C12P7/52

Controlling process gases

Biomass (e.g., plant biomass, animal biomass, and municipal waste biomass) is processed to produce useful intermediates and products, such as energy, fuels, foods or materials. For example, equipment, systems and methods are described that can be used to treat feedstock materials, such as cellulosic and/or lignocellulosic materials, in a vault in which hazardous gases are removed, destroyed and/or converted. The treatments are efficient and can reduce the recalcitrance of the lignocellulosic material so that it is easier to produce an intermediate or product, e.g., sugars, alcohols, sugar alcohols and energy, from the lignocellulosic material.

Butyrate-producing bacterium and use thereof

A butyrate-producing bacterium belonging to Anaerostipes hadrus is provided. The amount of butyrate produced is at least 1.5 times that of Anaerostipes hadrus YIT 10092.sup.T (DSM 3319.sup.T) and is measured by thawing a frozen stock solution of the bacterial strain (a 10% (w/v) skim milk-2% sodium glutamate solution with suspended bacterial cells) (cell count: 2.0 to 5.510.sup.10 cells/mL), inoculating the solution at 1% to 4 mL of a PY liquid medium supplemented with 33 mM sodium acetate and 0.5 (w/v) % glucose (PYGA medium), followed by anaerobic culture at 37 C. for 24 hours, then inoculating the culture solution at 1% to a PYGA medium, followed by anaerobic culture at 37 C. for 24 hours, then inoculating the culture solution at 1% to a PY medium containing 33 mM sodium acetate and 0.5 (w/v) % L-sorbose, followed by anaerobic culture at 37 C. for 24 hours, and then measuring the butyrate concentration.

Butyrate-producing bacterium and use thereof

A butyrate-producing bacterium belonging to Anaerostipes hadrus is provided. The amount of butyrate produced is at least 1.5 times that of Anaerostipes hadrus YIT 10092.sup.T (DSM 3319.sup.T) and is measured by thawing a frozen stock solution of the bacterial strain (a 10% (w/v) skim milk-2% sodium glutamate solution with suspended bacterial cells) (cell count: 2.0 to 5.510.sup.10 cells/mL), inoculating the solution at 1% to 4 mL of a PY liquid medium supplemented with 33 mM sodium acetate and 0.5 (w/v) % glucose (PYGA medium), followed by anaerobic culture at 37 C. for 24 hours, then inoculating the culture solution at 1% to a PYGA medium, followed by anaerobic culture at 37 C. for 24 hours, then inoculating the culture solution at 1% to a PY medium containing 33 mM sodium acetate and 0.5 (w/v) % L-sorbose, followed by anaerobic culture at 37 C. for 24 hours, and then measuring the butyrate concentration.

INTEGRATED MIXOTROPHIC FERMENTATION METHOD

Integrated mixotrophic fermentation method comprising (i) an isolated naturally acetogenic organism; (ii) a first feedstock comprising a carbon source for use in a fermentation medium; (iii) a second feedstock comprising elemental hydrogen for use in the fermentation medium; wherein the second feedstock comprises performing electrolysis; and (iv) culturing the organism in the fermentation medium, whereby both feedstocks are metabolized and a fermentation broth is formed, which broth comprises at least one bioproduct.

PROCESS FOR PRODUCING BTX AND ALCOHOLS BY CATALYTIC PYROLYSIS OF BIOMASS AND FERMENTATION OF THE GASEOUS PYROLYSIS EFFLUENT

A process is described for producing BTX and alcohols from biomass, by a) catalytic pyrolysis of the biomass in a fluidized-bed reactor producing a gaseous pyrolysis effluent; b) separation of said gaseous pyrolysis effluent into at least one BTX fraction and a gaseous effluent containing at least carbon monoxide and carbon dioxide, c) sending all of the gaseous effluent from separation b) into fermentation producing a liquid fermentation stream containing at least one stream containing at least one oxygenated compound chosen from alcohols, diols, acid alcohols, carboxylic acids, aldehydes, ketones and esters, d) separating the fermentation stream obtained on conclusion of c) into at least the stream containing at least one oxygenated compound, an aqueous fraction, and an unreacted gaseous effluent, e) recycling at least part of unreacted gaseous effluent into the catalytic pyrolysis a).

ACETYL-COA CARBOXYLASES

The present invention provides various combinations of genetic modifications to a transformed host cell that provide increase conversion of carbon to a chemical product. The present invention also provides methods of fermentation and methods of making various chemical products.

ACETYL-COA CARBOXYLASES

The present invention provides various combinations of genetic modifications to a transformed host cell that provide increase conversion of carbon to a chemical product. The present invention also provides methods of fermentation and methods of making various chemical products.

METHOD FOR PRODUCING 3-HYDROXYPROPIONIC ACID AND OTHER PRODUCTS
20190119708 · 2019-04-25 ·

This invention relates to metabolically engineered microorganism strains, such as bacterial strains, in which there is an increased utilization of malonyl-CoA for production of a chemical product, which includes 3-hydroxypropionic acid.

METHOD FOR PRODUCING 3-HYDROXYPROPIONIC ACID AND OTHER PRODUCTS
20190119708 · 2019-04-25 ·

This invention relates to metabolically engineered microorganism strains, such as bacterial strains, in which there is an increased utilization of malonyl-CoA for production of a chemical product, which includes 3-hydroxypropionic acid.

METHOD FOR PRODUCING ISOBUTENE FROM 3-METHYLCROTONYL-COA

Described is a method for the production of isobutene from 3-methylcrotonyl-CoA comprising the steps of: (a) enzymatically converting 3-methylcrotonyl-CoA into 3-methylbutyric acid; and (b) further enzymatically converting the thus produced 3-methylbutyric acid into isobutene.

The conversion of 3-methylcrotonyl-CoA into 3-methylbutyric acid can be achieved by first enzymatically converting 3-methylcrotonyl-CoA into 3-methyl butyryl-CoA and further enzymatically converting the thus produced 3-methylbutyryl-CoA into 3-methylbutyric acid. Alternatively, the conversion of 3-methylcrotonyl-CoA into 3-methylbutyric acid can be achieved by first enzymatically converting 3-methylcrotonyl-CoA into 3-methylcrotonic acid and then further enzymatically converting the thus produced 3-methylcrotonic acid into 3-methylbutyric acid.