Process for the production of an enzymatic cocktail using solid residues from a process for the biochemical coversion of lignocellulosic materials

• US 9,885,027 B2
• Filed: 11/27/2012
• Issued: 02/06/2018
• Est. Priority Date: 12/14/2011
• Status: Active Grant

• Current Assignee: IFP Energies Nouvelles
• Original Assignee: IFP Energies Nouvelles
• Inventors: Ben Chaabane, Fadhel, Louret, Sylvain
• Primary Examiner(s): Fan, Lynn Y
• Application Number:
  US14/365,274
• Publication Number:
  US 20140349373A1
• Time in Patent Office: 1,897 Days
• CPC Class Codes: C12N 1/16 Yeasts; Culture media therefor
• CPC Class Codes: C12N 9/2437 Cellulases (3.2.1.4; 3.2.1.74; 3.2.1.91; 3.2.1.150)
• CPC Class Codes: C12N 9/2477 Hemicellulases not provided in a preceding group
• CPC Class Codes: C12P 21/00 Preparation of peptides or proteins single cell protein C12N1/00
• CPC Class Codes: C12P 2203/00 Fermentation products obtained from optionally pretreated or hydrolyzed cellulosic or lignocellulosic material as the carbon source ethanol C12P7/10
• CPC Class Codes: C12P 7/10 substrate containing cellulosic material
• CPC Class Codes: C12Y 302/01004 Cellulase (3.2.1.4), i.e. endo-1,4-beta-glucanase
• CPC Class Codes: C12Y 302/01074 Glucan 1,4-beta-glucosidase (3.2.1.74)
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel

Abstract

The present invention concerns a process for the production of an enzymatic cocktail by submerged culture with a cellulolytic microorganism, comprising two phases:

• • a phase a) for growth of said microorganism in the presence of at least one carbonaceous growth substrate in a closed reactor, said growth phase being carried out with a concentration of carbonaceous growth substrate in the range 10 to 90 g/L;
  • a phase b) for the production of the enzymatic cocktail, in which at least one carbonaceous inducer substrate is supplied, said carbonaceous inducer substrate being at least one solid residue obtained from the step for enzymatic hydrolysis of lignocellulosic materials which have undergone a pre-treatment step, said production phase being carried out with a concentration of carbonaceous production substrate in the range 150 to 400 g/L.

Claims

1. A process for the production of an enzymatic cocktail with a cellulolytic microorganism, comprising two phases:

a phase a) comprising growing said microorganism in the presence of at least one carbonaceous growth substrate in a closed reactor, said phase a) being carried out with a concentration of carbonaceous growth substrate in the range of 10 to 90 g/L; and

a phase b) comprising producing the enzymatic cocktail, in which at least one carbonaceous inducer substrate is supplied to the reactor, said carbonaceous inducer substrate being at least one solid residue obtained by enzymatic partial hydrolysis of lignocellulosic materials which have undergone a pre-treatment step, said solid residue having a liquid portion and a solid portion wherein the solid portion constitutes 10% to 40% by weight of the solid residue and said solid residue having no solid residue obtained from ethanolic fermentation of enzymatic hydrolysates from the enzymatic partial hydrolysis of lignocellulosic materials which have undergone a pre-treatment step, said phase b) being carried out with a concentration of carbonaceous inducer substrate in the range of 150 to 400 g/L, wherein the partial hydrolysis is conducted with an initial enzymatic cocktail, wherein, in the partial hydrolysis, only 20% to 70% by weight of the lignocellulosic materials subject to the enzymatic partial hydrolysis are hydrolysed and wherein the partial hydrolysis is conducted with;

a dry matter content of more than 20% by weight; and

/or

with less than 10 mg of the initial enzymatic cocktail per gram of cellulose in the lignocellulosic materials which have undergone a pre-treatment step.

2. The process according to claim 1, in which the portion of lignin in the solid portion of said solid residue is 45% to 80% by weight.

3. The process according to claim 1, in which said solid residue is separated from the effluent of the enzymatic partial hydrolysis.

4. The process according to claim 1, in which said carbonaceous inducer substrate is used as a mixture with at least one other carbonaceous substrate selected from the group consisting of inducer and non-inducer sugars.

5. The process according to claim 4, in which said other carbonaceous substrate is selected from the group consisting of lactose, glucose, cellulosic hydrolysate, hemicellulosic hydrolysate, cellobiose and xylose, used alone or as a mixture.

6. The process according to claim 1, in which the carbonaceous inducer substrate contains at least 5% by weight of cellulose.

7. The process according to claim 1, in which the specific flow rate at which the carbonaceous inducer substrate used in said phase b) is supplied is in the range of 35 to 65 mg of carbonaceous inducer substrate per gram of microorganism per hour.

8. The process according to claim 1, in which said carbonaceous inducer substrate is separated after the pre-treatment of the lignocellulosic materials.

9. The process according to claim 1, in which said partial hydrolysis is initiated with an amount of initial enzymatic cocktail in the range of from 1 mg to less than 10 mg per gram of cellulose in the lignocellulosic materials which have undergone a pre-treatment step.

10. The process according to claim 9, in which said partial hydrolysis is carried out with an amount of dry matter in the range of from more than 20% to 40% by weight.

11. The process according to claim 1, in which the cellulolytic microorganism is selected from the group consisting of strains of fungi belonging to the genuses Trichoderma, Aspergillus, Penicillium and Schizophyllum.

12. The process according to claim 11, in which the cellulolytic microorganism belongs to the species Trichoderma reesei.

13. The process according to claim 1, wherein the pre-treatment step which the lignocellulosic materials have undergone is an acid pre-treatment step.

14. The process according to claim 1, wherein the pre-treatment step which the lignocellulosic materials have undergone is a steam explosion step with prior impregnation of said materials with an aqueous sulphuric acid solution.