Polyolefin waste plastic self-exothermic phase change thermal cracking process

A technology for waste plastics and polyolefins, which is applied in the field of self-exothermic phase change thermal cracking process of polyolefin waste plastics, can solve the problems of not being able to eliminate white pollution, difficult to recycle and reuse, and increase operating costs, and is easy to promote on a large scale. Application, equipment manufacturing maturity, the effect of reducing energy consumption

Active Publication Date: 2021-09-24
佛山市科恒博环保技术有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In addition, the performance of plastics degrades after repeated melting and recycling, so mechanical recycling technology cannot be used as the ultimate way to eliminate white pollution
[0003] The traditional pyrolysis technology generally adopts the process of catalytic pyrolysis, which has the disadvantages of high process temperature, long reaction time, and low added value of the product. The complete thermal conversion of waste plastics into product oil requires a temperature condition of at least 430°C-550°C
In the process of catalytic pyrolysis, the catalyst is mixed with the raw materials, and the carbon residue generated by the thermal conversion of waste plastics sticks to the surface of the catalyst, which makes the catalyst easily deactivated and difficult to recycle and reuse, increasing the operating cost

Method used

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  • Polyolefin waste plastic self-exothermic phase change thermal cracking process

Examples

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Effect test

Embodiment 1

[0043] A self-exothermic phase-change pyrolysis process for polyolefin waste plastics, comprising the following steps:

[0044] (1) Carry out impurity removal and drying pretreatment to polyethylene waste plastics;

[0045] (2) Place the pretreated polyethylene waste plastics in the first high-pressure reactor 7 with a filling rate of 0.35, and feed inert gas to replace the air in the high-pressure reactor;

[0046] (3) Into the first high-pressure reactor 7, the phase builder is imported, and the phase builder is nitrogen with an initial pressure value of 1MPa;

[0047] (1) Heat the first high-pressure reactor 7 to 380°C, the heating rate is 15°C / min, the internal pressure of the first high-pressure reactor 7 is 5.26MPa under the temperature condition of 380°C, and the polyethylene waste plastic undergoes a self-exothermic phase change The thermal cracking reaction produces thermal cracking products, and the average carbon numbers of the thermal cracking products and product...

Embodiment 2

[0051] A self-exothermic phase-change pyrolysis process for polyolefin waste plastics, comprising the following steps:

[0052] (1) Carry out impurity removal and drying pretreatment to polyethylene waste plastics;

[0053] (2) Place the pretreated polyethylene waste plastics in the first high-pressure reactor 7 with a filling rate of 0.35, and feed inert gas to replace the air in the high-pressure reactor;

[0054] (3) Into the first high-pressure reactor 7, import phase builder, described phase builder is the gas in the hot state from the thermal cracking reaction of the second high-pressure reactor 15 and the gas in the gas collection tank 21;

[0055] (4) Heat the first high-pressure reactor 7 to 380°C, the heating rate is 15°C / min, and the internal pressure of the first high-pressure reactor 7 is 4.27MPa under the temperature condition of 340°C, and the polyethylene waste plastic undergoes a self-exothermic phase change The thermal cracking reaction produces thermal crac...

Embodiment 3

[0059] A self-exothermic phase-change pyrolysis process for polyolefin waste plastics, comprising the following steps:

[0060] (1) Carry out impurity removal and drying pretreatment to polyethylene waste plastics;

[0061] (2) Place the pretreated polyethylene waste plastics in the first high-pressure reactor 7 with a filling rate of 0.35, and feed inert gas to replace the air in the high-pressure reactor;

[0062] (3) Into the first high pressure reactor 7, import phase builder, described phase builder is the gas in the hot state after the pyrolysis reaction from the second high pressure reactor 15 and the gas in the gas collection tank 21;

[0063] (4) Heat the first high-pressure reactor 7 to 340°C, the heating rate is 15°C / min, the internal pressure of the first high-pressure reactor 7 is 4.18MPa under the temperature condition of 340°C, and the polyethylene waste plastic undergoes a self-exothermic phase change The thermal cracking reaction produces thermal cracking pro...

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Abstract

The invention relates to the technical field of waste plastic recycling, and particularly discloses a polyolefin waste plastic self-exothermic phase change thermal cracking process which comprises the following steps: placing polyolefin waste plastic in a high-pressure reactor, and introducing inert gas to replace air in the high-pressure reactor; inputting a phase construction agent into the high-pressure reactor, wherein the phase construction agent comprises inert gas with an initial pressure value greater than 0.5 MPa and / or hydrocarbon liquid with a boiling point lower than 125 DEG C; heating the high-pressure reactor to 340-380 DEG C, enabling the pressure value in the high-pressure reactor to be 2-6 MPa, subjecting the polyolefin waste plastic to a self-exothermic phase change thermal cracking reaction, and obtaining a thermal cracking product. The self-exothermic phase change of the polyolefin waste plastic long-chain hydrocarbon is realized by establishing a specific phase state condition, so that the thermal cracking reaction temperature is greatly increased, the deep cracking of the polyolefin waste plastic is promoted, and the energy consumption in the heat treatment process can be obviously reduced.

Description

technical field [0001] The invention relates to the technical field of recycling waste plastics, in particular to a self-exothermic phase-change pyrolysis process for polyolefin waste plastics. Background technique [0002] According to statistics, as of 2015, the total global plastic production has reached 6.3 billion tons; another scholar predicts that the current annual growth rate of plastic production is about 4%, which means that more plastic waste will be generated; and statistics show that, Only about 9% of plastic waste is recycled, 12% is incinerated, and 79% flows into terrestrial and marine ecosystems, ultimately endangering the health of various organisms including humans. Although incineration treatment can achieve heat recovery, based on the current global annual output of waste plastics of 260 million tons, if all of them flow to incineration, the potential CO 2 Emissions, about three times the mass of plastic, are equivalent to about 2% of total global carb...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G1/10
CPCC10G1/10C10G2300/1003C10G2300/305
Inventor 袁浩然顾菁程磊磊王亚琢吴玉锋杨希贤
Owner 佛山市科恒博环保技术有限公司
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