Abstract: The invention relates to a process for the preparation of a fermentation product from lignocellulosic material, comprising the following steps: a) optionally, pretreatment 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 the amounts of formed hydrolysed oxidation products at the end of the enzymatic hydrolysis by the oxidation by LPMO of the lignocellulosic material containing cellulose and/or cello-oligosaccharides is kept between 3 to 80 g/kg glucan present in the lignocellulosic material by adding a s

Abstract: The invention relates to a process for the preparation of a fermentation product from lignocellulosic material, comprising the following steps: a) optionally, pretreatment 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 the amounts of formed hydrolysed oxidation products at the end of the enzymatic hydrolysis by the oxidation by LPMO of the lignocellulosic material containing cellulose and/or cello-oligosaccharides is kept between 3 to 80 g/kg glucan present in the lignocellulosic material by adding a s

Abstract: The invention relates to a process for the preparation of a fermentation product from lignocellulosic material, comprising the following steps: a) optionally, pretreatment 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 the amounts of formed hydrolysed oxidation products at the end of the enzymatic hydrolysis by the oxidation by LPMO of the lignocellulosic material containing cellulose and/or cello-oligosaccharides is kept between 3 to 80 g/kg glucan present in the lignocellulosic material by adding a su

Abstract: A process for the isolation of levulinic acid obtained by acid catalyzed hydrolysis of a C6-carbohydrate-containing feedstock, including the following steps: a) providing a solution 1 comprising at least 5 wt. % of levulinic acid, at least 0.1 wt. % of formic acid and at most 94.9 wt. % of solvent, relative to the total weight of solution 1, b) feeding solution 1 to a first evaporation step to treat solution 1 and to obtain solution 2, comprising at least 25 wt. % of levulinic acid, less than 20 wt. % of solvent and at least 1 wt. % of formic acid, relative to the total weight of solution 2, c) feeding solution 2 to a second evaporation step to treat solution 2 and to obtain solution 3, comprising at least 30 wt. % of levulinic acid and less than 1.0 wt. % of formic acid, relative to the total weight of solution 3, d) feeding solution 3 to a third evaporation step to treat solution 3 and to obtain levulinic acid with a purity of at least 90 wt. % and containing less than 1000 wppm angelica lactone.

Abstract: A levulinic acid composition A having: a. at least 95 wt. % of levulinic acid; b. between 5 wppm and 5000 wppm of formic acid; and c. less than 1000 wppm of angelica lactone, based on the total weight of the composition. A process for the isolation of a levulinic acid composition, having the following steps: a. performing acid catalyzed hydrolysis of a C6 carbohydrate-containing feedstock to obtain reaction product X, b. subjecting of reaction product X to solid-liquid separation to provide a composition 1, c. feeding composition 1 to at least two purification steps to treat composition 1 to obtain a levulinic acid composition, wherein a second or a further purification step is a melt crystallization step.

Abstract: A process for the isolation of levulinic acid obtained by acid catalyzed hydrolysis of a C6-carbohydrate-containing feedstock, including the following steps: a) providing a solution 1 comprising at least 5 wt. % of levulinic acid, at least 0.1 wt. % of formic acid and at most 94.9 wt. % of solvent, relative to the total weight of solution 1, b) feeding solution 1 to a first evaporation step to treat solution 1 and to obtain solution 2, comprising at least 25 wt. % of levulinic acid, less than 20 wt. % of solvent and at least 1 wt. % of formic acid, relative to the total weight of solution 2, c) feeding solution 2 to a second evaporation step to treat solution 2 and to obtain solution 3, comprising at least 30 wt. % of levulinic acid and less than 1.0 wt. % of formic acid, relative to the total weight of solution 3, d) feeding solution 3 to a third evaporation step to treat solution 3 and to obtain levulinic acid with a purity of at least 90 wt. % and containing less than 1000 wppm angelica lactone.

Abstract: A process for the isolation of levulinic acid obtained by acid catalyzed hydrolysis of a C6-carbohydrate-containing feedstock, including the following steps: a) providing a solution 1 comprising at least 5 wt. % of levulinic acid, at least 0.1 wt. % of formic acid and at most 94.9 wt. % of solvent, relative to the total weight of solution 1, b) feeding solution 1 to a first evaporation step to treat solution 1 and to obtain solution 2, comprising at least 25 wt. % of levulinic acid, less than 20 wt. % of solvent and at least 1 wt. % of formic acid, relative to the total weight of solution 2, c) feeding solution 2 to a second evaporation step to treat solution 2 and to obtain solution 3, comprising at least 30 wt. % of levulinic acid and less than 1.0 wt. % of formic acid, relative to the total weight of solution 3, d) feeding solution 3 to a third evaporation step to treat solution 3 and to obtain levulinic acid with a purity of at least 90 wt. % and containing less than 1000 wppm angelica lactone.

