# US 11,306,113 B2 · Process for the production of cellulose, lignocellulosic sugars, lignosulfonate, and ethanol

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- Number: US 11,306,113 B2
- Document ID: US11306113B2
- Status: Granted
- Kind: B2
- Application number: 16/875,241
- Filed: 2020-05-15
- Published: 2021-05-13
- Granted: 2022-04-19
- Earliest claimed: 2019-11-13
- Assignees: American Process International LLC
- Applicants: American Process International LLC
- Inventors: Mikhail Iakovlev; Theodora Retsina; Adriaan van Heiningen; Myrto Papaioannou; Eleni Natsi
- Web page: https://patentgrep.com/patent/US11306113B2

## CPC

- C07G 1/00: Low-molecular-weight derivatives of lignin (high-molecular-weight derivatives of lignin {C08H6/00})
- C08B 1/003: {Preparation of cellulose solutions, i.e. dopes, with different possible solvents, e.g. ionic liquids (solutions used in the manufacture of monocomponent artificial filaments or cellulose or derivatives thereof D01F2/02)}
- C08H 6/00: {Macromolecular compounds derived from lignin, e.g. tannins, humic acids}
- C08H 8/00: Macromolecular compounds derived from lignocellulosic materials {(pretreatment thereof B27N)}
- C08L 1/02: Cellulose; Modified cellulose
- C08L 97/005: {Lignin}
- C08L 97/02: Lignocellulosic material, e.g. wood, straw or bagasse {(manufacture of articles made from lignocellulosic material by dry processes B27N)}
- C12P 7/10: substrate containing cellulosic material
- C12P 19/02: Monosaccharides (2-ketogulonic acid C12P7/60)
- C12P 19/04: Polysaccharides, i.e. compounds containing more than five saccharide radicals attached to each other by glycosidic bonds
- C12P 19/14: produced by the action of a carbohydrase {(EC 3.2.x)}, e.g. by alpha-amylase {, e.g. by cellulase, hemicellulase}
- C13K 1/02: obtained by saccharification of cellulosic materials (manufacture of fodder A23K10/32)
- D21C 1/02: with water or steam
- D21C 3/06: sulfur dioxide; sulfurous acid; bisulfites {sulfites}
- D21C 5/005: {Treatment of cellulose-containing material with microorganisms or enzymes}
- D21C 9/00: After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters {; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere (polysaccharides, derivatives thereof C08B; paper-making D21B - D21H)}
- D21C 11/0007: {Recovery of by-products, i.e. compounds other than those necessary for pulping, for multiple uses or not otherwise provided for (volatile compounds obtained by decomposition of spent liquors in order to regenerate them D21C11/125; compounds obtained by fractionating the liquors in order to regenerate them D21C11/0042)}
- C12P 2201/00: Pretreatment of cellulosic or lignocellulosic material for subsequent enzymatic treatment or hydrolysis
- Y02E 50/10: Biofuels, e.g. bio-diesel
- C07G: COMPOUNDS OF UNKNOWN CONSTITUTION (sulfonated fats, oils or waxes of undetermined constitution C07C309/62)
- C08B: POLYSACCHARIDES; DERIVATIVES THEREOF (polysaccharides containing less than six saccharide radicals attached to each other by glycosidic linkages C07H; fermentation or enzyme-using processes C12P19/00; sugar industry C13; production of cellulose D21)
- C08H: DERIVATIVES OF NATURAL MACROMOLECULAR COMPOUNDS (polysaccharides C08B; natural rubber C08C; natural resins or their derivatives C09F; bituminous materials C10)
- C08L: COMPOSITIONS OF MACROMOLECULAR COMPOUNDS (compositions based on polymerisable monomers C08F, C08G; artificial filaments or fibres D01F; textile treating compositions D06)
- C12P: FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE {(brewing of beer C12C; producing vinegar C12J; producing specific peptides or proteins C07K; producing enzymes C12N9/00; DNA or RNA concerning genetic engineering, vectors, e.g. plasmids, or their isolation, preparation or purification C12N15/00; measuring or testing processes involving enzymes or microorganisms C12Q; measuring or testing processes involving nucleic acid amplification reactions C12Q1/6844; fermentation processes to form a food composition, A21 or A23; compounds in general, see the relevant compound class, e.g. C01, C07)}
- C13K: SACCHARIDES OBTAINED FROM NATURAL SOURCES OR BY HYDROLYSIS OF NATURALLY OCCURRING DISACCHARIDES, OLIGOSACCHARIDES OR POLYSACCHARIDES (chemically synthesised sugars or sugar derivatives C07H; polysaccharides, e.g. starch, derivatives thereof C08B; malt C12C; fermentation or enzyme-using processes for preparing compounds containing saccharide radicals C12P19/00; production of sucrose C13B)
- D21C: PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- Y02E: REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION

