B29B2017/0244

MULTILAYER STRUCTURE, AND SEPARATION METHOD AND RECYCLING METHOD THEREFOR
20240116281 · 2024-04-11 · ·

Provided are a multilayer structure and the like being superior in adhesiveness of an interlayer under high humidity and separability of a barrier layer in water, and even in a case in which the barrier layer is exposed to water in a separating and collecting step, being superior in viscosity stability after separating and collecting a resin that constitutes the barrier layer. The multilayer structure of the present invention is a multilayer structure including a barrier layer (A), a water-soluble layer (B), and an adhesive layer (C), in which: the adhesive layer (C) is laminated via the water-soluble layer (B) on one or both faces of the barrier layer (A); the barrier layer (A) contains a polyamide or an ethylene-vinyl alcohol copolymer (a1) as a principal component; and the water-soluble layer (B) contains an alkali metal ion (b1) at a content of 100 ppm or more and 2,000 ppm or less.

Process for separating a fibrous target component from textile waste

A process (1, 101, 201) for separating a fibrous target component (21) from textile waste (2, 5) is shown, said textile waste (2, 5) containing the target component (21) and at least one ancillary component (22), whereby the target component (21) consists of water-swellable textile fibers (51) with a density higher than the density of water, the process (1, 101, 201) comprising the steps: a) dispersing the comminuted textile waste (5) in an aqueous solution (7) to obtain a suspension (8) containing the textile waste (5), and b) separating the dispersed textile waste (5) into a high-density target fraction (81) comprising the target component (21), and a low-density residual fraction (82) comprising the at least one ancillary component (22), according to the respective density of said components (21, 22). In order to provide a reliable, fast process for the separation of water-swellable fibers from other textile fibers which are similar in density, it is proposed, that the aqueous solution (7) is an alkaline aqueous solution (7) and the target component fibers (51) are swelled in the alkaline aqueous solution (7) prior to step b), thereby increasing the density and weight of said target component (21) relative to the density and weight of the ancillary component (22).

METHOD AND APPARATUS FOR WASHING PLASTICS MATERIALS
20190321831 · 2019-10-24 ·

Method for washing a plastics material and for separating contaminating substances therefrom comprises the steps of: supplying a first flow of a washing fluid together with the plastics material with contaminants to a washing container in which a stirrer generates a turbulent action to detach mechanically the contaminants adhering to the plastics material, enabling a first fraction of heavier contaminants to precipitate onto a first bottom portion of the container, thus performing a first action of separating contaminants; transferring a second flow: of fluid with floating plastics material from the container to a first separating chamber, in which a second separating action takes place with the precipitation of a second fraction of the contaminants onto a second bottom portion of the first chamber; conveying a third flow of fluid with floating plastics material from the first chamber to a second separating chamber and evacuating by overflowing an outgoing flow of fluid together with the processed plastics material; in the transit froth the first chamber to the second chamber the agglomerates of floating plastics are disaggregated, and to the third flow and to the plastics material a downward propelling action inside the second chamber is imparted to promote a third separating action with precipitation of a third fraction of the contaminants onto a third bottom portion of the second chamber; removing from the second chamber a recirculation flow comprising precipitated fluid and contaminants and sending the recirculation flow to a screen unit that retains the contaminants, returning the washing fluid to the first or second chamber. The apparatus for implementing the aforesaid method is also disclosed.

SYSTEMS FOR MANUFACTURING BULKED CONTINUOUS FILAMENT FROM RECYCLED PET
20190263022 · 2019-08-29 ·

A system for manufacturing bulked continuous carpet filament that is adapted for providing a polymer melt and dividing the polymer melt into a plurality of streams (e.g., at least six or eight streams) to increase a surface area of the polymer melt. The plurality of streams is then exposed to a pressure that is below approximately 5 millibars. The streams are then recombined into a single polymer stream and formed into bulked continuous carpet filament. In various embodiments, an extruder, such as a multi-screw extruder, is used to divide the polymer melt into the plurality of streams.

METHODS FOR MANUFACTURING BULKED CONTINUOUS FILAMENT FROM RECYCLED PET
20240157605 · 2024-05-16 · ·

A method of manufacturing bulked continuous carpet filament that includes providing a polymer melt and separating the polymer melt from the extruder into at least eight streams. The multiple streams are exposed to a chamber pressure within a chamber that is below approximately 25 millibars, or another predetermined pressure. The streams are recombined into a single polymer stream. Polymer from the polymer stream is then formed into bulked continuous carpet filament.

WASTE PLASTIC DENSITY SEPARATION

Methods and systems for separating mixed plastic waste are provided herein. The methods generally comprise separating the mixed plastic waste into a PET-enriched stream and one or more PET-depleted streams. The separating may be accomplished using the combinations of two or more density separation stages. Exemplary density separation stages include sink-float separators and centrifugal force separators. The PET-enriched and PET-depleted streams may be recovered and/or directed to downstream chemical recycling processes.

Method, process and system for recycling an asphalt-based roofing material

The present disclosure provides a method, process and system for recycling an asphalt-based roofing material. In particular, the method, process and system are capable of removing and recovering an aggregate product, fiber product and an asphalt product from the asphalt-based roofing material. The aggregate, fiber and asphalt products each may be reused in a variety of applications.

DISPOSABLE DIAPER RECYCLING AND APPLICATIONS THEREOF
20190183071 · 2019-06-20 · ·

One embodiment provides a modular green roof tray, house plant growth media and horticulture growth media, and a tree protection mat for weed and moisture control made from recycled disposable diapers. The growth medium and tree protection mat contain superabsorbent materials from diaper that can absorb waters and greatly reduce irrigation so to provide a drought resistant feature. One embodiment also provides a manufacturing process to perform 100% recycling of disposed diapers.

Method of separating waste material
10279510 · 2019-05-07 · ·

A method of separating waste material to a plurality of separated materials is disclosed herein. The method is effected by subjecting the waste material to a separation according to specific gravity, to thereby obtain two or more fractions, and optionally subjecting one or more of said fractions to additional separation procedures, to thereby obtain two or more of a low-density polymeric material, a high-density polymeric material, a metal, a glass, an oil, and lignocelluloses. The disclosed method can further be effected by processing one or more of the separated materials to thereby obtain one or more processed materials of a beneficial use. Further disclose herein are separated and/or processed materials obtainable by the method, articles-of-manufacturing comprising same, and systems for separating and/or processing the waste material.

SYSTEMS AND METHODS FOR MANUFACTURING BULKED CONTINUOUS FILAMENT FROM COLORED RECYCLED PET
20190118413 · 2019-04-25 ·

A method of manufacturing bulked continuous carpet filament that includes providing a polymer melt and separating the polymer melt from the extruder into at least eight streams. The multiple streams are exposed to a chamber pressure within a chamber that is below approximately 5 millibars. The streams are recombined into a single polymer stream and formed into bulked continuous carpet filament.