US2016280882A1PendingUtilityA1
Process For Recycling Polyacetals
Est. expiryNov 24, 2031(~5.4 yrs left)· nominal 20-yr term from priority
C08G 2/36C08G 65/06C08G 65/16C08G 2/10C07D 323/06C08J 2359/02C07D 323/00C08J 11/16C07D 323/04C07C 47/04C08G 2650/62C08G 65/30C08J 11/28Y02W30/62C08J 2359/00Y02P20/10
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Claims
Abstract
A process for recycling polyoxymethylene polymers is disclosed. A polyoxymethylene polymer is at least partially dissolved in an aprotic compound. The resulting solution or suspension (liquid mixture) is then contacted with a catalyst which causes the polyoxymethylene polymer to be converted into a cyclic acetal. The cyclic acetal can be separated, collected and used in other processes. In one embodiment, the cyclic acetal may be used to produce a polyoxymethylene polymer.
Claims
exact text as granted — not AI-modified1 .- 20 . (canceled)
21 . A process for the recycling of oxymethylene homo- or copolymers comprising the steps:
a) at least partly dissolving an oxymethylene homo- or copolymer in an aprotic compound; b) converting the at least partly dissolved oxymethylene homo- or copolymer in the presence of a catalyst to cyclic acetals; and c) converting the cyclic acetals obtained in step b) optionally together with comonomer(s) to oxymethylene polymers.
22 . A process according to claim 21 , wherein at least 20 wt.-% of the oxymethylene homo- or copolymer is dissolved in the aprotic compound.
23 . A process according to claim 21 , wherein the oxymethylene polymer is at least partly dissolved at a temperature higher than 100° C.
24 . A process according to claim 21 , wherein the aprotic compound has a boiling point of 120° C. or higher, determined at 1 bar.
25 . A process according to claim 21 , wherein the oxymethylene polymer, the aprotic compound and the catalyst form a reaction mixture and wherein the reaction mixture comprises at least 60 wt.-% of the aprotic compound, wherein the weight is based on the total weight of the reaction mixture.
26 . A process according to claim 21 , wherein the aprotic compound comprises a sulfur containing organic compound.
27 . A process according to claim 21 , wherein the aprotic compound comprises a dipolar nitro-group free compound.
28 . A process according to claim 21 , wherein the aprotic compound is represented by formula (I):
wherein
n is an integer ranging from 1 to 6, and
wherein the ring carbon atoms may optionally be substituted by one or more substituents, selected from C 1 -C 8 -alkyl which may be branched or unbranched.
29 . A process according to claim 21 , wherein the aprotic compound is sulfolane.
30 . A process according to claim 21 , wherein the aprotic compound is represented by formula (II):
wherein R 1 and R 2 are independently selected from C 1 -C 8 -alkyl which may be branched or unbranched.
31 . A process according to claim 21 , wherein the aprotic compound is represented by formula (III):
wherein
n is an integer ranging from 1 to 6, and
wherein the ring carbon atoms may optionally be substituted by one or more substituents, selected from C 1 -C 8 -alkyl which may be branched or unbranched; or
the aprotic compound is represented by formula (IV):
wherein R 3 and R 4 are independently selected from C 1 -C 8 -alkyl which may be branched or unbranched.
32 . A process according to claim 21 , wherein the conversion to the cyclic acetal is carried out at a temperature ranging from 40° C. to 130° C. and is carried out at a pressure of from 10 millibars to 10 bars.
33 . A process according to claim 21 , wherein higher than 30 percent of the oxymethylene homo- or copolymer is converted into the cyclic acetal.
34 . A process according to claim 21 , further comprising the step of converting the cyclic acetals formed during the process into an oxymethylene polymer.
35 . A process according to claim 21 , wherein the oxymethylene homo- or copolymer is at least partly dissolved in the aprotic compound while being heated and wherein the resulting liquid medium is cooled prior to being contacted with the catalyst.Cited by (0)
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