Methods and devices for mechanical separation of multilayer interlayers
US-2024217227-A1 · Jul 4, 2024 · US
US12036563B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12036563-B2 |
| Application number | US-202017427254-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 31, 2020 |
| Priority date | Feb 1, 2019 |
| Publication date | Jul 16, 2024 |
| Grant date | Jul 16, 2024 |
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The invention pertains to a process for separating mixtures of solids based on their densities. The present invention also relates to the use of a separating liquid (L) for separating plastic solids from metal-containing solids based on their densities, wherein the separating liquid (L) has a density d3 such that 1.5<d3<2.0; wherein the solids have a particle size ranging from 0.1 to 100 mm. The separating liquid (L) is preferably a fluorinated fluid.
Opening claim text (preview).
The invention claimed is: 1. A process for separating mixtures of solids based on their densities, comprising: a) bringing a mixture of at least one plastic solid and at least one metal-containing solid having two distinct densities d1 and d2, into contact with a separating liquid (L) having a density d3, distinct from d1 and d2, wherein 1.5<d3<2.0, wherein the separating fluid (L) is a fluorinated fluid selected from the group consisting of fluorinated polyethers, fluorinated alkyl polymers, and fluorinated heteroalkyl polymers and wherein the solids have a particle size ranging from 0.1 to 100 mm; b) separating the at least one plastic solid from the at least one metal-containing solid by a density separation; c) optionally repeating steps a) and b). 2. The process according to claim 1 , wherein the plastic solid is filled or unfilled and comprises at least one component selected from the group consisting of cellulose acetate, cellulose butyrate, cellulose propionate, ethylene vinyl acetate (EVA), polyamides, polybutylene (PB), polycarbonate (PC), poly(carbonate/ester), polyethylene terephthalate glycol (PETG), glycol modified copolyester (PCTG), polybutylene terephthalate (PBT), polyethylene terephthalate (PET), copolyester PBT/PET, polyetherimide (PEI), low-density polyethylene (LDPE), medium-density polyethylene (MDPE), High-density polyethylene (HDPE), polyphenylene oxide/polystyrene (PPO/PS), polyphenylene sulfide (PPS), polypropylene (PP), polystyrene (PS), polyaryl ether sulfone (PAES), polyaryl ether ketone (PAEK), polyurethane (PU), polyvinylchloride (PVC), polyvinyl difluoride (PVDF), styrene-acrylonitrile (SAN) and thermoplastic elastomers (T/P elastomers). 3. The process according to claim 1 , wherein the plastic solid comprises at least one polyaryl ether sulfone (PAES) and or at least one polyaryl ether ketone (PAEK). 4. The process according to claim 1 , wherein the metal-containing solid is selected from the group consisting of cast iron, carbon steel, manganese steel, chrome steel, chromium-nickel steel, stainless steel, copper, brass, tin bronze, aluminium, titanium, titanium alloys and magnesium. 5. The process according to claim 1 , wherein the separating fluid (L) is a fluorinated fluid comprising at least one fluoropolyether (PFPE) chain. 6. The process according to claim 1 , wherein the separating fluid (L) is a fluorinated fluid comprising at least one fluoropolyether (PFPE) chain of formula (III): [(CF 2 O) n (CF 2 CF 2 O) m ]p (III) wherein: n and m, independently from each other, are integers ≥0, the number average molecular weight (Mn) of the chain is between 400 and 10,000. 7. The process according to claim 6 , wherein formula (III) is such that m and n are both integers >0, and the ratio m/n ranges between 0.1 and 10. 8. The process according to claim 1 , wherein the separating fluid (L) has a density as follows: 1.55<d3<1.9. 9. The process according to claim 1 , further comprising removing floating solids after contact with the separating liquid (L) and drying the solids. 10. The process according to claim 2 , wherein the plastic solid comprises at least one polyamide selected from the group consisting of PA 6,6, PA 6, PA 6,10, PA 6,12, PA 11, PA 12. 11. The process according to claim 7 , wherein the ratio m/n ranges between 0.5 and 10.
Polysulfones; Polyethersulfones · CPC title
from phenols · CPC title
using selective solvents for polymer components · CPC title
PSU, i.e. polysulfones; PES, i.e. polyethersulfones or derivatives thereof · CPC title
Use of {PA, i.e.} polyamides, e.g. polyesteramides {or derivatives thereof}, as moulding material · CPC title
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