Polyolefin mimic polyester copolymers
US-2024218116-A1 · Jul 4, 2024 · US
US2023295396A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2023295396-A1 |
| Application number | US-202118010995-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jun 15, 2021 |
| Priority date | Jun 17, 2020 |
| Publication date | Sep 21, 2023 |
| Grant date | — |
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A process (1, 2) for processing feedstock containing cotton fibres and PET fibres, the process (1, 2) comprises: i. heating a suspension of feedstock containing cotton fibres and PET fibres in water at a temperature above 180° C. to produce a mixture comprising char; ii. removing the water from the mixture comprising char; iii. adding a base to the mixture comprising char to produce a terephthalate salt in a liquid phase; iv. removing the char from the liquid phase to produce dried char; v. acidifying the liquid phase to produce terephthalic acid.
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1 . A process for processing feedstock containing cotton fibres and PET fibres, the process comprising: i. heating a suspension of feedstock containing cotton fibres and PET fibres in water at a temperature above 180° C. to produce a mixture comprising char; ii. removing the water from the mixture comprising char; iii. adding a base to the mixture comprising char to produce a terephthalate salt in a liquid phase; iv. removing the char from the liquid phase to produce dried char; v. acidifying the liquid phase to produce terephthalic acid. 2 . A process according to claim 1 , further comprising shredding the feedstock prior to Step i. 3 . A process according to claim 1 , wherein the ratio of water to feedstock is between 4:1 to 8:1 (w/w). 4 . A process according to claim 1 , wherein Step i. comprises heating a suspension of feedstock containing cotton fibres and PET fibres in water at a temperature of between 180 to 240° C. 5 . A process according to claim 1 , wherein Step i. further comprises heating a suspension of feedstock containing cotton fibres and PET fibres in water under a pressure of greater than 2.0×10 6 Pa (20 bar). 6 . A process according to claim 2 , wherein Step ii. Comprises removing the water from the mixture comprising char via filtration. 7 . A process according to claim 1 , further comprising recovering ethylene glycol from the water removed in Step ii. of the process. 8 . A process according to claim 1 , wherein Step iii. comprises adding a base comprising ammonia and/or ammonium hydroxide to the mixture comprising char to produce diammonium terephthalate in a liquid phase. 9 . A process according to claim 8 , wherein Step iii. is performed at a temperature, e.g. between 0 to 40° C. 10 . A process according to claim 1 , wherein Step iv. comprises filtering the char from the liquid phase and further comprises drying the filtered char to produce a solid fuel. 11 . (canceled) 12 . A process according to claim 1 , further comprising forming pellets and/or briquettes from the char to form a solid fuel. 13 . A process according to claim 1 , further comprising Step vi. purifying the liquid phase by contacting the liquid phase with one or more of activated carbon or clay. 14 . A process according to claim 12 , wherein Step vi. is performed after Step iii. and before Step v. 15 . A process according to claim 12 , comprising subsequently removing the activated carbon and/or clay by filtration. 16 . (canceled) 17 . A process according to claim 1 , wherein the pure terephthalic acid is collected via filtration. 18 . A process according to claim 1 , further comprising Step vii. torrefaction of the mixture comprising char. 19 . A process according to claim 18 , wherein Step vii. is performed after Step ii. and before Step iii. of the process. 20 . A process according to claim 18 , wherein Step vii. is performed at a temperature between 200 to 280° C. 21 . A process according to claim 18 , wherein Step vii. is performed for less than one hour. 22 . Terephthalic acid produced from the process of claim 1 .
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