Co2 electroreduction to multi-carbon products in strong acid
US-2024093390-A1 · Mar 21, 2024 · US
US12378338B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12378338-B2 |
| Application number | US-202117194998-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 8, 2021 |
| Priority date | Sep 14, 2018 |
| Publication date | Aug 5, 2025 |
| Grant date | Aug 5, 2025 |
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To provide a method for producing pellets from which an ion exchange membrane excellent in stability of the electrolysis voltage can be formed, pellets, and an ion exchange membrane. The method for producing pellets of the present invention is a method for producing pellets, which comprises extruding a melt containing a fluorinated polymer having groups convertible to ion exchange groups from a die of a melt-extruder to obtain a strand containing the fluorinated polymer, and cutting the strand to obtain pellets containing the fluorinated polymer, wherein the temperature of the die when the melt containing the fluorinated polymer is extruded from the die is less than 200° C., and when the groups convertible to ion exchange groups of the fluorinated polymer are converted to ion exchange groups, the ion exchange capacity of the resulting fluorinated polymer is at least 1.1 milliequivalent/g dry resin.
Opening claim text (preview).
What is claimed is: 1. A method for producing pellets, comprising: extruding a melt comprising a fluorinated polymer from a die of a melt-extruder to obtain a strand comprising the fluorinated polymer; and cutting the strand to obtain pellets comprising the fluorinated polymer, wherein the extruding of the melt is from the die having a temperature of less than 200° C., and the fluorinated polymer has convertible groups which are convertible to ion exchange groups such that the fluorinated polymer has ion exchange capacity of at least 1.1 milliequivalent/g dry resin upon conversion of the convertible groups to ion exchange groups. 2. The method for producing pellets according to claim 1 , wherein the cutting of the strand produce the pellets having a light transmittance of from 30 to 60%. 3. The method for producing pellets according to claim 1 , wherein the ion exchange capacity of the fluorinated polymer upon conversion of the convertible groups is at most 2.00 milliequivalent/g dry resin. 4. The method for producing pellets according to claim 1 , wherein the convertible groups are convertible to carboxylic acid functional groups or sulfonic acid functional groups. 5. The method for producing pellets according to claim 1 , wherein the fluorinated polymer is a copolymer of a fluorinated olefin and a monomer of formula (1), CF 2 ═CF—(O) p —(CF 2 ) q —(CF 2 CFX) r —(O) s —(CF 2 ) t —(CF 2 CFX′) u -A 1 where X and X are each independently a fluorine atom or a trifluoromethyl group, A 1 is a group convertible to a carboxylic acid functional group, p is an integer of 0 or 1, q is an integer of from 0 to 12, r is an integer of from 0 to 3, s is an integer of from 0 or 1, t is an integer of from 0 to 12, and u is an integer of from 0 to 3, provided that 1≤p+s, and 1≤r+u. 6. The method for producing pellets according to claim 1 , wherein the fluorinated polymer is a copolymer of a fluorinated olefin and a monomer of formula (2), CF 2 ═CF-L-(A) n where L is a n+1 valent perfluorinated hydrocarbon group which may contain an oxygen atom, n is 1 or 2, and A is a group convertible to a sulfonic acid functional group. 7. The method for producing pellets according to claim 6 , wherein the monomer of the formula (2) is a compound of formula (2-1), CF 2 ═CF—O—R f1 -A, a compound of formula (2-2), CF 2 ═CF—R f1 -A, or a compound of formula (2-3), where r is 0 or 1; R f1 is a perfluoroalkylene group which may contain an oxygen atom between carbon atoms, R f2 is a single bond or a perfluoroalkylene group which may contain an oxygen atom between carbon atoms, and A is as defined for the formula (2). 8. The method for producing pellets according to claim 1 , further comprising: processing the pellets to form an ion-exchange membrane. 9. The method for producing pellets according to claim 1 , wherein the temperature of the die when the melt is extruded from the die is at least 140° C. 10. The method for producing pellets according to claim 1 , wherein the temperature of the die when the melt is extruded from the die is at most 160° C. 11. The method for producing pellets according to claim 1 , wherein the temperature of the die when the melt is extruded from the die is at least 140° C. and at most 150° C. 12. The method for producing pellets according to claim 1 , wherein the ion exchange capacity of the fluorinated polymer upon conversion of the convertible groups is at least 1.2 milliequivalent/g dry resin and at most 1.90 milliequivalent/g dry resin.
based on organic materials · CPC title
Homopolymers or copolymers of esters containing halogen atoms · CPC title
containing fluorine atoms · CPC title
containing fluorine · CPC title
Powdering or granulating · CPC title
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