Furan-2,5-dicarboxylic acid purge process

US2015321119A1 · US · A1

Patent metadata
FieldValue
Publication numberUS-2015321119-A1
Application numberUS-201414317782-A
CountryUS
Kind codeA1
Filing dateJun 27, 2014
Priority dateMay 8, 2014
Publication dateNov 12, 2015
Grant date

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

Official abstract text for this publication.

Disclosed is an oxidation process to produce a crude carboxylic acid product carboxylic acid product. The process comprises oxidizing a feed stream comprising at least one oxidizable compound to generate a crude carboxylic acid slurry comprising furan-2,5-dicarboxylic acid (FDCA) and compositions thereof. Also disclosed is a process to produce a dry purified carboxylic acid product by utilizing various purification methods on the crude carboxylic acid.

First claim

Opening claim text (preview).

We claim: 1 . A process to produce an impurity rich waste stream stream in a carboxylic acid process, said process comprising: contacting a mother liquor in a solvent recovery zone to produce said impurity rich waste stream; wherein said mother liquor stream comprises at least one of the following: (i) 2,5-diformylfuran in an amount ranging from about 150 ppm to about 2.0 wt %, (ii) levulinic acid in an amount ranging from about 150 ppm to about 2.0 wt %, (iii) succinic acid in an amount ranging from about 150 ppm to about 2.0 wt %, and (iv) acetoxy acetic acid in an amount ranging from about 150 ppm to about 2.0 wt %. 2 . A process according to claim 1 wherein said process further comprises routing a portion of said impurity rich waste stream to a solid-liquid separation zone to form a purge mother liquor stream. 3 . A process according to claim 2 wherein said process further comprises routing a portion of said purge mother liquor stream to a mix zone to form an extraction feed stream. 4 . A process according to claim 1 wherein said process further comprises routing said extraction feed stream to an extraction zone to form a purge stream, a raffinate stream, and an extract stream. 5 . A process according to claim 1 wherein said solvent recovery zone comprises at least one evaporator. 6 . A process according to claim 1 wherein impurity rich waste stream is a slurry with weight % solids greater than 10%. 7 . A process according to claim 1 wherein impurity rich waste stream is a slurry with weight % solids greater than 30%. 8 . A process according to claim 1 wherein impurity rich waste stream is a slurry with weight % solids greater than 50%. 9 . A process according to claim 1 wherein said solvent recovery zone comprises at least two evaporators. 10 . A process according to claim 1 wherein said mother liquor stream comprises at least two of the following: (i) 2,5-diformylfuran in an amount ranging from about 150 ppm to about 2.0 wt %, (ii) levulinic acid in an amount ranging from about 150 ppm to about 2.0 wt %, (iii) succinic acid in an amount ranging from about 150 ppm to about 2.0 wt %, and (iv) acetoxy acetic acid in an amount ranging from about 150 ppm to about 2.0 wt %. 11 . A process according to claim 1 wherein said mother liquor stream comprises at least three of the following: (i) 2,5-diformylfuran in an amount ranging from about 150 ppm to about 2.0 wt %, (ii) levulinic acid in an amount ranging from about 150 ppm to about 2.0 wt %, (iii) succinic acid in an amount ranging from about 150 ppm to about 2.0 wt %, and (iv) acetoxy acetic acid in an amount ranging from about 150 ppm to about 2.0 wt %. 12 . A process according to claim 1 wherein said mother liquor stream comprises: (i) 2,5-diformylfuran in an amount ranging from about 150 ppm to about 2.0 wt %, (ii) levulinic acid in an amount ranging from about 150 ppm to about 2.0 wt %, (iii) succinic acid in an amount ranging from about 150 ppm to about 2.0 wt %, and (iv) acetoxy acetic acid in an amount ranging from about 150 ppm to about 2.0 wt %.

Assignees

Inventors

Classifications

  • Purification; Separation (separation of optically-active compounds C07B57/00); Stabilisation; Use of additives · CPC title

  • Furfural · CPC title

  • Fractional distillation {or use of a fractionation or rectification column} · CPC title

  • of carboxyl groups or salts, halides or anhydrides thereof · CPC title

  • Flash distillation · CPC title

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What does patent US2015321119A1 cover?
Disclosed is an oxidation process to produce a crude carboxylic acid product carboxylic acid product. The process comprises oxidizing a feed stream comprising at least one oxidizable compound to generate a crude carboxylic acid slurry comprising furan-2,5-dicarboxylic acid (FDCA) and compositions thereof. Also disclosed is a process to produce a dry purified carboxylic acid product by utilizing…
Who is the assignee on this patent?
Eastman Chem Co
What technology area does this patent fall under?
Primary CPC classification B01J27/32. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Thu Nov 12 2015 00:00:00 GMT+0000 (Coordinated Universal Time) (A1). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).