A waste volume reduction processing method includes a volume reduction step of reducing volume of waste in a volume reduction furnace in which temperature is raised in stages multiple times, the waste being a mixture of organic waste containing plastic and inorganic waste containing metal material, the volume reduction step including a first volume reduction step of storing and heating the waste in the volume reduction furnace in which temperature is raised up to around 200° C. to be kept, the volume reduction furnace being sealed in an oxygen-free state or in a low-oxygen state, the organic waste being reduced in volume to 20% to 30% of original volume.

A method for thermally decomposing a carbonaceous waste material including: filling a reactor defined by a reactor wall with the waste material and an auxiliary material, resulting in a reactor content, the auxiliary material including abrasive particles; heating the reactor contents in the absence of oxygen, such that gaseous products are formed by pyrolysis of the waste material and the abrasive particles do not melt or thermally decompose; moving the reactor contents during the pyrolysis, the moving being adapted to mix the reactor contents and to cause the abrasive particles to scrape over at least parts of the reactor wall. The auxiliary material has a composition to include a component adapted to bind halogens present in the gaseous products and/or so that the brittleness of the auxiliary material is greater than the brittleness of the reactor wall.

A process for converting solid plastic waste to hydrocarbon oil includes melting a feed comprising solid plastic waste to produce a liquefied plastic stream and visbreaking the liquefied plastic stream in a visbreaker unit having a visbreaker furnace and a soaker vessel. Visbreaking includes heating the liquefied plastic stream in the visbreaker furnace to produce a heated liquefied plastic stream, maintaining the heated liquefied plastic stream at the reaction temperature in the soaker vessel for a residence time to produce a visbreaker effluent, and injecting a stripping gas into the soaker vessel. The stripping gas includes at least one of steam, nitrogen, helium, argon, or combinations of these. The process includes introducing the stripping gas to the liquefied plastic stream upstream of the visbreaker furnace, the heated liquefied plastic stream downstream of the visbreaker furnace, or both. The visbreaker effluent is separated to produce a liquid hydrocarbon oil.

A process for converting solid plastic waste to hydrocarbon oil includes melting a feed comprising solid plastic waste to produce a liquefied plastic stream and visbreaking the liquefied plastic stream in a visbreaker unit having a visbreaker furnace and a soaker vessel. Visbreaking includes heating the liquefied plastic stream in the visbreaker furnace to produce a heated liquefied plastic stream, maintaining the heated liquefied plastic stream at the reaction temperature in the soaker vessel for a residence time to produce a visbreaker effluent, and injecting a stripping gas into the soaker vessel. The stripping gas includes at least one of steam, nitrogen, helium, argon, or combinations of these. The process includes introducing the stripping gas to the liquefied plastic stream upstream of the visbreaker furnace, the heated liquefied plastic stream downstream of the visbreaker furnace, or both. The visbreaker effluent is separated to produce a liquid hydrocarbon oil.

The present disclosure relates to degradation of polymer materials, such as plastic materials. More specifically, the present disclosure relates to a method for digestion of one or more plastic-comprising material by the use of at least one larva of the species selected from the group consisting of Galleria mellonella, Tenebrio molitor and Alphitobius diaperinus. The product obtained by the method is also within the inventive concept. The disclosure furthermore relates to use of said at least one larva for digestion of a plastic-comprising material.

The present disclosure relates to the production of biomass from at least one plastic polymer. More specifically, the present disclosure relates to use of a feed for production of biomass, wherein larvae of the family Pyralidae or of the family Tenebrionidae are fed on a feed comprising at least one plastic polymer, a related use of increasing pupation in a population of larva.

A process involving the steps in this order of: providing a waste plastics stream (A) comprising polyvinyl chloride (PVC); (i) supplying the waste plastics stream (A) to a reactor vessel; (ii) subjecting the waste plastics in the reactor vessel to a temperature of 250 C. and 350 C., preferably of 275 C. and 325 C., preferably for a period of 5-30 minutes, under applying a vacuum, preferably of 35 mbar, or using an inert gas sweep, and evacuating the generated hydrogen chloride (B) from the vessel, wherein the PVC is partially dechlorinated to form a waste plastics stream (C) comprising partially unsaturated PVC; (iii) removing the waste plastics stream (C) comprising partially unsaturated PVC from the reaction vessel; and (iv) separating the partially unsaturated PVC from the waste plastics stream to form a dechlorinated waste plastics stream (D).

The present application provides a treatment method and device for a waste plastic. A first aspect of the present application provides a treatment method for a waste plastic, including: firstly subjecting the waste plastic to a first pre-treatment to remove impurity and grease on a surface of the waste plastic, then subjecting the waste plastics to a second pre-treatment to convert a solid waste plastic into one in flow state; and finally, subjecting the waste plastic in flow state to a first cracking treatment and a second cracking treatment in sequence. Through the method provided in the present application, while cracking the waste plastic, chlorine element in the waste plastic may be removed by a multi-stage adsorption, which reduces chlorine content in the cracked oil, reduces pressure and burden in subsequent refining, and meets the limitation of the chlorine content in cracked products in downstream processes.

A method for recycling anode and/or cathode catalyst from the catalyst coated membranes comprising proton exchange membrane, a continuous nonporous cross-linked polyelectrolyte multilayer coating comprising alternating layers of a polycation polymer and a polyanion polymer, an anode coating layer comprising anode catalyst particles, a cathode coating layer comprising cathode catalyst particles, and optionally a second continuous nonporous cross-linked polyelectrolyte multilayer coating between the second surface of the proton exchange membrane and the cathode coating layer. The cross-linked polyelectrolyte multilayer coating between the proton exchange membrane and the anode and/or cathode catalyst coating layer is dissolved in an aqueous solution with a pH of greater than 7. The catalyst coated membrane is delaminated, and the anode and/or cathode catalyst is recovered.

The present disclosure relates to the production of biomass from at least one plastic polymer. More specifically, the present disclosure relates to use of a feed for production of biomass, wherein larvae of the family Pyralidae or of the family Tenebrionidae are fed on a feed comprising at least one plastic polymer, a related use of increasing pupation in a population of larva.