Process for pretreating biomasses in advance of their enzymatic treatment

• US 4,642,287 A
• Filed: 04/05/1984
• Issued: 02/10/1987
• Est. Priority Date: 04/14/1983
• Status: Expired due to Fees

• Current Assignee: Shinnenryoyu Kaihatsugijutsu Kenkyukumiai
• Original Assignee: Shinnenryoyu Kaihatsugijutsu Kenkyukumiai
• Inventors: Kurokawa, Yasuhiro, Matsuoka, Shingo, Akabane, Toshiaki, Inoi, Takeshi
• Primary Examiner(s): Nucker, Christine M.
• Assistant Examiner(s): DeSantis, Patricia L.
• Application Number:
  US06/596,937
• Time in Patent Office: 1,041 Days
• Field of Search: 435/99, 435/105, 127/37, 127/1
• US Class Current: 435/99
• CPC Class Codes: C12P 19/14 produced by the action of a carbohydrase (EC 3.2.x), e.g. by alpha-amylase , e.g. by cellulase, hemicellulase
• CPC Class Codes: C12P 2201/00 Pretreatment of cellulosic or lignocellulosic material for subsequent enzymatic treatment or hydrolysis
• CPC Class Codes: C13K 1/02 obtained by saccharification of cellulosic materials manufacture of fodder A23K10/32
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel

Abstract

An improved process for pretreating biomasses in advance of their enzymatic treatment is provided which process comprises subjecting a biomass together with an aqueous solution of an alkaline compound to kneading and reaction in a biaxial extruder, and which process has advantages that a continuous treatment in a very short time is possible, and the heat quantity required for the pretreatment is greatly reduced.

Claims

1. In the process of pretreating a biomass in advance of cellulose enzymatic treatment that includes contacting the biomass in finely divided form with an aqueous solution of an alkaline compound, the improvement comprising reducing the pretreatment time to one minute or less by introducing the biomass and the alkaline compound into a biaxial extruder and carrying out the pretreatment in said biaxial extruder.

2. A process according to claim 1 wherein said alkaline compound is NaOH or Na₂ S or a mixture of NaOH and Na₂ S.

3. A process according to claim 2 wherein said biomass and said aqueous solution of an alkaline compound are mixed together before being introduced into said biaxial extruder.

4. A process according to claim 3 wherein said biomass is a material obtained by cutting and grinding a biomass and has an average particle diameter of 15 mm or less.

5. A process according to claim 3 wherein the amount of said aqueous solution of an alkaline compound is in the range of 0.6 to 2 times by weight the amount of said biomass, and the alkaline compound is 10 to 24% by weight of said biomass.

6. A process according to claim 3 wherein the temperature of said mixture in said biaxial extruder is in the range of 60°

to 230°

C.

7. A process according to claim 3 wherein said biomass is at least one member selected from the group consisting of bagasse, Siebold'"'"'s beech, silver magnolia, Yezo spruce (Picea jezoensis CARR), white birch, corn rachis and paper.

8. A process according to claim 2 wherein said biomass and said aqueous solution of an alkali compound are separately introduced into said biaxial extruder so that mixing thereof only occurs in the biaxial extruder.

9. A process according to claim 8 wherein said biomass is a material obtained by cutting and grinding a biomass and has an average particle diameter of 30 mm or less.

10. A process according to claim 8 wherein said aqueous solution of an alkaline compound, in an amount of 3 to 15 times by weight the amount of said biomass is injected into said biaxial extruder separately from the introduction of the biomass into the extruder and said alkaline compound is 3-30% by weight of said biomass.

11. A process according to claim 8 wherein the temperature in said biaxial extruder is in the range of 60°

to 230°

C.

12. A process according to claim 8 wherein said biomass is at least one member selected from the group consisting of bagasse, Siebold'"'"'s beech, silver magnolia, Yezo spruce (Picea jezoenis CARR), white birch, corn rachis and papers.