Catalytic cracking method and system for waste plastics
A technology of catalytic cracking and waste plastics, which is applied in the field of catalytic cracking of waste plastics, can solve the problems of low added value of products, failure of pyrolysis oil, and substandard products, and achieve good environmental benefits, good environmental protection, and reduced carbon emissions. Effect
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Embodiment 1
[0061] The crushed waste plastic A is sent to the waste plastic pretreatment unit through the screw feeder. The waste plastic pretreatment unit adopts an external heating dissolving tank, and after mixing with the pretreatment agent and solvent oil, the impurities are removed at 320°C and 1MPa For processing, the residence time of waste plastic A is 30 minutes, and the material after the reaction is separated into insoluble matter and impurity-removed plastic-containing solution by a solid-liquid separation unit. The silicon content in the obtained impurity-containing plastic solution was 1.8 μg / g, and the chlorine content was 17.3 μg / g.
[0062] The solvent oil that adopts is the catalytic cracking diesel oil fraction obtained by the catalytic cracking unit of the present invention, and its distillation range is 205~360 ℃, and the total aromatics content is 78.2 mass %, and the single-ring aromatics content is 53.1 mass %; the weight of solvent oil and waste plastics The rati...
Embodiment 2
[0065] The crushed waste plastic A is sent to the waste plastic pretreatment unit through the screw feeder. The waste plastic pretreatment unit adopts an external heating dissolving tank, and after mixing with the pretreatment agent and solvent oil, the impurities are removed at 300°C and 2MPa For processing, the residence time of waste plastic A is 30 minutes, and the material after the reaction is separated into insoluble matter and impurity-removed plastic-containing solution by a solid-liquid separation unit. The silicon content in the obtained impurity-containing plastic solution was 2.5 μg / g, and the chlorine content was 18.2 μg / g.
[0066] The solvent oil used is refinery VGO, its distillation range is 275-581°C, the total aromatics content is 45.1% by mass, and the single-ring aromatics content is 21% by mass; the weight ratio of solvent oil to waste plastics is 5:1.
[0067] The pretreatment agent used is activated carbon and Fe 2 o 3 A mixture of activated carbon a...
Embodiment 3
[0069] The crushed waste plastic A is sent to the waste plastic pretreatment unit through the screw feeder. The waste plastic pretreatment unit adopts an external heating dissolving tank, and after mixing with the pretreatment agent and solvent oil, the impurities are removed at 300°C and 2MPa For processing, the residence time of waste plastic A is 30 minutes, and the material after the reaction is separated into insoluble matter and impurity-removed plastic-containing solution by a solid-liquid separation unit. The silicon content in the obtained impurity-containing plastic solution was 1.5 μg / g, and the chlorine content was 17.7 μg / g.
[0070] The solvent oil used is catalytic cracking light cycle oil, its distillation range is 156-338°C, the total aromatics content is 76.8% by mass, and the single-ring aromatics content is 63.8% by mass; the weight ratio of solvent oil to waste plastics is 5:1 .
[0071] The pretreatment agent used is activated carbon and Fe 2 o 3 A mix...
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