IP Library Granted Patent US 9,587,217
Granted Patent B2
US 9,587,217 · App. 13/982,420 · Granted Mar 7, 2017

Apparatus for producing saccharide solution that uses biomass as feedstock

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Quick Facts
Patent No.
US 9,587,217
App. No.
13/982,420
Granted
Mar 7, 2017
Kind
B2
Abstract

An apparatus for treating a biomass feedstock at a high temperature, includes a cooling device 90 for cooling a biomass treated liquid at a high temperature; an enzymatic saccharification tank 103 for saccharifying a cooled treated liquid 101 B with an enzyme; a solid-liquid separation apparatus 112 for removing water-slightly soluble substances contained in a saccharide solution 104 taken out from the enzymatic saccharification tank 103 and a foreign substance removing unit 113 provided with a microfiltration (MF) membrane 113 a ; a dilution tank 132 , disposed downstream of the foreign substance removing unit 113 , for diluting the saccharide solution from which the water-slightly soluble substances are removed by adding water thereto; a water separation unit 116 , provided with a reverse osmosis (RO) membrane 116 a , for removing water 114 from the diluted saccharide solution so as to obtain concentrated saccharide solution 115.

Claims (14)

1. An apparatus for producing saccharide solution that uses biomass as a feedstock comprising:

a hydrothermal decomposition apparatus that brings a biomass feedstock including at least cellulose, hemicellulose, and lignin into countercurrent contact with pressurized hot water and performs a high temperature and high pressure treatment in a temperature range of 180° C. to 240° C. so as to produce a biomass treated liquid containing a pressurized hot water soluble component of the biomass feedstock;

a cooling means that is provided downstream of the hydrothermal decomposition apparatus and cools the biomass treated liquid which has been discharged from the hydrothermal decomposition apparatus;

an enzymatic saccharification tank that is provided downstream of the cooling means and saccharifies the cooled treated liquid with an enzyme so as to produce a saccharide solution;

a saccharide solution purification means that is provided downstream of the enzymatic saccharification tank and removes a water-slightly soluble substance from the saccharide solution, the water-slightly soluble substance being a substance that is contained in the pressurized hot water soluble component, and solidified or colloidal due to the cooling;

a dilution tank that is disposed downstream of the saccharide solution purification means and adds water thereto so as to dilute the saccharide solution from which the water-slightly soluble substance has been removed;

a water separation unit that is provided with a reverse osmosis (RO) membrane and removes water from the diluted saccharide solution so as to obtain concentrated saccharide solution;

a first measurement unit that measures both of a turbidity and a light absorbance of the saccharide solution from which the water-slightly soluble substance has been removed, wherein

the saccharide solution purification means includes:

a saccharide solution purification tank that is provided downstream of the enzymatic saccharification tank to receive and retain the saccharide solution taken from the enzymatic saccharification tank;

a first circulation line that connects between a bottom portion of the saccharide solution purification tank and an upper portion of the saccharide solution purification tank to circulate the saccharide solution;

a second circulation line that connects between the bottom portion of the saccharide solution purification tank and the upper portion of the saccharide solution purification tank to circulate the saccharide solution;

a solid-liquid separation apparatus that is interposed in the first circulation line and removes the water-slightly soluble substance contained in the saccharide solution circulating in the first circulation line;

a foreign substance removing unit that is interposed in the second circulation line and has a microfiltration (MF) membrane by which the water-slightly soluble substance circulating in the second circulation line is further removed and through which the saccharide solution from which the remaining water-slightly soluble substance is thus removed is passed.

Assignments (5)
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 Mar 12, 2018
From: TORAY INDUSTRIES, INC.
To: MITSUBISHI HITACHI POWER SYSTEMS ENVIRONMENTAL SOLUTIONS, LTD.
Reel/Frame 045170/0991 →
CORRECTIVE ASSIGNMENT TO CORRECT THE ASSIGNEE NAME PREVIOUSLY RECORDED AT REEL: 039252 FRAME: 0945. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Recorded Sep 30, 2016
From: MITSUBISHI HEAVY INDUSTRIES MECHATRONICS SYSTEMS, LTD.
To: MITSUBISHI HITACHI POWER SYSTEMS ENVIRONMENTAL SOLUTIONS, LTD
Reel/Frame 040192/0054 →
CHANGE OF NAME Recorded Jul 26, 2016
From: MITSUBISHI HEAVY INDUSTRIES MECHATRONICS SYSTEMS, LTD.
To: MITSBISHI HITACHI POWER SYSTEMS ENVIRONMENTAL SOLUTIONS, LTD
Reel/Frame 039252/0945 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 30, 2013
From: NISHIMURA, AKIRA; YAMAUCHI, TAKAHIRO; OGURA, KENTARO; NISHIMOTO, HARUKA; KURIHARA, HIROYUKI; MINAMINO, ATSUSHI; SUZUKI, HIDEO; KONDO, GAKU
To: TORAY INDUSTRIES, INC.; MITSUBISHI HEAVY INDUSTRIES MECHATRONICS SYSTEMS, LTD.
Reel/Frame 030906/0351 →