Integrated process for the sustainable and autonomous co2-emission-free production of hydrogen and related system
US-2024200017-A1 · Jun 20, 2024 · US
US9587217B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9587217-B2 |
| Application number | US-201213982420-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 23, 2012 |
| Priority date | Mar 24, 2011 |
| Publication date | Mar 7, 2017 |
| Grant date | Mar 7, 2017 |
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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.
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.
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Separation or concentration of fermentation products (bioreactors combined with means for distillation or extraction of liquid fuel C12M43/02) · CPC title
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for producing fuels or solvents (C12M21/04 takes precedence; liquid carbonaceous fuels C10L1/00, solid fuels C10L5/00) · CPC title
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