Partial adaptation for butanol production

US9663759B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-9663759-B2
Application numberUS-201414320681-A
CountryUS
Kind codeB2
Filing dateJul 1, 2014
Priority dateJul 3, 2013
Publication dateMay 30, 2017
Grant dateMay 30, 2017

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.

Provided herein are processes for producing an improved culture of cells comprising an engineered butanol biosynthetic pathway. The processes comprise (a) providing a cell culture of recombinant microorganisms comprising an engineered butanol biosynthetic pathway, wherein the engineered butanol biosynthetic pathway is minimal or not activated; and (b) growing the culture of recombinant microorganisms under adaptive conditions whereby pathway activation is increased to produce an improved cell culture and whereby the improved cell culture is capable of continuing to grow in fermentation.

First claim

Opening claim text (preview).

What is claimed is: 1. A process for producing a culture of cells comprising an engineered butanol biosynthetic pathway: a) providing a cell culture of recombinant microorganisms comprising an engineered butanol biosynthetic pathway, wherein the recombinant microorganisms produce butanol; b) growing the culture of recombinant microorganisms in a propagation phase wherein the propagation phase is characterized by aerobic conditions and a butanol concentration of about 0 g/L to about 10 g/L; and c) growing the culture of step b) in a production phase wherein the production phase is characterized by anaerobic conditions and a butanol concentration of at least 25 g/L, wherein the recombinant microorganism is selected from a genus from the group consisting of Clostridium, Zymomonas, Escherichia, Salmonella, Serratia, Erwinia, Klebsiella, Shigella, Rhodococcus, Pseudomonas, Bacillus, Lactobacillus, Lactococcus, Enterococcus, Alcaligenes, Paenibacillus, Arthrobacter, Corynebacterium, Brevibacterium, Schizosaccharomyces, Kluveromyces, Yarrowia, Pichia, Zygosaccharomyces, Debaryomyces, Candida, Brettanomyces, Pachysolen, Hansenula, Issatchenkia, Trichosporon, Yamadazyma , and Saccharomyces. 2. The process of claim 1 , wherein the engineered butanol biosynthetic pathway is selected from the group consisting of: (a) a 1-butanol biosynthetic pathway; (b) a 2-butanol biosynthetic pathway; and (c) an isobutanol biosynthetic pathway. 3. The process of claim 1 , wherein the rate of butanol production of the provided cell culture of recombinant microorganisms is less than 0.20 grams of butanol per gram of dry cell weight of cells per hour (g/g dcw/hr). 4. The process of claim 1 , wherein the cell culture of recombinant microorganisms is grown under adaptive conditions selected from at least one of a source of carbon substrate, a dissolved oxygen concentration, a temperature, a pH, a substrate concentration, a butanol concentration, a 2-butanone concentration, or a component of the fermentation medium. 5. The process of claim 4 , wherein the adaptive condition comprises a substrate concentration and a dissolved oxygen concentration. 6. The process of claim 5 , wherein the substrate is glucose. 7. The process of claim 6 , wherein the glucose concentration is about 1 g/L to about 50 g/L. 8. The process of claim 7 , wherein the dissolved oxygen concentration is greater than 5%. 9. The process of claim 8 , wherein specific oxygen uptake rate (Sp. OUR) of the recombinant microorganism is about 0.5 millimoles per gram cells per hour (mM/g cells/hr) to about 5 mM/g cells/hr. 10. The process of claim 4 , wherein the cell culture is characterized by at least one of an increase in biomass production, a reduction in the amount of time for the fermentation, or a reduction or elimination of the production of an inhibitory product. 11. The process of claim 10 , wherein growing the culture under adaptive conditions increases the biomass production of the culture to a cell density of about 5 g/L to about 15 g/L. 12. The process of claim 10 , wherein the inhibitory product is isobutyric acid. 13. The process of claim 12 , wherein the growing the culture under adaptive conditions reduces the isobutyric acid concentration to about 0.1 g/L to about 2.5 g/L. 14. The process of claim 4 , wherein the dissolved oxygen concentration is less than 5%. 15. The process of claim 14 , wherein specific oxygen uptake rate (Sp. OUR) of the recombinant microorganism is about 0 millimoles per gram cells per hour (mM/g cells/hour) to about 2.5 mM/g cells/hr. 16. The process of claim 4 , wherein the cell culture is characterized by at least one of an increase in biomass production, a reduction in the amount of time for the fermentation, an increase in butanol yield, an increase in butanol productivity, an increase in biomass yield, or a delay in the production of an inhibitory product. 17. The process of claim 16 , wherein growing the culture under adaptive conditions increases the biomass production of the culture such that the culture is capable of growing for at least one generation in the fermentation. 18. The process of claim 16 , wherein growing the culture under adaptive conditions increases the biomass production of the culture such that the culture is capable of growing for at least two generations in the fermentation. 19. The process of claim 16 , wherein the butanol yield is increased to at least 30 g/L.

Assignees

Inventors

Classifications

  • Butanols · CPC title

  • Biofuels, e.g. bio-diesel · CPC title

  • Genes encoding for enzymes or proenzymes · CPC title

  • C12N1/36Primary

    Adaptation or attenuation of cells · 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 US9663759B2 cover?
Provided herein are processes for producing an improved culture of cells comprising an engineered butanol biosynthetic pathway. The processes comprise (a) providing a cell culture of recombinant microorganisms comprising an engineered butanol biosynthetic pathway, wherein the engineered butanol biosynthetic pathway is minimal or not activated; and (b) growing the culture of recombinant microorg…
Who is the assignee on this patent?
Butamax Advanced Biofuels Llc
What technology area does this patent fall under?
Primary CPC classification C12N1/36. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue May 30 2017 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 1 related publication on this page (citations in our corpus or others sharing the same primary CPC).