The present disclosure concerns recombinant yeast host cell for saccharification of a biomass. The recombinant yeast host cell has a genetic modification for expressing a heterologous polypeptide having glucoamylase activity (Penicillum oxalicum glucoamylase). In some embodiments, the heterologous polypeptide can comprise a signal sequence. The present disclosure also concerns a process for saccharification of a biomass using the recombinant yeast host cell as well as a process for fermenting the saccharified biomass into a fermentation product.

The present invention relates to processes of recovering oil after liquefaction and/or from thin stillage and/or syrup/evaporated centrate from a fermentation product production process by adding a thermostable protease to the whole stillage, thin stillage and/or syrup.

A process of recovering oil, comprising (a) converting a starch-containing material into dextrins with an alpha-amylase; (b) saccharifying the dextrins using a carbohydrate source generating enzyme to form a sugar; (c) fermenting the sugar in a fermentation medium into a fermentation product using a fermenting organism; (d) recovering the fermentation product to form a whole stillage; (e) separating the whole stillage into thin stillage and wet cake; (e′) optionally concentrating the thin stillage into syrup; (f) recovering oil from the thin stillage and/or optionally the syrup, wherein a protease and a phospholipase are present and/or added during steps (a) to (c). Use of a protease and a phospholipase for increasing oil recovery yields from thin stillage and/or syrup in a fermentation product production process.

Described are methods and compositions relating to granular starch-converting glucoamylases and α-amylases. The enzymes can be used to perform enzymatic starch hydrolysis of granular starch at or below the gelatinization temperature of insoluble granular starch.

Described are a recombinant host cell, a composition comprising a glucoamylase and methods of saccharifying the starch substrate using the glucoamylase. Moreover, the disclosure also relates to a process of producing fermentation products and a method for increasing starch digestibility in an animal as well as a method of producing a fermented beverage. The glucoamylase or 1,4-alpha-D-glucan glucohydrolase (EC 3.2.1.3) is preferably from the Mucorales-clade, especially having high sequence identity to the glucoamylase from Saksenaea vasiformis.

The present invention relates to variants of acid-alpha glucosidase and uses thereof. Said variants are sequence-optimized and/or are linked to a heterogenous signal peptide.

The invention is directed to non-natural yeast able to secrete significant amounts of glucoamylase into a fermentation media. The glucoamylase can promote degradation of starch material generating glucose for fermentation to a desired bioproduct, such as ethanol. The glucoamylase can be provided in the form of a glucoamylase fusion protein having secretion signal that is: derived from at least AA 1-19 of SEQ ID NO: 73, (ii) an amino acid sequence of at least AA 1-19 of SEQ ID NO: 74, (iii) SEQ ID NO: 77 (An aa), (iv) SEQ ID NO: 75 (Sc IV), (v) SEQ ID NO: 76 (Gg LZ), or (vi) SEQ ID NO: 78(Hs SA).

The present invention relates to filamentous fungal cells secreting a polypeptide of interest, wherein the expression of a citT gene is altered, reduced or eliminated compared to a non-mutated otherwise isogenic or parent cell, and methods of producing a secreted polypeptide of interest in said cells as well as methods of producing said cells.

The present invention relates to methods of mashing 100% adjunct grists. More specifically, the instant disclosure provides methods and compositions wherein an alpha-amylase in combination with an maltogenic alpha amylase and/or glucoamylse to make a non-malt wort composed by adjunct raw materials.

Aqueous fermentation feedstock and method of producing same. The feedstock includes glucose and dextrose oligomers, wherein (i) glucose concentration is in a range between 10 gram/Liter (g/L) and 150 g/L; (ii) dextrose oligomers concentration is in a range between 50 g/L and 300 g/L; and optionally (iii) slurried particles of less than 0.5 micron; (iv) slurried particles of more than 0.5 micron, wherein a content of such suspended particles of more than 0.5 micron is less than 30 g/L; (v) ash at a concentration in a range between 20 g/L and 50 g/L; (vi) lactate at a concentration in a range between 0.5 g/L and 10 g/L; (vii) protein at a concentration in a range between 5 g/L and 50 g/L; (viii) corn oil at a concentration of less than 10 g/L; and/or (ix) glycerol at a concentration in a range between 1 g/L and 30 g/L.