A fermentation process includes contacting a starch hydrolysate with a glucoamylase with agitation. And allowing for settling to form a multi-phase solution. A first phase of the multi-phase solution includes a saccharide component comprising about 30 wt % to about 80 wt % (e.g., 30 wt % to 70 wt %, 30 wt % to 60 wt %) based on a total carbohydrate present. The method further includes draining the first phase to isolate the first phase from a second phase to form a fermentation broth comprising a first portion of the first phase. The method further includes fermenting the fermentation broth until a concentration of glucose in the fermentation broth is 40 g/L or less. The method includes adding a second portion of the first phase to the fermentation broth to maintain a concentration of glucose in a range of from about 1 g/L to about 20 g/L in the fermentation broth.

A fermentation process includes contacting a starch hydrolysate with a glucoamylase with agitation. And allowing for settling to form a multi-phase solution. A first phase of the multi-phase solution includes a saccharide component comprising about 30 wt % to about 80 wt % (e.g., 30 wt % to 70 wt %, 30 wt % to 60 wt %) based on a total carbohydrate present. The method further includes draining the first phase to isolate the first phase from a second phase to form a fermentation broth comprising a first portion of the first phase. The method further includes fermenting the fermentation broth until a concentration of glucose in the fermentation broth is 40 g/L or less. The method includes adding a second portion of the first phase to the fermentation broth to maintain a concentration of glucose in a range of from about 1 g/L to about 20 g/L in the fermentation broth.

The present invention relates to isolated polypeptides having cellobiohydrolase activity and polynucleotides encoding the polypeptides. The invention also relates to nucleic acid constructs, vectors, and host cells comprising the polynucleotides as well as methods of producing and using the polypeptides.

The present invention relates to isolated polypeptides having cellobiohydrolase activity and polynucleotides encoding the polypeptides. The invention also relates to nucleic acid constructs, vectors, and host cells comprising the polynucleotides as well as methods of producing and using the polypeptides.

A method of producing saccharides, in which fluidity of the slurry including biomass can be retained; the used amount of the degrading enzyme can be reduced; and high concentration saccharides can be produced, is provided. In addition, a method of producing ethanol, in which high concentration ethanol can produced, is provided. The method of producing saccharides includes the steps of: adding a cellulose degrading enzyme to a slurry including a biomass; and degrading the cellulose included in the biomass by the degrading enzyme to produce saccharide including glucose as a major component. The concentration of the cellulose is retained at 75 g/L or less in a mixed solution including the slurry, the degrading enzyme, and an adsorption inhibitor inhibiting adsorption of the degrading enzyme to a lignin contained in the biomass.

A method of producing saccharides, in which fluidity of the slurry including biomass can be retained; the used amount of the degrading enzyme can be reduced; and high concentration saccharides can be produced, is provided. In addition, a method of producing ethanol, in which high concentration ethanol can produced, is provided. The method of producing saccharides includes the steps of: adding a cellulose degrading enzyme to a slurry including a biomass; and degrading the cellulose included in the biomass by the degrading enzyme to produce saccharide including glucose as a major component. The concentration of the cellulose is retained at 75 g/L or less in a mixed solution including the slurry, the degrading enzyme, and an adsorption inhibitor inhibiting adsorption of the degrading enzyme to a lignin contained in the biomass.

Processes and systems for recovering products from a fermentation mash. In some examples, a process for recovering products from a fermentation mash can include processing a ground corn product to produce a fermentation mash that can include ethanol. At least a portion of the ethanol can be separated from the fermentation mash to produce a whole stillage. The whole stillage can be separated to produce a fiber rich product and a filtrate. The fiber rich product can be hydrolyzed to produce a saccharification mash. The saccharification mash can be processed to produce additional ethanol and a stillage protein product.

Processes and systems for recovering products from a fermentation mash. In some examples, a process for recovering products from a fermentation mash can include processing a ground corn product to produce a fermentation mash that can include ethanol. At least a portion of the ethanol can be separated from the fermentation mash to produce a whole stillage. The whole stillage can be separated to produce a fiber rich product and a filtrate. The fiber rich product can be hydrolyzed to produce a saccharification mash. The saccharification mash can be processed to produce additional ethanol and a stillage protein product.

Systems and methods are provided for integrated conversion of biomass to ultimately form naphtha and/or diesel boiling range products. The integrated conversion can include an initial conversion of biomass to alcohols, such as by fermentation, followed by conversion of alcohols to olefins and then olefins to naphtha, jet, and diesel boiling range compounds, with high selectivity for formation of diesel boiling range compounds. The integrated conversion process can be facilitated by using a common catalyst for both the conversion of alcohols to olefins and the conversion of olefins to naphtha and/or diesel boiling range compounds. For example, ZSM-48 (an MRE zeotype framework structure catalyst) can be used as the catalyst for both conversion of alcohols to olefins and for oligomerization of olefins with increased selectivity for formation of diesel boiling range products.

Systems and methods are provided for integrated conversion of biomass to ultimately form naphtha and/or diesel boiling range products. The integrated conversion can include an initial conversion of biomass to alcohols, such as by fermentation, followed by conversion of alcohols to olefins and then olefins to naphtha, jet, and diesel boiling range compounds, with high selectivity for formation of diesel boiling range compounds. The integrated conversion process can be facilitated by using a common catalyst for both the conversion of alcohols to olefins and the conversion of olefins to naphtha and/or diesel boiling range compounds. For example, ZSM-48 (an MRE zeotype framework structure catalyst) can be used as the catalyst for both conversion of alcohols to olefins and for oligomerization of olefins with increased selectivity for formation of diesel boiling range products.