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Method for recycling waste plastics containing polybrominated diphenyls and polybrominated diphenyl ethers

A polybrominated diphenyl ether and polybrominated biphenyl technology, which is applied in the field of waste plastic regeneration, can solve the problems of high equipment requirements, unsuitable for large-scale production, and can not solve the problem of plastic waste regeneration well, so as to improve separation efficiency and realize physical circulation. The effect of using

Inactive Publication Date: 2011-05-11
广东泰昊新材料科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, there are the following problems in adopting this patented method to reclaim polybrominated diphenyl ether flame-retardant plastics: (1) decabromodiphenyl ether theoretically still has a solubility of 0.1 to 0.2 wt% in these solvents at room temperature, and the polybrominated diphenyl ethers below nona bromine The solubility is greater, due to the high boiling point and low volatility, most of the dissolved polybrominated diphenyl ethers cannot be removed with the solvent in the subsequent vacuum evaporation process
(2) The particle size of decabromodiphenyl ether raw materials is generally 1 to 5 microns. Experiments have found that the decabromodiphenyl ether particles in waste plastics will also partially dissolve when the plastic dissolves, resulting in a smaller particle size. Therefore There are a large number of decabromodiphenyl ether particles with a particle size of less than 1 micron in the plastic solution. These small particles cannot be separated even by high-speed centrifugation. As a result, the concentration of decabromodiphenyl ether in the plastic solution after centrifugation Significantly higher than its theoretical solubility in solvents
However, the supercritical extraction process has problems such as high equipment requirements, harsh separation conditions, and unsuitability for large-scale production.
[0007] It can be seen that the existing technology cannot better solve the regeneration problem of plastic wastes containing polybrominated biphenyls and polybrominated diphenyl ethers.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0041] 1kg of waste HIPS (high anti-filling polystyrene) particles containing 5% (weight) of decabromodiphenyl ether and 4kg of toluene are added in a 10-liter stirred tank, stirred and dissolved at normal temperature for 60min, and the solution is passed through a separating sieve (aperture diameter 0.5mm) separation, to obtain 4.9kg of plastic solution and 0.1kg of insoluble plastic particles and impurities such as screws, glass, and gravel. Pass the plastic solution through a high-speed tubular centrifuge, and separate 0.18kg of sludge-like filter residue and 4.72kg of filter solution at a speed of 10,000 rpm, and then add 4kg of toluene to the filter solution to reduce the concentration of HIPS to 10%. Around, heated to 50°C, placed frequency 100kHz, power 0.5W / cm 2 Under the action of ultrasonic waves, stir and dissolve at a speed of 500 rpm for 60 min, and then add it to a 8kg isopropanol stirring tank preheated to 50°C at a speed of 100ml / min for precipitation. The sti...

Embodiment 2

[0044] 1kg waste polystyrene (PS) containing 5% decabromodiphenyl ether, 3% decabromobiphenyl (PS) and 2.3kg limonene are added in a 10-liter stirring tank, stirred and dissolved at normal temperature for 60min, and the solution is passed through a separating sieve ( Aperture diameter is 1mm), obtain 3.19kg polymer solution and about 0.11kg insoluble plastic particles and impurities such as screws, glass, sand and gravel. Pass the polymer solution through a high-speed tubular centrifuge, and separate 0.25kg of sludge-like filter residue and 2.94kg of filter solution at a speed of 15,000 rpm, and then add 1kg of limonene to the filter solution to control the plastic concentration to about 20%. , heated to 60°C, at the same time at a frequency of 100kHz / , power of 0.5w / cm 2 Stir and dissolve at a speed of 1000 rpm for 120 min under the action of ultrasonic waves, and then add it to a 8kg n-propanol stirring tank preheated to 60°C at a speed of 100 ml / min for precipitation. Durin...

Embodiment 3

[0047] 1 kg of waste HIPS containing 10% decabromodiphenyl ether and 4 kg of butyl acetate were added to a 10-liter stirred tank, stirred and dissolved at room temperature for 90 min, and the solution was passed through a separating sieve (aperture 0.5 mm) to obtain 4.92 kg of polymer solution and 0.08kg of insoluble plastic particles and impurities such as screws, glass, and gravel. The polymer solution is passed through a high-speed tubular centrifuge, and 0.33kg of sludge-like filter residue and 4.59kg of filter solution are separated at a speed of 10,000 rpm, and 4.5kg of butyl acetate is added to the filter solution to reduce the concentration of the plastic. Decrease to about 10%, then heat to 50°C, put in frequency 50kHz, power 1.5w / cm 2 Stir and dissolve at a speed of 500 rpm for 60 min under the action of ultrasonic waves. Then add it into a 9.5kg ethanol stirring tank preheated to 50°C at a speed of 100ml / min for precipitation. The stirring speed of ethanol is 1000 ...

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PUM

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Abstract

The invention discloses a method for recycling waste plastics containing polybrominated diphenyls and polybrominated diphenyl ethers, which comprises the following steps: adding waste electronic plastics into a solvent A, dissolving the waste electronic plastics at normal temperature, screening the dissolved plastic solution by using a separating screen, centrifugalizing the screened plastic solution, complementally adding the solvent A into the centrifugalized plastic solution, applying ultrasonic waves onto the solution, adding the obtained plastic solution into a solvent B, and stirring for 30-90 minutes at the rotation speed of 1000-2000 revolutions / minute under the action of ultrasonic waves of which the frequency is 20-50 kHz and the power is 0.5-1.5 W / cm<2>; and sending the plastic precipitate into a twin screw extruder, and removing the residual solvent in the precipitate at 180-220 DEG C, thereby obtaining the recycled plastic product. The mass percent of polybrominated diphenyls and polybrominated diphenyl ethers in the plastics treated by using the method provided by the invention is reduced to lower than 0.1% without great loss of physical and mechanical properties.

Description

technical field [0001] The invention relates to a regeneration method of waste plastics, in particular to the recycling of polybrominated diphenyl ether and polybrominated biphenyl flame-retardant waste plastics, and the method is suitable for the regeneration of flame-retardant waste electronic plastics. Background technique [0002] The dismantling and recycling process of waste electronic and electrical equipment produces a large amount of plastic waste. These plastics are generally added with 5-20% brominated flame retardants. Among them, polybrominated biphenyls and polybrominated diphenyl ethers have been proven to be harmful to the environment, organisms and human beings. Persistent organic pollutants that are harmful to health, so the European Union clearly stipulates in the "Directive on the Restriction of the Use of Certain Hazardous Components in Electrical and Electronic Equipment" (RoHS Directive) that all products sold in the EU market will be effective from Jul...

Claims

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Application Information

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IPC IPC(8): C08J11/08C08L25/06C08L51/04C08L55/02C08L69/00
CPCY02W30/62
Inventor 彭绍洪陈烈强赵向阳
Owner 广东泰昊新材料科技有限公司
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