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Method and apparatus for hydrotreating waste plastics

A technology for hydrogenation treatment and waste plastics, which is applied in the direction of hydrogenation treatment process, hydrocarbon oil treatment, hydrocarbon oil treatment products, etc. It can solve the problems of insufficient catalyst wetting, low yield of liquid products, high cracking initiation temperature, etc., and achieve Excellent hydroisomerization effect, complete removal of impurities, and good cracking rate

Inactive Publication Date: 2020-07-03
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This one-step processing method causes the two raw materials to be heated quickly before they are fully mixed; at the same time, due to the high heating rate, the raw materials that have just been mixed will directly generate coke products before they have time to react. The liquid product yield is on the low side, only about 80wt%
[0006] Chinese patent CN1434100A uses waste plastics and oil mixed raw materials to produce fuel oil through pyrolysis. This method solves the problem of utilization of waste plastics, heavy oil and waste oil, but there is a high cracking initiation temperature, and light oil products such as Low yields of gasoline and diesel fractions, and the heavy oil mentioned is a long-chain, large-molecular-weight, high-viscosity oil produced during petroleum production
At the same time, in order to increase the mass transfer, the ratio of hydrogen to oil is usually much higher than that required for the reaction, and the low flow rate of the liquid will result in insufficient wetting of the catalyst.

Method used

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  • Method and apparatus for hydrotreating waste plastics
  • Method and apparatus for hydrotreating waste plastics
  • Method and apparatus for hydrotreating waste plastics

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0065] see figure 1 and figure 2 As shown, the waste plastic 1 (HDPE, high-density polyethylene) enters the oil-gas mixing equipment 3 through the heating furnace 2, and the hydrogen compressor 4 sends the hydrogen 6 into the oil-gas mixing equipment 3, and the waste plastic 1 and the hydrogen 6 are mixed and enter the first The liquid phase hydrogenation reactor 12-1 carries out the hydrocracking reaction, the first liquid phase hydrogenation reactor 12-1 is a thermal cracking reactor, and the thermal cracking reactor is a fixed bed reactor;

[0066] Wherein, the reaction conditions of the hydrocracking reaction are: a reaction temperature of 450° C., a hydrogen pressure of 1.5 MPa, and a reaction time of 1 h. The catalyst used in the hydrocracking reaction is a HZSM-5 molecular sieve catalyst;

[0067] The hydrocracking reaction product and Fischer-Tropsch wax enter the oil-gas mixing device 3 at a mass ratio of 1:1, and at the same time, the hydrogen compressor 4 sends h...

Embodiment 2

[0075] The difference from Example 1 is that the raw material is a 1:1 mixture of LDPE (low density polyethylene) and FT wax. Hydrocracking and hydroisomerization reaction conditions are consistent with embodiment 1, obtain product: C4 and below yield 2.8%, naphtha fraction yield 13.7%, diesel fraction yield is 30.5%, lubricating oil base oil total yield The rate is 55.8%. And, from the total base oil of lubricating oil, base oil products with a distillation range of 370-440 and a distillation range of 4CSt, and base oil products with a distillation range of >440°C and a distillation range of 6cSt are cut out.

[0076] According to the kinematic viscosity at 100°C, when the viscosity index reaches above 120, it belongs to Class III lubricating oil base oil, that is, high-grade lubricating oil base oil. (Classification refers to API lubricating oil standards and CNPC lubricating oil base oil industry standards)

[0077] The properties of the resulting product are shown in Tab...

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Abstract

The invention relates to a method for hydrotreating waste plastics. The method comprises the following steps: S1, adding waste plastics into a first liquid phase hydrogenation reactor, and carrying out a hydrocracking reaction under the conditions that the pressure is 1-3 MPa, the temperature is 500-700 DEG C and the time is 20-90 minutes to obtain a cracking product; S2, feeding the cracking product or the cracking product and an oil raw material into a second liquid phase hydrogenation reactor, and carrying out a hydroisomerization reaction to obtain an isomerization product, wherein the weight ratio of the cracking product to Fischer-Tropsch wax is 1:(0.5-3), the conditions of the hydroisomerization reaction are as follows: the pressure is 10-15 MPa, the temperature is 300-500 DEG C, and the reaction time is 1 hour, and the oil raw material is at least one selected from paraffin-based distillate oil and Fischer-Tropsch wax; and S3, performing distillation or high-pressure separationon the isomerization product to obtain lubricating oil base oil, diesel oil and hydrocarbon gas. The invention also relates to a device for hydrotreating waste plastics.

Description

technical field [0001] The invention relates to a method and device for hydrogenation treatment of waste plastics, in particular to a method for treating waste plastics with a liquid phase hydrogenation treatment device. The invention uses a liquid-phase hydrogenation reactor to carry out hydrocracking and hydrogenation isomerization. The liquid-phase hydrogenation reactor adopts a multi-point quantitative hydrogen replenishment method, cancels a circulating hydrogen compressor, and improves hydrogenation efficiency. Background technique [0002] According to the latest information from China Petroleum and Chemical Network: China's annual waste plastic production is about 34.13 million tons, and the recycling amount reaches more than 24.878 million tons, accounting for about 30% of China's plastic consumption. Waste plastic resources are called "the second mineral deposit of human beings" by modern economists. Plastic raw materials are chemical products extracted from natur...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G1/10C10G1/06C10G65/12
CPCC10G1/06C10G1/10C10G65/12C10G2300/1003C10G2400/04C10G2400/10C10G2400/26
Inventor 付凯妹王嘉祎王晶晶庄梦琪翟绪丽王燕张志华谢彬张占全张雅琳袁晓亮余颖龙王延飞庞子翔杨晓彦喻昊安谧
Owner PETROCHINA CO LTD
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