C12P19/02

System and method for producing a sugar stream with front end oil separation

An improved dry grind system and method for producing a sugar stream from grains or similar carbohydrate sources and/or residues, such as for biochemical production, with front end oil separation. Prior to or after saccharification, oil can be removed from a sugar/carbohydrate stream. After saccharification and prior to a sugar conversion process, the sugar/carbohydrate stream includes a desired Dextrose Equivalent (DE) where DE describes the degree of conversion of starch to dextrose can be produced, with such sugar stream being available for biochemical production, e.g., alcohol production, or other processes. In addition, the systems and methods also can involve the removal of certain grain components, e.g., corn kernel components, including protein and/or fiber. In other words, oil separation and sugar stream production occurs on the front end of the system and method.

Engineered microorganisms for the production of intermediates and final products

The present disclosure relates to a non-naturally occurring microorganism that includes an endogenous genetic deletion that eliminates the expression of at least a pyruvate kinase, where the genetically modified prokaryotic microorganism is capable of producing 3-deoxy-D-arabino-heptulosonate-7-phosphate.

IMMOBILIZED ENZYME PRODUCTION LINE, METHOD OF MAKING AN IMMOBILIZED ENZYME PRODUCTION LINE, AND METHOD OF MAKING COMPOUNDS USING THE IMMOBILIZED ENZYME PRODUCTION LINE
20220380747 · 2022-12-01 ·

An enzyme production line having a plurality of enzymes 3 bound to a support 4 for running a series of catalyzed reactions to convert a substrate 30 to a final product 32. A method of using the enzyme production line to form a final product 32 in which a substrate 30 contacts a first enzyme 3 bound to a support 4 to form an intermediate and contacting the intermediate with a second enzyme 3 bound to a support 4 to form a final product 32.

IMMOBILIZED ENZYME PRODUCTION LINE, METHOD OF MAKING AN IMMOBILIZED ENZYME PRODUCTION LINE, AND METHOD OF MAKING COMPOUNDS USING THE IMMOBILIZED ENZYME PRODUCTION LINE
20220380747 · 2022-12-01 ·

An enzyme production line having a plurality of enzymes 3 bound to a support 4 for running a series of catalyzed reactions to convert a substrate 30 to a final product 32. A method of using the enzyme production line to form a final product 32 in which a substrate 30 contacts a first enzyme 3 bound to a support 4 to form an intermediate and contacting the intermediate with a second enzyme 3 bound to a support 4 to form a final product 32.

NOVEL FRUCTOSE-4-EPIMERASE AND METHOD FOR PREPARING TAGATOSE USING SAME

The present application relates to a fructose-4-epimerase variant exhibiting tagatose conversion activity and a method for preparing tagatose using the same.

NOVEL FRUCTOSE-4-EPIMERASE AND METHOD FOR PREPARING TAGATOSE USING SAME

The present application relates to a fructose-4-epimerase variant exhibiting tagatose conversion activity and a method for preparing tagatose using the same.

IMPROVED METHOD FOR MANUFACTURING ALLULOSE

The present disclosure relates to an improved method for producing allulose and, more particularly, to a method for preparing a fructose-containing raw material solution by using raw sugar as a raw substrate used in the production process.

Process for enzymatic hydrolysis of lignocellulosic material and fermentation of sugars

The invention relates to a process for the preparation of a fermentation product from lignocellulosic material, comprising the following steps: a) optionally, pre-treatment of the lignocellulosic material, b) optionally, washing of the optionally pretreated lignocellulosic material, c) enzymatic hydrolysis of the optionally washed and/or optionally pretreated lignocellulosic material using an enzyme composition comprising at least two cellulases and whereby the enzyme composition at least comprises LPMO, and optionally purifying the hydrolysed lignocellulosic material, d) fermentation of the hydrolysed lignocellulosic material to produce a fermentation product, and e) optionally, recovery of a fermentation product, wherein oxygen is consumed in amounts corresponding to between 20 and 5000 mmol molecular oxygen per kg glucan present in the lignocellulosic material, the oxygen is added after the pretreatment and before and/or during the enzymatic hydrolysis of the lignocellulosic material, preferably in an amount corresponding to at least 30 mmol molecular oxygen per kg glucan present in the lignocellulosic material, more preferably in an amount corresponding to at least 40 mmol molecular oxygen per kg glucan present in the lignocellulosic material, and most preferably in an amount corresponding to at least 50 mmol molecular oxygen per kg glucan present in the lignocellulosic material is consumed.

Process for enzymatic hydrolysis of lignocellulosic material and fermentation of sugars

The invention relates to a process for the preparation of a fermentation product from lignocellulosic material, comprising the following steps: a) optionally, pre-treatment of the lignocellulosic material, b) optionally, washing of the optionally pretreated lignocellulosic material, c) enzymatic hydrolysis of the optionally washed and/or optionally pretreated lignocellulosic material using an enzyme composition comprising at least two cellulases and whereby the enzyme composition at least comprises LPMO, and optionally purifying the hydrolysed lignocellulosic material, d) fermentation of the hydrolysed lignocellulosic material to produce a fermentation product, and e) optionally, recovery of a fermentation product, wherein oxygen is consumed in amounts corresponding to between 20 and 5000 mmol molecular oxygen per kg glucan present in the lignocellulosic material, the oxygen is added after the pretreatment and before and/or during the enzymatic hydrolysis of the lignocellulosic material, preferably in an amount corresponding to at least 30 mmol molecular oxygen per kg glucan present in the lignocellulosic material, more preferably in an amount corresponding to at least 40 mmol molecular oxygen per kg glucan present in the lignocellulosic material, and most preferably in an amount corresponding to at least 50 mmol molecular oxygen per kg glucan present in the lignocellulosic material is consumed.

Compositions and methods for production of organic acids

Provided herein are compositions and methods for production of organic acids. In particular, provided herein are consolidated bioprocessing compositions and methods for single reactor production of organic acids.