## Abstract

A process for the production of cellulose, lignocellulosic sugars, lignosulfonate, and ethanol from lignocellulosic biomass. The process comprises steaming, pretreatment, chemical recovery, saccharification, and optionally fermentation. The pretreatment conditions use only sulfur dioxide and water, simultaneously resulting in high glucan conversion to glucose at low enzyme charges, high recovery of hemicellulose-derived monomeric sugars, high lignosulfonate yield, and the absence of lignin precipitates. High-yield production of ethanol through fermentation can be obtained using this process.

## Claims

### Claim 1

A process for producing cellulose, lignocellulosic sugars, lignosulfonate, and ethanol, from lignocellulosic biomass comprising:
(a) contacting lignocellulosic biomass in a first container with steam, wherein the lignocellulosic biomass absorbs water from the steam, thereby removing air from the lignocellulosic biomass;
(b) contacting the steamed lignocellulosic biomass in a second container with a pretreatment composition comprising sulfur dioxide and water at a temperature between 125° C. and 133° C. under pressure for 20-90 minutes to generate pretreated material;
wherein the pretreatment composition comprises about 40 wt. % sulfur dioxide and about 60 wt. % water based on the combined weight of sulfur dioxide and water (including water from the steamed lignocellulosic biomass), and the ratio of pretreatment composition to lignocellulosic biomass dry weight is from about 1 to 8 kg/kg (including water from the steamed lignocellulosic biomass in the mass of the pretreatment composition);
thereby releasing and/or dissolving lignin and hemicellulose from the lignocellulosic biomass into the pretreatment composition and leaving a solid fraction comprising cellulose, wherein the lignin content in the solid fraction comprising cellulose is less than 14 wt. %, the cellulose yield is about 87 wt. % to about 97 wt. % based on the amount of cellulose in the lignocellulosic biomass, and a total saccharide recovery from the lignocellulosic biomass after steps (a) and (b) is greater than 91%;
wherein 75-100% of the lignin from the lignocellulosic biomass is sulfonated to produce lignosulfonic acid (LS), and at least about 85% of the sugar moieties of the released hemicellulose from the lignocellulosic biomass are hydrolyzed to monosaccharide form; and
wherein the pretreated material comprises 0.1 wt. % furfural or less; 0.2 wt. % levulinic acid or less, and less than 0.1 wt. % hydroxymethylfurfural, with respect to dry weight of the pretreated material;
(c) releasing pressure from the pretreated material, and recovering sulfur dioxide from gas released from the pretreated material as a result of releasing pressure;
(d) removing dissolved material from the cellulose by washing with water or by applying pressure to the cellulose to drain off the dissolved material, to provide washed cellulose or pressed cellulose, referred to as a washed cellulose stream, wherein the dissolved material comprises lignosulfonic acid (LS), lignin, hemicellulose oligomers, and monosaccharides;
(e) adjusting the pH of the washed cellulose stream from step (d) and contacting it with a cellulase, a glucosidase, a hemicellulase, or a combination thereof, to produce glucose and to release small amounts of insoluble lignin and hemicellulose-derived monosaccharides; and
(f) neutralizing the glucose and the dissolved material to an appropriate pH level and subjecting the glucose, the dissolved material, or a combination thereof to fermentation to produce ethanol.