Abstract: The invention relates to a process for the preparation of a fermentation product from lignocellulosic material, comprising the following steps: a) optionally, pretreatment 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 the amounts of formed hydrolysed oxidation products at the end of the enzymatic hydrolysis by the oxidation by LPMO of the lignocellulosic material containing cellulose and/or cello-oligosaccharides is kept between 3 to 80 g/kg glucan present in the lignocellulosic material by adding a s

Abstract: A process for the isolation of levulinic acid including the following steps: a. performing acid catalyzed hydrolysis of a C6 carbohydrate-containing feedstock to obtain reaction product X, b. purifying of reaction product X to provide a composition 1, comprising at least 75 wt. % levulinic acid, at most 15 wt. % solvent and at most 10 wt. % impurities, based on the total weight of composition 1, c. feeding composition 1 to a melt crystallization cycle, d. repeating the melt crystallization cycle as many times as necessary to obtain as composition 2 a levulinic acid with a predetermined purity, and e. isolating the levulinic acid with a predetermined purity.

Abstract: A process for the isolation of levulinic acid obtained by acid catalyzed hydrolysis of a C6-carbohydrate-containing feedstock, including the following steps: a) providing a solution 1 comprising at least 5 wt. % of levulinic acid, at least 0.1 wt. % of formic acid and at most 94.9 wt. % of solvent, relative to the total weight of solution 1, b) feeding solution 1 to a first evaporation step to treat solution 1 and to obtain solution 2, comprising at least 25 wt. % of levulinic acid, less than 20 wt. % of solvent and at least 1 wt. % of formic acid, relative to the total weight of solution 2, c) feeding solution 2 to a second evaporation step to treat solution 2 and to obtain solution 3, comprising at least 30 wt. % of levulinic acid and less than 1.0 wt. % of formic acid, relative to the total weight of solution 3, d) feeding solution 3 to a third evaporation step to treat solution 3 and to obtain levulinic acid with a purity of at least 90 wt. % and containing less than 1000 wppm angelica lactone.

Abstract: A process for the purification of levulinic acid including the following steps: a. providing a composition 1, comprising at least 75 wt. % of levulinic acid; b. cooling composition 1 to at least one temperature Tc, wherein Tc is a temperature in the range 1.23*(W1)?104.5?Tc (° C.)?1.23*(W1)?89.5, wherein W1 is the weight % of levulinic acid in composition 1, to obtain a cooled composition 1; c. performing melt crystallization of composition 1 including the steps of: i. bringing the cooled composition 1 into contact with levulinic acid crystal seeds, ii. allowing the levulinic acid in composition 1 to crystallize at at least one temperature Tc to obtain crystals 1 and liquid 1, and iii. draining of liquid 1; d. optionally, treating crystals 1, after draining of liquid 1, by sweating, according to the following steps: i. heating the crystals 1 at a temperature between 5 and 40° C. to obtain crystals 2 and liquid 2, and ii. draining of liquid 2; e.

Abstract: A levulinic acid composition A having: a. at least 95 wt. % of levulinic acid; b. between 5 wppm and 5000 wppm of formic acid; and c. less than 1000 wppm of angelica lactone, based on the total weight of the composition. A process for the isolation of a levulinic acid composition, having the following steps: a. performing acid catalyzed hydrolysis of a C6 carbohydrate-containing feedstock to obtain reaction product X, b. subjecting of reaction product X to solid-liquid separation to provide a composition 1, c. feeding composition 1 to at least two purification steps to treat composition 1 to obtain a levulinic acid composition, wherein a second or a further purification step is a melt crystallization step.

Abstract: A process for the purification of levulinic acid including the following steps: a. providing a composition 1, comprising at least 75 wt. % of levulinic acid; b. cooling composition 1 to at least one temperature Tc, wherein Tc is a temperature in the range 1.23*(W1)?104.5?Tc (° C.)?1.23*(W1)?89.5, wherein W1 is the weight % of levulinic acid in composition 1, to obtain a cooled composition 1; c. performing melt crystallization of composition 1 including the steps of: i. bringing the cooled composition 1 into contact with levulinic acid crystal seeds, ii. allowing the levulinic acid in composition 1 to crystallize at at least one temperature Tc to obtain crystals 1 and liquid 1, and iii. draining of liquid 1; d. optionally, treating crystals 1, after draining of liquid 1, by sweating, according to the following steps: i. heating the crystals 1 at a temperature between 5 and 40° C. to obtain crystals 2 and liquid 2, and ii. draining of liquid 2; e.

