Invention Grant
- Patent Title: Method and device for the destructive distillation of polyethylene and polypropylene waste
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Application No.: US17294269Application Date: 2019-07-03
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Publication No.: US11884783B2Publication Date: 2024-01-30
- Inventor: Remzi Iskanderovich Seidametov , Sabri Narimanovich Setmanbetov
- Applicant: Remzi Iskanderovich Seidametov , Sabri Narimanovich Setmanbetov
- Applicant Address: RU Simferopol
- Assignee: Remzi Iskanderovich Seidametov,Sabri Narimanovich Setmanbetov
- Current Assignee: Remzi Iskanderovich Seidametov,Sabri Narimanovich Setmanbetov
- Current Assignee Address: RU Simferopol
- Agency: Aird & McBurney LP
- Priority: RU 2019101720 2019.01.22
- International Application: PCT/RU2019/000475 2019.07.03
- International Announcement: WO2020/096482A 2020.05.14
- Date entered country: 2021-05-14
- Main IPC: C08J11/06
- IPC: C08J11/06 ; C10B53/07 ; C08J11/04

Abstract:
The invention relates to a method and device for processing industrial and domestic polyethylene and polypropylene waste by destructive distillation. A method for the destructive distillation of polyethylene and polypropylene waste includes charging a destructive distillation reactor with polyethylene and polypropylene waste that has been pre-cleaned of contaminants by flotation, and heating the furnace of the distillation reactor using a fuel burner; maintaining the temperature in a hydrocarbon collector tank using exhaust gases, regulating the outlet temperature of a vapour-gas mixture of hydrocarbons, and recovering paraffin fractions; fractionating the remaining distillation products in a fractionating column, and regulating the outlet temperature of the remaining vapour-gas mixture from the fractionating column; cooling the remaining vapour-gas mixture, separating same into a naphtha fraction and a gas fraction, and charging a subsequent destructive distillation reactor with feedstock, wherein prior to charging, the bottom part of each reactor is coated with a layer of a non-stick lubricant, the reactor furnaces are connected with the aid of air cushions, and the reactors are charged in several steps according to the following cycle: “charging a reactor with feedstock, generating a vacuum in the charged reactor space, heating the reactor to 110-260° C. to liquefy the charged feedstock”.
Public/Granted literature
- US20220002515A1 METHOD AND DEVICE FOR THE DESTRUCTIVE DISTILLATION OF POLYETHYLENE AND POLYPROPYLENE WASTE Public/Granted day:2022-01-06
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