition process of aluminum composite |
| CN201776143U (en) * | 2010-08-03 | 2011-03-30 | 沈安平 | V-shaped agitated reactor |
-
2010
- 2010-08-03 CN CN201010243437XA patent/CN101912758B/en active Active
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0228724A2 (en) * | 1985-12-19 | 1987-07-15 | DANECO DANIELI ECOLOGIA SpA | Separator for aggregate |
| EP1038581A1 (en) * | 1999-03-22 | 2000-09-27 | Eco-Bat S.p.A. | Equipment and process to make separations and reactions among solids in aqueous suspensions and/or among liquids and solids |
| CN1600439A (en) * | 2003-09-22 | 2005-03-30 | 汉斯·胡贝尔机械设备制造股份公司 | Apparatus for separating organic material from inorganic material |
| CN2820306Y (en) * | 2005-09-20 | 2006-09-27 | 常州市荣创自动化设备厂 | Screw type solid material continuous stirrer |
| CN101165084A (en) * | 2007-09-20 | 2008-04-23 | 曹光军 | Plastic-aluminum separating agent and plastic-aluminum separating method |
| CN101759868A (en) * | 2009-12-15 | 2010-06-30 | 巨锋 | Decomposition process of aluminum composite |
| CN201776143U (en) * | 2010-08-03 | 2011-03-30 | 沈安平 | V-shaped agitated reactor |
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| CN101912758A (en) | 2010-12-15 |
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Effective date of registration: 20190822 Address after: 252400 No. 2 Industrial Park Road, Shenzhou Office, Shenxian County, Liaocheng City, Shandong Province Patentee after: Liaocheng Tianyi Environmental Protection Machinery Equipment Co., Ltd. Address before: No. 88-43 Zhenxing Street, Juxian County, Liaocheng City, Shandong Province, 252400 Patentee before: Shen Anping |
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