CN103922539A - Water circulation method in regenerated aluminum-plastic composite product separation process - Google Patents

Water circulation method in regenerated aluminum-plastic composite product separation process Download PDF

Info

Publication number
CN103922539A
CN103922539A CN201410142790.7A CN201410142790A CN103922539A CN 103922539 A CN103922539 A CN 103922539A CN 201410142790 A CN201410142790 A CN 201410142790A CN 103922539 A CN103922539 A CN 103922539A
Authority
CN
China
Prior art keywords
water
tank
pool
plastic
aluminum
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201410142790.7A
Other languages
Chinese (zh)
Inventor
马学东
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ANHUI TENGYUE ALUMINIUM PLASTIC Co Ltd
Original Assignee
ANHUI TENGYUE ALUMINIUM PLASTIC Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by ANHUI TENGYUE ALUMINIUM PLASTIC Co Ltd filed Critical ANHUI TENGYUE ALUMINIUM PLASTIC Co Ltd
Priority to CN201410142790.7A priority Critical patent/CN103922539A/en
Publication of CN103922539A publication Critical patent/CN103922539A/en
Pending legal-status Critical Current

Links

Landscapes

  • Manufacture And Refinement Of Metals (AREA)

Abstract

The invention discloses a water circulation method in a regenerated aluminum-plastic composite product separation process, and relates to the technical field of resource recycling. The water circulation method comprises the following processing steps: 1) pumping water in a hydrolytic tank into a plate-and-frame press to filter, flowing filtered water into a reflux tank, and returning a filter residue to the hydrolytic tank to be separated; 2) adjusting the pH value of water in the reflux tank to keep the water in the reflux tank neutral, and then putting the water in the reflux tank into a stewing pool to be stewed for 7-15 days; 3) flowing the water at the middle and upper parts of the stewing pool into an SBR pool to carry out aerobic biochemical treatment, and flowing supernate after stewing in the SBR pool into a regulating reservoir; 4) filling clean water into the regulating reservoir, and putting the water in the regulating reservoir into a clean water basin, wherein the water in the clean water basin is supplied to the hydrolytic tank to be used. The wastewater is comprehensively utilized in cycle, so as to achieve zero emission and zero pollution. The water source can be supplied after the water source in the circulation system is naturally consumed, so that the system is simple in process and convenient to operate, the environment can be effectively protected, and water resources are saved.

