Processing biomass
US-2015353974-A1 · Dec 10, 2015 · US
US9365876B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9365876-B2 |
| Application number | US-201113992443-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 8, 2011 |
| Priority date | Dec 9, 2010 |
| Publication date | Jun 14, 2016 |
| Grant date | Jun 14, 2016 |
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A method produces a chemical through continuous fermentation including: (a) culturing a cell in a culture medium in a fermentor to ferment a feedstock to produce a chemical; (b) conducting filtration of the culture medium with a separation membrane module; (c) separating a permeate containing the chemical from the culture medium while retaining a non-permeated liquid in the fermentor, and (d) supplying a gas from at least one of a lower portion of the separation membrane module and a pipe communicating between the fermentor and the separation membrane module to adjust a gas linear velocity in the separation membrane module to 0.15 cm/s to 70 cm/s while supplying the separation membrane module with a liquid.
Opening claim text (preview).
The invention claimed is: 1. A method of producing a chemical through continuous fermentation comprising: (a) culturing a cell in a culture medium in a fermentor to ferment a feedstock to produce a chemical; (b) conducting filtration of the culture medium with a separation membrane module; (c) separating a permeate containing the chemical from the culture medium while retaining a non-permeated liquid in the fermentor, and (d) supplying a gas from at least one of a lower portion of the separation membrane module and a pipe communicating between the fermentor and the separation membrane module to adjust a gas linear velocity in the separation membrane module to 0.15 cm/s to 70 cm/s while supplying the separation membrane module with the culture medium. 2. The method according to claim 1 , wherein in (d), the gas contains oxygen. 3. The method according to claim 2 , further comprising, in addition to (d), (e) supplying the fermentor with a gas, wherein: the gas is supplied in (d) intermittently, and when the gas is not supplied in (d), a supply rate of the gas in (e) is increased compared with that when the gas is supplied in (d). 4. The method according to claim 1 , wherein the filtration in (b) is conducted intermittently. 5. The method according to claim 1 , wherein the cell is a microorganism. 6. The method according to claim 5 , wherein the microorganism is a microorganism belonging to any of the Genus Escherichia , the Genus Providencia , the Genus Corynebacterium , the Genus Brevibacterium , and the Genus Serratia. 7. The method according to claim 6 , wherein the microorganism is any of Escherichia coli, Providencia rettgeri, Corynebacterium glutamicum, Brevibacterium flavum, Brevibacterium lactofermentum , and Serratia marcescens. 8. The method according to claim 1 , wherein the cell is a yeast. 9. The method according to claim 1 , wherein the chemical is an amino acid. 10. The method according to claim 9 , wherein the amino acid is L-threonine, L-lysine, L-glutamic acid, L-tryptophan, L-isoleucine, L-glutamine, L-arginine, L-alanine, L-histidine, L-proline, L-phenylalanine, L-aspartic acid, L-tyrosine, L-methionine, L-serine, L-valine, or L-leucine. 11. The method according to claim 1 , wherein the chemical is an organic acid. 12. The method according to claim 11 , wherein the chemical is lactic acid. 13. The method according to claim 1 , wherein the chemical is cadaverine.
Separation or concentration of fermentation products (bioreactors combined with means for distillation or extraction of liquid fuel C12M43/02) · CPC title
Lactic acid · CPC title
Percolation · CPC title
of pressure · CPC title
Lysine; Diaminopimelic acid; Threonine; Valine · CPC title
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