C12P19/14

Trichoderma filamentous fungus mutant strain and method of producing protein

A mutant strain of a filamentous fungus of the genus Trichoderma having a reduced function of a polypeptide consisting of the amino acid sequence represented by SEQ ID NO: 2; and a method of producing a sugar from a cellulose-containing biomass, the method including: step a of producing a cellulase by cultivating a Trichoderma reesei mutant strain having a reduced function of a polypeptide consisting of the amino acid sequence represented by SEQ ID NO: 2, and step b of saccharifying the biomass by using the cellulase obtained in the step a.

SYSTEM AND METHOD FOR PRODUCING A SUGAR STREAM WITH FRONT END OIL SEPARATION
20230079475 · 2023-03-16 ·

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.

SYSTEM AND METHOD FOR PRODUCING A SUGAR STREAM WITH FRONT END OIL SEPARATION
20230079475 · 2023-03-16 ·

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.

USE OF DISTILLABLE VOLATILE SALT FOR THE PRETREATMENT OF BIOMASS

The present invention provides for a method to produce a sugar from a biomass, the method comprising: (a) providing a first mixture comprising a solubilized biomass and a distillable acid-base conjugate salt (DABCS) or deep eutectic solvent (DES), wherein (i) the DABCS is a protic ionic liquid (PIL) or a protic salt comprising a DABCS cation and a DABCS anion, and (ii) the DES is any combination of Lewis or Brønsted acid and base comprising any anionic and/or cationic species that have sufficient vapor pressure so that it can be readily distilled; and (b) distilling at least part of the DABCS from the first mixture in order to separate the at least part of the DABCS from the first mixture.

USE OF DISTILLABLE VOLATILE SALT FOR THE PRETREATMENT OF BIOMASS

The present invention provides for a method to produce a sugar from a biomass, the method comprising: (a) providing a first mixture comprising a solubilized biomass and a distillable acid-base conjugate salt (DABCS) or deep eutectic solvent (DES), wherein (i) the DABCS is a protic ionic liquid (PIL) or a protic salt comprising a DABCS cation and a DABCS anion, and (ii) the DES is any combination of Lewis or Brønsted acid and base comprising any anionic and/or cationic species that have sufficient vapor pressure so that it can be readily distilled; and (b) distilling at least part of the DABCS from the first mixture in order to separate the at least part of the DABCS from the first mixture.

Alpha-amylase variants and polynucleotides encoding same

The present invention relates to variants of a parent alpha-amylase. The present invention also relates to polynucleotides encoding the variants and to nucleic acid constructs, vectors, and host cells comprising the polynucleotides, and methods of using the variant enzymes.

Alpha-amylase variants and polynucleotides encoding same

The present invention relates to variants of a parent alpha-amylase. The present invention also relates to polynucleotides encoding the variants and to nucleic acid constructs, vectors, and host cells comprising the polynucleotides, and methods of using the variant enzymes.

METHOD FOR INCREASING BACKSET RECYCLE IN DRY GRIND ALCOHOL PRODUCTION

The present invention relates to a dry grind ethanol process in which post-distillation backset is subjected to aerobic fermentation to remove components that are inhibitory to an ethanolagen, such as yeast, allowing the utilization of an increased amount of post-distillation backset during the initial preparation of starch-containing substrates for the dry grind ethanol process. Aerobic fermentation of the post-distillation backset allows substantially higher backset recycle, resulting in fresh water savings and increased sustainability.

METHOD FOR INCREASING BACKSET RECYCLE IN DRY GRIND ALCOHOL PRODUCTION

The present invention relates to a dry grind ethanol process in which post-distillation backset is subjected to aerobic fermentation to remove components that are inhibitory to an ethanolagen, such as yeast, allowing the utilization of an increased amount of post-distillation backset during the initial preparation of starch-containing substrates for the dry grind ethanol process. Aerobic fermentation of the post-distillation backset allows substantially higher backset recycle, resulting in fresh water savings and increased sustainability.

CORN SWEET STEEPING
20230131928 · 2023-04-27 ·

Described is a process for releasing soluble starch hydrolysates or hydrolysed starch syrup from substantially intact corn kernels during high temperature steeping at a temperature at or above the gelatinization temperature of starch in the corn kernels, and the recovery of protein and oil-enhanced, carbohydrate-depleted residuals that are ideally suited for use as high quality animal feed or other food-grade products.