IP Library Granted Patent US 8,163,517
Granted Patent B2
US 8,163,517 · App. 12/440,524 · Granted Apr 24, 2012

Organic material production system using biomass material and method

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Quick Facts
Patent No.
US 8,163,517
App. No.
12/440,524
Granted
Apr 24, 2012
Kind
B2
Abstract

An organic material production system using biomass material includes: a hydrothermal decomposition apparatus ( 13 ) that causes the biomass material ( 11 ) and hot compressed water ( 12 ) to countercurrently contact with each other and undergo hydrothermal decomposition, and that transfers a lignin component and a hemicellulose component into the hot compressed water, so as to separate the lignin component and the hemicellulose component from a biomass solid residue; a cellulose enzymatic saccharification device ( 17 ) that treats, with an enzyme, cellulose in the biomass solid residue, so as to enzymatically saccharify the cellulose to a first sugar solution containing hexose; an alcohol fermenter ( 18 ) that produces alcohols by fermentation using the obtained first sugar solution; a sulfuric acid decomposition device ( 33 ) that decomposes, with sulfuric acid, the hemicellulose component in hot water ( 30 ) discharged from the hydrothermal decomposition apparatus, which contains the eluted lignin component and the eluted hemicellulose component, so as to decompose the hemicellulose component to a second sugar solution containing pentose; and a second alcohol fermenter ( 34 ) that produces, using the second sugar solution containing pentose, alcohols by fermentation.

Claims (28)

1. An organic material production system using biomass material, the organic material production system comprising:

a hydrothermal decomposition apparatus that causes the biomass material and hot compressed water to countercurrently contact with each other and undergo hydrothermal decomposition, and that transfers a lignin component and a hemicellulose component into the hot compressed water, so as to separate the lignin component and the hemicellulose component from a biomass solid residue;

an enzymatic saccharification device that treats, with an enzyme, cellulose in the biomass solid residue discharged from the hydrothermal decomposition apparatus, so as to enzymatically saccharify the cellulose to a first sugar solution containing hexose;

a first fermenter that produces, using the first sugar solution obtained by the first enzymatic saccharification device, any one of alcohols, substitutes for petroleum, or amino acids by fermentation;

a sulfuric acid decomposition device that decomposes, with sulfuric acid, the hemicellulose component in hot water discharged from the hydrothermal decomposition apparatus, so as to decompose the hemicellulose component to a second sugar solution containing pentose; and

a second fermenter that produces, using the second sugar solution obtained by the sulfuric acid decomposition device, any one of alcohols, substitutes for petroleum, or amino acids by fermentation,

wherein the hydrothermal decomposition device has a reaction temperature ranging from 180° C. to 240° C. and has a condition of hot compressed water, and

wherein the sulfuric acid decomposition device has a decomposition temperature ranging from 100° C. to 140° C.

2. A method for organic material production using biomass material, the method comprising:

a hydrothermal decomposition process that causes the biomass material and hot compressed water to countercurrently contact with each other and undergo hydrothermal decomposition;

an enzymatic saccharification process that treats, with an enzyme, cellulose in the biomass solid residue discharged from the hydrothermal decomposition process, so as to enzymatically saccharify the cellulose to a first sugar solution containing hexose;

a first fermentation process that produces, using the first sugar solution obtained by the first enzymatic saccharification process, any one of alcohols, substitutes for petroleum, or amino acids by fermentation;

a sulfuric acid decomposition process that decomposes, with sulfuric acid, the hemicellulose component in hot water discharged from the hydrothermal decomposition process, so as to decompose the hemicellulose component to a second sugar solution containing pentose; and

a second fermentation process that produces, using the second sugar solution obtained by the sulfuric acid decomposition device, any one of alcohols, substitutes for petroleum, or amino acids by fermentation,

wherein a reaction temperature of the hydrothermal decomposition ranges from 180° C. to 240° C., and

wherein the sulfuric acid decomposition process has a decomposition temperature ranging from 100° C. to 140° C.

3. An organic material production system using biomass material, the organic material production system comprising:

a hydrothermal decomposition apparatus that causes the biomass material and hot compressed water to countercurrently contact with each other and undergo hydrothermal decomposition, and that transfers a lignin component and a hemicellulose component into the hot compressed water, so as to separate the lignin component and the hemicellulose component from a biomass solid residue;

an enzymatic saccharification device that treats, with an enzyme, cellulose in the biomass solid residue discharged from the hydrothermal decomposition apparatus, so as to enzymatically saccharify the cellulose to a first sugar solution containing hexose; and

a sulfuric acid decomposition device that decomposes, with sulfuric acid, the hemicellulose component in hot water discharged from the hydrothermal decomposition apparatus, so as to decompose the hemicellulose component to a second sugar solution containing pentose;

a second fermenter that produces, using the second sugar solution obtained by the sulfuric acid decomposition device, any one of alcohols, substitutes for petroleum, or amino acids by fermentation,

wherein the hydrothermal decomposition device has a reaction temperature ranging from 180° C. to 240° C. and has a condition of hot compressed water, and

wherein the sulfuric acid decomposition device has a decomposition temperature ranging from 100° C. to 140° C.

4. A method for organic material production using biomass material, the method comprising:

a hydrothermal decomposition process that causes the biomass material and hot compressed water to countercurrently contact with each other and undergo hydrothermal decomposition; an enzymatic saccharification process that treats, with an enzyme, cellulose in the biomass solid residue discharged from the hydrothermal decomposition process, so as to enzymatically saccharify the cellulose to a first sugar solution containing hexose; and

a sulfuric acid decomposition process that decomposes, with sulfuric acid, the hemicellulose component in hot water discharged from the hydrothermal decomposition process, so as to decompose the hemicellulose component to a second sugar solution containing pentose,

wherein a reaction temperature of the hydrothermal decomposition ranges from 180° C. to 240° C., and

wherein the sulfuric acid decomposition process has a decomposition temperature ranging from 100° C. to 140° C.

Assignments (4)
CHANGE OF NAME Recorded Jan 21, 2021
From: MITSUBISHI HITACHI POWER SYSTEMS ENVIRONMENTAL SOLUTIONS, LTD.
To: MITSUBISHI POWER ENVIRONMENTAL SOLUTIONS, LTD.
Reel/Frame 055055/0721 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 21, 2016
From: MITSUBISHI HEAVY INDUSTRIES MECHATRONICS SYSTEMS, LTD.
To: MITSUBISHI HITACHI POWER SYSTEMS ENVIRONMENTAL SOLUTIONS,LTD.
Reel/Frame 040093/0420 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 20, 2012
From: MITSUBISHI HEAVY INDUSTRIES, LTD.
To: MITSUBISHI HEAVY INDUSTRIES MECHATRONICS SYSTEMS, LTD.
Reel/Frame 028596/0878 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 20, 2009
From: GENTA, MINORU; UEHARA, RYOSUKE; TERAKURA, SEIICHI; FUJITA, KINYA
To: MITSUBISHI HEAVY INDUSTRIES, LTD.
Reel/Frame 022428/0766 →