Method for processing lignocellulose containing material
First Claim
1. A method for processing biomass derived from plants or animals to make available saccharides and proteins therein for further processing, comprising the steps of:
- a. pre-treating said biomass material containing lignocellulose with an aqueous solution of acid or base to hydrolyze the saccharides from the lignocellulose or the proteins from the biomass material; and
b. subsequently passaging super heated “
SHS”
steam at an elevated pressure through a pressure chamber containing said pre-treated biomass material to further increase the separation of the saccharides from the lignocellulose or the proteins from the biomass material;
wherein the water activity “
Aw”
of the super heated steam is controlled by means of temperature and pressure of the super heated steam to be less than 1 and is defined by the formula
Aw=PSHS/Psaturated steam at TSHS with P=absolute pressure,and wherein the super heated steam is applied for at least 1 minute and less than 30 minutes.
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Accused Products
Abstract
The invention is related to a method for processing biomass derived from plants or animals, comprising the steps of:
- a. pre treating said material with an aqueous solution of acid or base;
- b. subsequently passaging saturated or super heated steam through said material,
wherein the water activity of the process is controlled by means of temperature and pressure of the super heated steam to be less than 1, preferably less than 0.8, more preferably in the range of 0.4-0.8.
With such a process it is possible to disintegrate or make more accessible for subsequent treatments the lignocellulose from lignocellulose containing materials, like wood or other plant material, chitin from exoskeletons from Crustacea like crabs and shrimps, and proteins such as keratin from pig hair or chicken feather, for further derivation, like acylation, oxidation, etherification, carboxymethylation or esterification, or further enzymatic hydrolysis, and/or for production of chemicals, e.g. as sugars from carbohydrates for fermentation processes such as the production of (bio-) ethanolor as keratine hydrolysates for applications in paper or cosmetics.
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Citations
20 Claims
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1. A method for processing biomass derived from plants or animals to make available saccharides and proteins therein for further processing, comprising the steps of:
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a. pre-treating said biomass material containing lignocellulose with an aqueous solution of acid or base to hydrolyze the saccharides from the lignocellulose or the proteins from the biomass material; and b. subsequently passaging super heated “
SHS”
steam at an elevated pressure through a pressure chamber containing said pre-treated biomass material to further increase the separation of the saccharides from the lignocellulose or the proteins from the biomass material;wherein the water activity “
Aw”
of the super heated steam is controlled by means of temperature and pressure of the super heated steam to be less than 1 and is defined by the formula
Aw=PSHS/Psaturated steam at TSHS with P=absolute pressure,and wherein the super heated steam is applied for at least 1 minute and less than 30 minutes. - View Dependent Claims (2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 16, 19)
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15. A method for processing biomass derived from plants or animals to make available saccharides and proteins therein for further processing, comprising the steps of:
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a. pre-treating said biomass material containing lignocellulose with an aqueous solution of acid or base to hydrolyze the saccharides from the lignocellulose or the proteins from the biomass material; and b. subsequently passaging super heated “
SHS”
steam at an elevated pressure through a pressure chamber containing said pre-treated biomass material to further increase the separation of the saccharides or the proteins from the biomass material;wherein the water activity “
Aw”
of the super heated steam is controlled by means of temperature and pressure of the super heated steam to be less than 1 and is defined by the formula Aw=PSHS/Psaturated steam at TSHS with P=absolute pressure, and the temperature of the super heated steam is between 150 and 220°
C., and wherein the super heated steam is applied for at least 1 minute and less than 30 minutes.- View Dependent Claims (17, 18, 20)
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Specification