Process and systems for obtaining 1,4-butanediol from fermentation broths

US2018237367A1 · US · A1

Patent metadata
FieldValue
Publication numberUS-2018237367-A1
Application numberUS-201715845398-A
CountryUS
Kind codeA1
Filing dateDec 18, 2017
Priority dateMar 15, 2013
Publication dateAug 23, 2018
Grant date

How to read this patent

A practical reading order for non-experts. Skip the full description unless you need deep technical detail.

  1. Title

    What the patent document calls the invention.

  2. Abstract

    A short plain-language summary of the technical disclosure.

  3. Assignees and inventors

    Who owns or filed the patent and who is credited as inventor.

  4. Key dates

    Filing, priority, publication, and grant dates set the timeline.

  5. First independent claim

    The legal scope of protection — read this for what is actually claimed.

  6. CPC / IPC classifications

    Technology tags used to group this patent with similar filings.

  7. Citations and related patents

    Prior art links and similar publications in this corpus.

Abstract

Official abstract text for this publication.

A process of purifying 1,4-butanediol (1,4-BDO) from a fermentation broth including separating solid materials, salts and water, and subjecting the resulting material to a two, three or four column distillation system, that can include a wiped film evaporator to produce a purified 1,4-butanediol product.

First claim

Opening claim text (preview).

1 . A process of purifying 1,4-butanediol (1,4-BDO) comprising: (a) subjecting a crude 1,4-BDO mixture to a first column distillation procedure to remove materials with a boiling point lower than 1,4-BDO from the crude 1,4-BDO mixture to produce a first 1,4-BDO-containing product stream; and (b) subjecting the first 1,4-BDO-containing product stream to a second column distillation procedure to remove materials with boiling points higher than 1,4-BDO as a first high-boilers stream, to produce a purified 1,4-BDO product, wherein the purified 1,4-BDO product is collected from a side-draw of the second column distillation procedure. 2 . The process of claim 1 , further comprising (c) subjecting the first high-boilers stream to wiped-film evaporation (WFE) to produce a first WFE distillate and subjecting the first WFE distillate to step (b). 3 . The process of claim 1 further comprising (d) subjecting the first 1,4-BDO-containing product stream, prior to performing step (b), to an intermediate column distillation procedure to remove materials with boiling points higher than 1,4-BDO as a second high-boilers stream. 4 . The process of claim 3 , further comprising (c) subjecting the second high-boilers stream to wiped-film evaporation (WFE) producing a second WFE distillate and subjecting the second WFE distillate to step (d). 5 . The process of claim 3 further comprising (e) treating the first 1,4-BDO-containing product stream with a hydrogenation reaction prior to performing step (b). 6 . The process of claim 1 further comprising (f) treating the purified 1,4-BDO product with a hydrogenation reaction. 7 . The process of claim 1 wherein the crude 1,4-BDO mixture is at least 50% (w/w), 60% (w/w), 70% (w/w), 80% (w/w), 85% (w/w) or 90% (w/w) 1,4-BDO. 8 . The process of claim 1 , wherein the purified 1,4-BDO product is greater than 90% (w/w), 91% (w/w), 92% (w/w), 93% (w/w), 94% (w/w), 95% (w/w), 96% (w/w), 97%, (w/w) 98% (w/w), 99% (w/w), 99.1% (w/w), 99.2% (w/w), 99.3% (w/w), 99.4% (w/w), 99.5% (w/w), 99.6% (w/w), 99.7% (w/w), 99.8% (w/w) or 99.9% (w/w), 1,4-BDO. 9 . The process of claim 1 , wherein recovery of 1,4-BDO in the purified 1,4-BDO product from the crude 1,4-BDO mixture is greater than 40%, 50%, 60%, 70%, 80%, 90%, 95%, 96%, 97%, 98% or 99%. 10 . The process of claim 1 , wherein the purified 1,4-BDO product collected from the side draw is in a vapor phase. 11 . The process of claim 1 , wherein the first column distillation procedure and second column distillation procedures are each performed at pressures equal to or less than atmospheric pressure. 12 . The process of claim 11 , wherein the pressure of the first column distillation procedure differs from the pressure of the second distillation procedure. 13 . The process of claim 1 further comprising culturing a modified non-naturally occurring organism to produce a 1,4-BDO in a fermentation broth, subjecting the fermentation broth to a separation procedure to obtain a separated 1,4-BDO product, and subjecting the separated 1,4-BDO product to water removal and salt removal to produce the crude 1,4-BDO mixture, wherein the separation procedure consists of a first filtration and a second filtration, wherein the first filtration is microfiltration or ultrafiltration, and wherein the second filtration is nanofiltration. 14 . The process of claim 13 , further comprising subjecting the crude 1,4-BDO mixture to a polishing ion exchange using a polishing ion exchange resin that is an anion exchange resin. 15 . The process of claim 13 , wherein the water removal is by evaporation. 16 . The process of claim 13 , wherein the salt removal is by primary ion exchange. 17 . A system for purifying 1,4-BDO comprising: a first distillation column receiving a crude 1,4-BDO mixture and generating a first stream of materials with boiling points lower than 1,4-BDO and a 1,4-BDO-containing product stream; a second distillation column receiving the 1,4-BDO-containing product stream at a feed point and generating a first stream of materials with boiling points higher than 1,4-BDO, a second stream of materials with boiling points lower than 1,4-BDO, and a purified 1,4-BDO product from a side-draw; and a wiped-film evaporator receiving the first stream of materials with boiling points higher than 1,4-BDO and generating a distillate, wherein the distillate is fed to the second distillation column. 18 . The system of claim 17 further comprising a hydrogenation reactor constructed to treat the purified 1,4-BDO product generated by the second distillation column. 19 - 21 . (canceled) 22 . The system of claim 17 , wherein the side-draw is located above the feed point of the second distillation column. 23 - 39 . (canceled)

Assignees

Inventors

Classifications

  • by two or more of a fractionation, separation or rectification step · CPC title

  • 1,4-Butanediol; 1,3-Butanediol; 1,2-Butanediol; 2,3-Butanediol · CPC title

  • by continuous methods · CPC title

  • Separation; Purification; Use of additives, e.g. for stabilisation · CPC title

  • Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring · CPC title

Patent family

Related publications grouped by family.

External sources

Frequently asked questions

Answers are generated from the same data shown on this page.

What does patent US2018237367A1 cover?
A process of purifying 1,4-butanediol (1,4-BDO) from a fermentation broth including separating solid materials, salts and water, and subjecting the resulting material to a two, three or four column distillation system, that can include a wiped film evaporator to produce a purified 1,4-butanediol product.
Who is the assignee on this patent?
Genomatica Inc
What technology area does this patent fall under?
Primary CPC classification C07C29/80. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Thu Aug 23 2018 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).