Apparatus for producing saccharide solution that uses biomass as feedstock

US9587217B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-9587217-B2
Application numberUS-201213982420-A
CountryUS
Kind codeB2
Filing dateMar 23, 2012
Priority dateMar 24, 2011
Publication dateMar 7, 2017
Grant dateMar 7, 2017

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

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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.

First claim

Opening claim text (preview).

The invention claimed is: 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.

Assignees

Inventors

Classifications

  • Xylose · CPC title

  • Apparatus specially designed for the use of free, immobilized or carrier-bound enzymes · CPC title

  • Separation or concentration of fermentation products (bioreactors combined with means for distillation or extraction of liquid fuel C12M43/02) · CPC title

  • C12M43/00Primary

    Combinations of bioreactors or fermenters with other apparatus · CPC title

  • for producing fuels or solvents (C12M21/04 takes precedence; liquid carbonaceous fuels C10L1/00, solid fuels C10L5/00) · CPC title

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What does patent US9587217B2 cover?
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 t…
Who is the assignee on this patent?
Nishimura Akira, Yamauchi Takahiro, Ogura Kentaro, and 7 more
What technology area does this patent fall under?
Primary CPC classification C12M43/00. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Mar 07 2017 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).