### Claim 2 (depends on 1)

The process of claim 1 wherein recovering sulfur dioxide comprises:
(i) releasing gas comprising sulfur dioxide and water vapor from the pretreated material at elevated temperature and optionally lower pressure;
(ii) condensing the gas to provide a gas comprising sulfur dioxide and a liquid comprising water;
(iii) liquefying the gas comprising sulfur dioxide by pressure change and/or temperature reduction to provide liquid sulfur dioxide; and
(iv) introducing the liquid sulfur dioxide to a container for contacting steamed lignocellulosic biomass with a pretreatment composition.

### Claim 3 (depends on 2)

The process of claim 2 wherein the gas comprising sulfur dioxide is purified by removing water vapor and organic volatiles.

### Claim 4 (depends on 2)

The process of claim 2 wherein the liquid sulfur dioxide is stored as liquid sulfur dioxide in a separate container before being reused in the pretreatment composition in step (b) of the process.

### Claim 5 (depends on 1)

The process of claim 1 wherein the pretreated material after step (c) and/or the dissolved material after step (d) is retained at elevated temperature, to facilitate sulfur dioxide recovery.

### Claim 6 (depends on 1)

The process of claim 1 where the step (b) pretreatment is performed in a continuous mode.

### Claim 7 (depends on 1)

The process of claim 1 where the step (b) pretreatment is performed in a batch mode.

### Claim 8 (depends on 1)

The process of claim 1 where the enzymatic hydrolysis of step (e) is performed in a continuous mode.

### Claim 9 (depends on 1)

The process of claim 1 where the enzymatic hydrolysis of step (e) is performed in a batch mode.

### Claim 10 (depends on 1)

The process of claim 1 wherein one or more of water, phosphoric acid, hydrochloric acid, sulfuric acid, nitric acid, acetic acid, formic acid, oxalic acid, and process condensates are added to step (c), step (d), or both.

### Claim 11 (depends on 1)

The process of claim 1 wherein washed cellulose stream, the dissolved material, the glucose, or a combination thereof, are subjected to pH adjustment to a pH of 7-11, before enzyme hydrolysis step (e), before fermentation step (f), or before both steps (e) and (f), followed by pH adjustment to a pH of less than 7.

### Claim 12 (depends on 1)

The process of claim 1 wherein residual sulfur dioxide is removed from the washed cellulose stream, from the dissolved material, from the glucose, or from a combination thereof, before enzyme hydrolysis step (e), before fermentation step (f), or before both steps (e) and (f), by adding one or more aqueous solutions comprising formaldehyde, acetaldehyde, or hydrogen peroxide.

### Claim 13 (depends on 1)

The process of claim 1 further comprising bleaching the washed pulp to produce cellulose that can be converted to nanocellulose and/or dissolving pulp, including but not limited to viscose, cellulose ethers, and cellulose esters.

### Claim 14 (depends on 1)

The process of claim 1 wherein the process produces at least about 257 kg of ethanol and at least about 250 kg lignosulfonate per bone dry tonne of wood sawdust.

### Claim 15

A process for producing lignocellulosic sugars, lignosulfonate, and ethanol, from lignocellulosic biomass comprising:
(a) contacting lignocellulosic biomass in a first container with steam, wherein the lignocellulosic biomass absorbs water from the steam, thereby removing air from the lignocellulosic biomass;
(b) contacting the steamed lignocellulosic biomass in a second container with a pretreatment composition comprising sulfur dioxide and water at a temperature between 125° C. and 133° C. under pressure for 20-90 minutes to generate pretreated material;
wherein the pretreatment composition comprises about 40 wt. % sulfur dioxide and about 60 wt. % water based on the combined weight of sulfur dioxide and water (including water from the steamed lignocellulosic biomass), and the ratio of pretreatment composition to lignocellulosic biomass dry weight is from about 1 to 8 kg/kg (including water from the steamed lignocellulosic biomass in the mass of the pretreatment composition);
thereby releasing and/or dissolving lignin and hemicellulose from the lignocellulosic biomass into the pretreatment composition and leaving a solid fraction comprising cellulose, wherein the lignin content in the solid fraction comprising cellulose is less than 14 wt. %, the cellulose yield is about 87 wt. % to about 97 wt. % based on the amount of cellulose in the lignocellulosic biomass, and a total saccharide recovery from the lignocellulosic biomass after steps (a) and (b) is greater than 91%;
wherein 75-100% of the lignin from the lignocellulosic biomass is sulfonated to produce lignosulfonic acid (LS), and at least about 85% of the sugar moieties of the released hemicellulose from the lignocellulosic biomass are hydrolyzed to monosaccharide form; and
wherein the pretreated material comprises 0.1 wt. % furfural or less; 0.2 wt. % levulinic acid or less, and less than 0.1 wt. % hydroxymethylfurfural, with respect to dry weight of the pretreated material;
(c) releasing pressure from the pretreated material and recovering sulfur dioxide from gas released from the pretreated material as a result of releasing pressure, producing a first mixture;
(d) neutralizing the first mixture to an appropriate pH level for enzymatic hydrolysis;
(e) contacting the neutralized first mixture with a cellulase, a glucosidase, a hemicellulase, or a combination thereof, to provide a second mixture comprising glucose derived from cellulose and monosaccharides derived from hemicellulose as well as lignosulfonate (salt of lignosulfonic acid), lignin, and oligosaccharides; and
(f) adjusting pH of the second mixture and subjecting the second mixture to fermentation to produce ethanol.

