Production of a fermentation product

• US 8,067,193 B2
• Filed: 01/20/2005
• Issued: 11/29/2011
• Est. Priority Date: 02/04/2004
• Status: Expired due to Fees

• Current Assignee: CIBA Specialty Chemicals Water Treatments Limited (BASF SE)
• Original Assignee: CIBA Specialty Chemicals Water Treatments Limited (BASF SE)
• Inventors: Symes, Kenneth Charles, Mistry, Rajesh, Hughes, Jonathan
• Primary Examiner(s): Ariani; Kade
• Application Number:
  US10/587,583
• Publication Number:
  US 20070172913A1
• Time in Patent Office: 2,504 Days
• Field of Search: None
• US Class Current: 435/41
• CPC Class Codes: C02F 1/001 Processes for the treatment of water whereby the filtration technique is of importance C02F1/44 takes precedence; construction of filters in general B01D24/00 - B01D41/00
• CPC Class Codes: C02F 1/281 using inorganic sorbents
• CPC Class Codes: C02F 1/56 Macromolecular compounds
• CPC Class Codes: C02F 2103/32 from the food or foodstuff industry, e.g. brewery waste waters
• CPC Class Codes: C02F 2103/34 from industrial activities not provided for in groups C02F2103/12 - C02F2103/32
• CPC Class Codes: C02F 2209/09 Viscosity
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel

Abstract

A process of separating suspended solids from a fermentation liquor by subjecting the liquor to a solids-liquid separation stage, wherein the fermentation liquor is produced in a fermentation process for the production of a fermentation product, in which the liquor has been subjected to a temperature of at least 50° C., wherein the solids-liquid separation stage is assisted by a treatment system, characterised in that the treatment system comprises an anionic polymer selected from natural polymers and modified natural polymers having a high anionic charge such that the equivalent weight is below 300, and synthetic polymers formed from at least 50% by weight anionic monomer units.

Claims

1. A process of separating suspended solids from a fermentation liquor comprising the following sequence of steps:

(i) producing the fermentation liquor in a fermentation process for the production of a fermentation product;

(ii) subjecting the fermentation liquor produced in step (i) to a temperature of at least 50°

C. and recovering the fermentation product from said liquor; and

(iii) subjecting the fermentation liquor obtained in step (ii) to a solids-liquid separation stage to separate the suspended solids and remove the suspended solids from the liquor,

wherein the solids-liquid separation stage is assisted by a treatment system, and wherein the treatment system comprises an anionic polymer selected from natural polymers and modified natural polymers having an anionic charge such that the equivalent weight is below 300, and synthetic polymers, the anionic polymer is formed from at least 50% by weight anionic monomer units and said anionic monomer units are selected from the group consisting of (meth)acrylic acids or salts, maleic acid or salts, itaconic acid or salts and fumaric acid or salts.

2. A process according to claim 1 in which said fermentation liquor in step (ii) is subjected to a distillation stage in which the fermentation product is recovered, wherein the liquor is removed from the distillation stage as a stillage stream and then subjected to the solids-liquid separation stage.

3. A process according to claim 1 in which the treatment system comprises an anionic polymer formed from at least 65% by weight anionic monomer units.

4. A process according to claim 1 in which the anionic polymer exhibits an intrinsic viscosity of at least 4 dl/g (measured using a suspended level viscometer in 1M NaCl buffered to pH 7.5 at 25°

C.).

5. A process according to claim 1 in which the treatment system further comprises addition of a cationic polymer that exhibits an intrinsic viscosity below 4 dl/g (measured using a number 1 suspended level viscometer in 1M NaCl buffered to pH 7.0 at 25°

C.).

6. A process according to claim 5 in which the cationic polymer exhibits a charge density of at least 3 meq/g.

7. A process according to claim 5 in which the cationic polymer is selected from the group consisting of polyamines, amine/epihalohydrin addition polymers, polymers of dicyandiamide with formaldehyde, polymers of diallyldimethyl ammonium chloride (DADMAC), cationic starch and cationic inulin, polymers of dialkyl amino alkyl(meth)acrylates (or salts) and dialkyl amino alkyl(meth) acrylamides (or salts).

8. A process according to claim 5 in which the anionic polymer and cationic polymer are added sequentially.

9. A process according to claim 1 in which the dose of anionic polymer is at least 50 grams per tonne (based on dry weight of fermentation liquor).

10. A process according to claim 5 in which the dose of cationic polymer is at least 50 grams per tonne (based on dry weight of fermentation liquor).

11. A process according to claim 1 in which the treatment system further comprises addition of a siliceous material.

12. A process according to claim 11 in which the siliceous material is selected from the group consisting of silica based particles, silica microgels, colloidal silica, silica sols, silica gels, polysilicates, cationic silica, aluminosilicates, polyaluminosilicates, borosilicates, polyborosilicates, zeolites and swellable clays.

13. A process according to claim 11 in which the siliceous material is an anionic microparticulate material.

14. A process according to claim 11 in which the siliceous material is a bentonite type clay.

15. A process according to claim 11 in which the siliceous material is selected from the group consisting of hectorite, smectites, montmorillonites, nontronites, saponite, sauconite, hormites, attapulgites and sepiolites.

16. A process according to claim 1 in which the fermentation liquor is subjected to a mechanical dewatering stage during or subsequent to application of the treatment system.

17. A process according to claim 16 in which the mechanical dewatering step is selected from the group consisting of a centrifuge, a screw press, a filter press, a belt filter press, a horizontal belt filter, and a pressure filter.

18. A process according to claim 1 in which the treated liquor from which suspended solids have been removed are recycled and used as wash water.

19. A process according to claim 1 in which the fermentation liquor comprises lignin and in which the separated solids are dewatered and then subjected to a drying stage to provide a dry solid material and in which the dry solid material is used as a solid fuel.

20. A process according to claim 1 in which said fermentation liquor in step (ii) is derived from crop sugars and in which the separated solids are dewatered and then subjected to a drying stage to provide a dry solid material and in which the dry solid material is used as a solid fuel or as an animal feed.

21. A process according to claim 1 in which the fermentation product is selected from the group consisting of ethanol, glycerol, acetone, n-butanol, butanediol, isopropanol, butyric acid, methane, citric acid, fumaric acid, lactic acid, propionic acid, succinic acid, itaconic acid, acetic acid, acetaldehyde and 3-hydroxypropionic acid, glycolic acid, tartaric acid, and amino acids or salts of any of these acids.