Description

Water cycle method in regeneration plastic-aluminum composite product separating technology
Technical field
The present invention relates to resource reutilization technical field, be specifically related to a kind of water cycle method in regeneration plastic-aluminum composite product separating technology.
Background technology
Aluminium scrap is moulded goods through processing, and can reclaim aluminium and plastics, and the aluminium of recovery and plastics can directly or be applied to decoration, finishing and packaging etc. after modification, apply more and more extensively, have higher recovery value.Under the overall situation reduce gradually in resource, price increasing gradually, if can be recycled, important economic worth and energy-saving and emission-reduction meaning will be there is.
At present, plastic-aluminum separating method is common acid-soluble or the molten partition method of alkali, weak acid multi_layer extraction method and a demixing of solvents partition method etc.Utilize aluminium can be dissolved in the principle of soda acid, use method acid-soluble or that alkali is molten the al dissolution in material, thus recycled plastic, and then aluminum bearing waste is made to polymerize aluminum chloride or Tai-Ace S 150.This acid-soluble or molten partition method of alkali has the halfway shortcoming of recovery.
In addition, utilize organic monoacid molecule can permeate plastic layer as acetic acid, formic acid etc., so dissolve each layer of bonding aluminium oxide compound and the aluminium in wrapping material and plastics are distinguished complete separation by the characteristic that can not dissolve pure aluminum.This weak acid multi_layer extraction method has long reaction time, shortcoming that separation efficiency is low.In addition, utilize plastics by organic solvent as the character of the swelling such as toluene, chloroform, with an organic solvent to make plastics swelling, aluminium is peeled off from plastic-aluminum sheet, then recycle respectively.This demixing of solvents partition method has the shortcoming that solvent consumption is large, toxicity is large, cost is high, and can produce more waste water in removal process, and the wasting of resources is larger.
Summary of the invention
Technical problem to be solved by this invention is to provide a kind of environmental pollution that reduces, water cycle method in the regeneration plastic-aluminum composite product separating technology of raising resource utilization.
Technical problem to be solved by this invention realizes by the following technical solutions:
A kind of regeneration plastic-aluminum composite product environmental protection separating technology, comprises following processing step,
1) purchase sorting: from the regeneration plastic-aluminum goods (as plastic-aluminum cable, aluminum-plastic composite membrane, aluminium plastic composite packaging paper etc.) of various places purchase different colours, specification, by manual removal, extract after the impurity elimination of copper core, unification is stacked plastic-aluminum goods neat;
2) separate first: the regeneration plastic-aluminum goods unification after impurity elimination is put into high speed disintegrator, carry out fragmentation, be processed into the plastic-aluminum piece of block specification;
3) secondary separation: block plastic-aluminum is transported to the reactor of semitight by travelling belt, passes into and be steam heated to 100 DEG C, the temperature profile different according to plastic-aluminum, within 30-120 minute, make the aluminium plastic material being tightly combined with each other, separate gradually, obtain purity higher aluminum and mould parting material;
4) aluminum-plastic separation material is put into high-speed grinder and grind, cross 80-150 mesh sieve, then the aluminum-plastic separation materials processing of powdery is become to particulate state plastic-aluminum mixing material;
5) separate for three times: particulate state plastic-aluminum mixing material is placed in to hydrolytic tank by transport unit, in hydrolytic tank, inject normal-temperature water, utilize the mobility of stirring wheel and water, make granular plastic-aluminum mixing material through overcooling, natural separation after expanding with heat and contract with cold, utilize its different density, on plastics, float, aluminium powder sinks;
6) plastic grain floating in collection and the aluminium powder of sinking, obtain purity and reach 99% plastic grain and aluminium powder;
7) by plastic grain and aluminium powder airing (oven dry) respectively, after being dried, unitizing warehouse-in, aluminium powder is for the preparation of aluminum products such as aluminium bars, and recycled plastic granules is for the preparation of plastics such as battery jars.
A kind of water cycle method in regeneration plastic-aluminum composite product separating technology, comprises following processing step,
1) water in hydrolytic tank is pumped into flame filter press and carry out filtration treatment, the water after filtration flows into backflow pool, and filter residue comes back in hydrolytic tank and separates;
2) the pH value of water in adjusting backflow pool, makes the water in backflow pool keep neutral, then the water in backflow pool is put into standing pond, leaves standstill 7-15 days;
3) will leave standstill middle and upper part, pond and divide water to carry out aerobic treatment from flowing to SBR pond, after SBR pond leaves standstill, supernatant liquor flows into equalizing tank;
4) in equalizing tank, fill into clear water, then the water in equalizing tank is put into clean water basin, the water in these clean water basin is used for providing hydrolytic tank to use.
The invention has the beneficial effects as follows: the present invention fully utilizes waste water circulation, reach zero release, zero pollutes; after the water source in the recycle system consumes naturally, can supplement it, system process is simple; easy to operate, effectively protection of the environment, saving water resource.
Brief description of the drawings
Fig. 1 is process flow diagram of the present invention.
Embodiment
For technique means, creation characteristic that the present invention is realized, reach object and effect is easy to understand, below in conjunction with concrete diagram, further set forth the present invention.
As shown in Figure 1, a kind of water cycle method in regeneration plastic-aluminum composite product separating technology, comprises following processing step,
1) water in hydrolytic tank is pumped into flame filter press and carry out filtration treatment, the water after filtration flows into backflow pool, and filter residue comes back in hydrolytic tank and separates;
2) the pH value of water in adjusting backflow pool, makes the water in backflow pool keep neutral, then the water in backflow pool is put into standing pond, leaves standstill 7-15 days;
3) will leave standstill middle and upper part, pond and divide water to carry out aerobic treatment from flowing to SBR pond, after SBR pond leaves standstill, supernatant liquor flows into equalizing tank;
4) in equalizing tank, fill into clear water, then the water in equalizing tank is put into clean water basin, the water in these clean water basin is used for providing hydrolytic tank to use.
More than show and described ultimate principle of the present invention and principal character and advantage of the present invention.The technician of the industry should understand; the present invention is not restricted to the described embodiments; that in above-described embodiment and specification sheets, describes just illustrates principle of the present invention; without departing from the spirit and scope of the present invention; the present invention also has various changes and modifications, and these changes and improvements all fall in the claimed scope of the invention.The claimed scope of the present invention is defined by appending claims and equivalent thereof.