### Claim 16 (depends on 15)

The process of claim 15 wherein recovering sulfur dioxide comprises:
(i) releasing gas comprising sulfur dioxide and water vapor from the pretreated material at elevated temperature and optionally lower pressure;
(ii) condensing the gas to provide a gas comprising sulfur dioxide and a liquid comprising water;
(iii) liquefying the gas comprising sulfur dioxide by pressure change and/or temperature reduction to provide liquid sulfur dioxide; and
(iv) introducing the liquid sulfur dioxide to a container for contacting steamed lignocellulosic biomass with a pretreatment composition.

### Claim 17 (depends on 16)

The process of claim 16 wherein the gas comprising sulfur dioxide is purified by removing traces of water vapor and organic volatiles.

### Claim 18 (depends on 16)

The process of claim 16 wherein the liquid sulfur dioxide is stored as liquid sulfur dioxide in a separate container before being reused in the pretreatment composition in step (b) of the process.

### Claim 19 (depends on 15)

The process of claim 15 wherein the pretreated material is retained at elevated temperature after step (c), to facilitate sulfur dioxide recovery.

### Claim 20 (depends on 15)

The process of claim 15 wherein one or more of water, phosphoric acid, hydrochloric acid, sulfuric acid, nitric acid, acetic acid, formic acid, oxalic acid, and process condensates are added to step (c).

### Claim 21 (depends on 15)

The process of claim 15 wherein the first mixture after step (c), the second mixture after step (e), or both, are subjected to pH adjustment to a pH of 7-11, before enzyme hydrolysis step (e), before fermentation step (f), or before both steps (e) and (f), followed by pH adjustment to a pH of less than 7.

### Claim 22 (depends on 15)

The process of claim 15 wherein residual sulfur dioxide is removed from the first mixture after step (c), from the second mixture after step (e), or from both, by adding one or more aqueous solutions comprising formaldehyde, acetaldehyde, or hydrogen peroxide.

### Claim 23 (depends on 15)

The process of claim 15 wherein the process produces at least about 257 kg of ethanol and at least about 250 kg lignosulfonate per bone dry tonne of wood sawdust.

