Method for preparing high-quality tar by pyrolyzing plastic wastes
A waste, high-quality technology, used in the preparation of liquid hydrocarbon mixtures, products, coke ovens, etc., can solve the problems of cluttered products, low content of gasoline and diesel fractions, rough production processes, etc., to improve the octane number. , The effect of low operating cost and flexible operation
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[0057] In the present invention, wt% means weight%.
[0058] Plastic waste rich in polyethylene (PE), polypropylene (PP), polystyrene (PS), polyvinyl chloride (PVC), etc. is sent to the pyrolysis reactor, and the temperature of the pyrolysis reaction is controlled at 500°C , the system maintains a slightly positive pressure operation (1-5KPa), and the generated high-temperature pyrolysis steam is sent to the catalytic reactor, and the catalytic reactor adopts a fluidized bed reactor. The catalytic cracking temperature is controlled at 450°C, the catalytic reactor is heated and kept warm by electric heating, and the catalyst is Al 2 o 3 -SiO 2 solid catalyst. After 3 days of operation, the catalyst is regenerated in the catalyst regenerator, the regeneration method is air combustion, and the temperature is 900°C. The high-temperature pyrolysis steam is exported from the outlet of the catalytic reactor into the condensation separation device, and light oil, pyrolysis water a...
Embodiment 2
[0068] Plastic wastes rich in polyethylene (PE), polypropylene (PP), polystyrene (PS), polyvinyl chloride (PVC), etc. are sent to the pyrolysis reactor, and the temperature of the pyrolysis reaction is controlled at 500°C , the system maintains a slightly positive pressure operation (1-5KPa), and the generated high-temperature pyrolysis steam is sent to the catalytic reactor, and the catalytic reactor adopts a fluidized bed reactor. The catalytic cracking temperature is controlled at 450°C, the catalytic reactor is heated and kept warm by electric heating, and the catalyst is Al 2 o 3 -SiO 2solid catalyst. After running for 3 days, it will be regenerated in the catalyst regenerator. The regeneration method is air combustion and the temperature is 900°C. The high-temperature pyrolysis steam is exported from the outlet of the catalytic reactor into the condensation separation device, and light oil, pyrolysis water and pyrolysis gas are separated. Part of the pyrolysis gas is...
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