Claims (1)

1. a water cycle method in regeneration plastic-aluminum composite product separating technology, is characterized in that: comprise following processing step,
1) water in hydrolytic tank is pumped into flame filter press and carry out filtration treatment, the water after filtration flows into backflow pool, and filter residue comes back in hydrolytic tank and separates;
2) the pH value of water in adjusting backflow pool, makes the water in backflow pool keep neutral, then the water in backflow pool is put into standing pond, leaves standstill 7-15 days;
3) will leave standstill middle and upper part, pond and divide water to carry out aerobic treatment from flowing to SBR pond, after SBR pond leaves standstill, supernatant liquor flows into equalizing tank;
4) in equalizing tank, fill into clear water, then the water in equalizing tank is put into clean water basin, the water in these clean water basin is used for providing hydrolytic tank to use.
CN201410142790.7A 2014-04-10 2014-04-10 Water circulation method in regenerated aluminum-plastic composite product separation process Pending CN103922539A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410142790.7A CN103922539A (en) 2014-04-10 2014-04-10 Water circulation method in regenerated aluminum-plastic composite product separation process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410142790.7A CN103922539A (en) 2014-04-10 2014-04-10 Water circulation method in regenerated aluminum-plastic composite product separation process

Publications (1)

Publication Number Publication Date
CN103922539A true CN103922539A (en) 2014-07-16

Family

ID=51140973

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201410142790.7A Pending CN103922539A (en) 2014-04-10 2014-04-10 Water circulation method in regenerated aluminum-plastic composite product separation process

Country Status (1)

Country Link
CN (1) CN103922539A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105819556A (en) * 2016-04-20 2016-08-03 兰溪市博远金属有限公司 Sludge treatment process for aluminum regeneration process
CN107176631A (en) * 2017-06-07 2017-09-19 常州市海若纺织品有限公司 A kind of method that water purification agent is prepared based on waste aluminium plastic material

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1337280A (en) * 2000-08-09 2002-02-27 杨春庭 Method of treating underproof composite aluminium-plastic pipe
KR100917097B1 (en) * 2009-02-09 2009-09-15 (주) 한호건설 Sequencing batch membrane bio reactor process and the device
CN202705171U (en) * 2012-08-06 2013-01-30 厦门陆海科技工程有限公司 Aluminum plastic separation waste water treatment system

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1337280A (en) * 2000-08-09 2002-02-27 杨春庭 Method of treating underproof composite aluminium-plastic pipe
KR100917097B1 (en) * 2009-02-09 2009-09-15 (주) 한호건설 Sequencing batch membrane bio reactor process and the device
CN202705171U (en) * 2012-08-06 2013-01-30 厦门陆海科技工程有限公司 Aluminum plastic separation waste water treatment system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105819556A (en) * 2016-04-20 2016-08-03 兰溪市博远金属有限公司 Sludge treatment process for aluminum regeneration process
CN107176631A (en) * 2017-06-07 2017-09-19 常州市海若纺织品有限公司 A kind of method that water purification agent is prepared based on waste aluminium plastic material

Similar Documents

Publication Publication Date Title
CN103949458B (en) Regeneration plastic-aluminum composite article environmental protection separating technology
CN104552659B (en) Buoyancy separation device for automobile non-metal smashed waste
CN202876534U (en) Tailing dry emission system
CN104708730A (en) PET bottle recycling process
CN105576315A (en) Method for recycling crushed waste storage battery shells
CN103923343A (en) Process for separating and regenerating aluminum-plastic product by adopting steam-heating mode
CN103922539A (en) Water circulation method in regenerated aluminum-plastic composite product separation process
CN102126917B (en) High purity recycling and energy integration technology for different concentrations of dichloromethane wastewater
CN102151686A (en) Process for recycling waste toothpaste aluminum-plastic composite packaging material
CN101912868A (en) Separation and recovery technology for waste aluminum-plastic composite packaging material
CN108748786A (en) A kind of regeneration PE material manufacturing techniques
CN102463637A (en) Method for producing regenerative plastic particle by using plastic waste
CN104276687B (en) A kind of method of animal protein feed in recycling casing processing-waste
CN206204023U (en) A kind of waste mortar recycle and reuse system
CN204490696U (en) Oil field slurry containing oil treating device
CN201325937Y (en) Protein recovery device for protein and starch separation section in the production of corn starch
CN205115079U (en) Concrete mixing plant effluent treatment plant
CN202461103U (en) Continuous automation aluminum-plastic separating system
CN106865904A (en) A kind of photovoltaic industry sewage classification processing method
CN108589362B (en) A kind of dry isolated method of waste and old paper composite wallpaper
CN206428168U (en) A kind of refinement mother liquor cyclic utilization system
CN202322554U (en) Wastewater recycling, using and treating system
CN205115168U (en) Stamp waste water recycling processing system
CN214344623U (en) Anti-aging agent TMQ subsides residual processing apparatus
CN202460290U (en) System for processing sludge

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C02 Deemed withdrawal of patent application after publication (patent law 2001)
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20140716