### Claim 24

A process for producing cellulose, lignocellulosic sugars, lignosulfonate, and ethanol, from wood sawdust comprising:
(a) contacting wood sawdust in a first container with steam, wherein the wood sawdust absorbs water from the steam, thereby removing air from the wood sawdust;
(b) contacting the steamed wood sawdust in a second container with a pretreatment composition comprising sulfur dioxide and water at a temperature of about 130° C. under pressure for about 60-90 minutes to generate pretreated material;
wherein the pretreatment composition comprises about 40 wt. % sulfur dioxide and about 60 wt. % water based on the combined weight of sulfur dioxide and water (including water from the steamed wood sawdust), and the ratio of pretreatment composition to wood sawdust dry weight is from about 2 kg/kg to 8 kg/kg (including water from the steamed wood sawdust in the mass of the pretreatment composition);
thereby releasing and/or dissolving lignin and hemicellulose from the wood sawdust into the pretreatment composition and leaving a solid fraction comprising cellulose, wherein the lignin content in the solid fraction comprising cellulose is less than 14 wt. %, the cellulose yield is about 87 wt. % to about 97 wt. % based on the amount of cellulose in the wood sawdust, and a total saccharide recovery from the wood sawdust after steps (a) and (b) is greater than 91%;
wherein at least about 85% of the lignin from the wood sawdust is sulfonated to produce lignosulfonic acid (LS), and at least about 85% of the sugar moieties of the released hemicellulose from the wood sawdust are hydrolyzed to monosaccharide form; and
wherein the pretreated material comprises less than 0.1 wt. % furfural; less than 0.1 wt. % hydroxymethylfurfural, and about 0.1 wt. % levulinic acid or less, with respect to dry weight of the pretreated material;
(c) releasing pressure from the pretreated material, and recovering sulfur dioxide from gas released from the pretreated material as a result of releasing pressure;
(d) removing dissolved material from the cellulose by washing with water or by applying pressure to the cellulose to drain off the dissolved material, to provide washed cellulose or pressed cellulose, referred to as a washed cellulose stream, wherein the dissolved material comprises lignosulfonic acid (LS), lignin, hemicellulose oligomers, and monosaccharides;
(e) adjusting the pH of the washed cellulose stream from step (d) and contacting it with a cellulase, a glucosidase, a hemicellulase, or a combination thereof, to produce glucose and to release small amounts of insoluble lignin and hemicellulose-derived monosaccharides; and
(f) neutralizing the glucose and the dissolved material to an appropriate pH level and subjecting the glucose, the dissolved material, or a combination thereof to fermentation to produce ethanol, wherein when the glucose and dissolved material are subjected to fermentation, at least about 275 kg ethanol per bone dry tonne of wood sawdust is produced.

### Claim 25

A process for producing ethanol and lignosulfonate from wood sawdust comprising:
(a) contacting wood sawdust in a first container with steam, wherein the wood sawdust absorbs water from the steam, thereby removing air from the wood sawdust;
(b) contacting the steamed wood sawdust in a second container with a pretreatment composition comprising sulfur dioxide and water at a temperature of about 130° C. under pressure for about 60-90 minutes to generate pretreated material;
wherein the pretreatment composition comprises about 40 wt. % sulfur dioxide and 60 wt. % water based on the combined weight of sulfur dioxide and water (including water from the steamed wood sawdust), and the ratio of pretreatment composition to wood sawdust dry weight is from about 2 kg/kg to 8 kg/kg (including water from the steamed wood sawdust in the mass of the pretreatment composition);
thereby releasing and/or dissolving lignin and hemicellulose from the wood sawdust into the pretreatment composition and leaving a solid fraction comprising cellulose, wherein the lignin content in the solid fraction comprising cellulose is less than 14 wt. %, the cellulose yield is about 87 wt. % to about 97 wt. % based on the amount of cellulose in the wood sawdust, and a total saccharide recovery from the wood sawdust after steps (a) and (b) is greater than 91%; and
wherein the pretreated material comprises 0.1 wt. % furfural or less; 0.2 wt. % levulinic acid or less, and less than 0.1 wt. % hydroxymethylfurfural, with respect to dry weight of the pretreated material;
wherein at least 85% of the lignin from the wood sawdust is sulfonated to produce lignosulfonic acid (LS), and at least about 85% of the sugar moieties of the released hemicellulose from the wood sawdust are hydrolyzed to monosaccharide form;
(c) releasing pressure from the pretreated material and recovering sulfur dioxide from gas released from the pretreated material as a result of releasing pressure, producing a first mixture;
(d) neutralizing the first mixture to an appropriate pH level for enzymatic hydrolysis;
(e) contacting the neutralized first mixture with a cellulase, a glucosidase, a hemicellulase, or a combination thereof, to provide a second mixture comprising glucose derived from cellulose and monosaccharides derived from hemicellulose as well as lignosulfonate (salt of lignosulfonic acid), lignin, and oligosaccharides; and
(f) adjusting pH of the second mixture and subjecting the second mixture to fermentation to produce at least about 275 kg of ethanol per bone dry tonne of wood sawdust.