Abstract: The invention provides a process for the isolation of levulinic acid and formic acid from a composition comprising formic acid and levulinic acid, said process comprising a solid-liquid separation step, a vapor removal step, and a solvent-solvent extraction step, wherein a vapor condensate vapor and/or an aqueous phase from the solvent extraction is used to wash the solid fraction. Washing with vapor condensate results in higher levulinic acid yields (higher levulinic acid recovery) as compared to washing with normal water. Washing with aqueous phase results in a less compressible filter cake. Washing first with aqueous phase and subsequently with condensate results in even higher levulinic acid yields. The process is suitable for isolating levulinic acid and formic acid from compositions made by acid hydrolysis of a lignocellulosic biomass, and also from compositions made by acid hydrolysis of sugars such as glucose and fructose.

Abstract: The invention relates to a process for the preparation of a fermentation product from lignocellulosic material, comprising the following steps: a) optionally, pretreatment 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 the amounts of formed hydrolysed oxidation products at the end of the enzymatic hydrolysis by the oxidation by LPMO of the lignocellulosic material containing cellulose and/or cello-oligosaccharides is kept between 3 to 80 g/kg glucan present in the lignocellulosic material by adding a s

Abstract: The invention relates to a process for the production of 5-formylvaleric acid and adipic acid or esters thereof from an isomeric mixture of pentenoic acid or esters thereof said mixture comprising at least 4-pentenoic acid or esters thereof, and further comprising 3-pentenoic acid and/or 2-pentenoic acid or esters thereof. The process allows for efficient production of two different intermediates for producing polyamide using a single process, with good selectivity, little waste, in an economically efficient fashion. The process is very suitable to use an isomeric pentenoic acid mixture obtained from valerolactone, and can be used to produce renewable polyamide intermediates using a single process.

Abstract: The invention relates to a process for the production of 5-formylvaleric acid and adipic acid or esters thereof from an isomeric mixture of pentenoic acid or esters thereof said mixture comprising at least 4-pentenoic acid or esters thereof, and further comprising 3-pentenoic acid and/or 2-pentenoic acid or esters thereof. The process allows for efficient production of two different intermediates for producing polyamide using a single process, with good selectivity, little waste, in an economically efficient fashion. The process is very suitable to use an isomeric pentenoic acid mixture obtained from valerolactone, and can be used to produce renewable polyamide intermediates using a single process.

Abstract: A process for producing furfural and levulinic acid from lignocellulose-comprising biomass is disclosed. The biomass is slurried using water and optionally an acid, subjected to hydrolysis, and then subjected to a solid/liquid separation to yield at least an aqueous fraction comprising C5 and C6 sugars and a solid fraction comprising cellulose and lignin. Furfural is obtained by adding an organic solvent to the aqueous fraction, heating at 120-220° C. for a sufficient time to form furfural, cooling, and separating an organic phase comprising at least part of the furfural from an aqueous phase. Levulinic acid is obtained by suspending the solid fraction in water and optionally an acid, heating the suspension to 140-220° C., and separating an aqueous fraction comprising the levulinic acid from a solid fraction.

Abstract: The invention provides a process for the isolation of levulinic acid and formic acid from a composition comprising formic acid and levulinic acid, said process comprising a solid-liquid separation step, a vapor removal step, and a solvent-solvent extraction step, wherein a vapor condensate vapor and/or an aqueous phase from the solvent extraction is used to wash the solid fraction. Washing with vapor condensate results in higher levulinic acid yields (higher levulinic acid recovery) as compared to washing with normal water. Washing with aqueous phase results in a less compressible filter cake. Washing first with aqueous phase and subsequently with condensate results in even higher levulinic acid yields. The process is suitable for isolating levulinic acid and formic acid from compositions made by acid hydrolysis of a lignocellulosic biomass, and also from compositions made by acid hydrolysis of sugars such as glucose and fructose.

Abstract: The invention provides a process for the production of a biomass hydrolysate suitable for the production of levulinic acid and formic acid, a biomass hydrolysate obtainable by said process, a process for the production of levulinic acid and formic acid from said biomass, and levulinic acid and formic acid obtainable by said process. The hydrolysis process includes a single hydrolysis step wherein a slurried biomass is subjected to a temperature of between 120 and 200° C., preferably between 160 and 190° C., for a time period of between 2 and 8 hours, preferably between 20 and 140 minutes at a mineral acid concentration of between 1-15 wt %. The process can be carried out starting from lignocellulosic biomass, and also from glucose and fructose.