METHOD AND SYSTEM FOR UPGRADING BIOGAS USING PSA

    公开(公告)号:US20250001351A1

    公开(公告)日:2025-01-02

    申请号:US18695788

    申请日:2022-09-21

    Abstract: A method for upgrading biogas wherein biogas is provided in one or more pressurized vessels. A plurality of pressurized feeds are produced in a process comprising decompressing biogas from at least one of the one or more vessels and as the biogas is decompressed providing portions of the biogas at successively lower pressures. The plurality of pressurized feeds, which have different average pressures, are provided to a pressure swing adsorption process wherein an adsorbent bed is pressurized by successively feeding gas from each of the pressurized feeds in the plurality into the adsorbent bed in order of increasing average pressure. Accordingly, compression costs can be reduced.

    Process comprising acid pretreatment and enzymatic hydrolysis

    公开(公告)号:US11008598B2

    公开(公告)日:2021-05-18

    申请号:US15550525

    申请日:2016-03-16

    Abstract: Provided herein is a process for producing a fermentation product from a lignocellulosic feedstock. The process comprises soaking a lignocellulosic feedstock in an aqueous solution to produce a soaked feedstock. The soaked feedstock is at least partially dewatered and the at least partially dewatered feedstock is subjected to pretreating. The pretreatment chemical is sulfur dioxide, sulfurous acid or a combination thereof and can be added to the process at any stage prior to and/or during pretreatment. The pretreated feedstock composition is fed to an enzymatic hydrolysis conducted at a temperature that is higher than 58° C. The cellulose in the pretreated feedstock composition is hydrolyzed with cellulase enzymes in the presence of the dissolved solids to produce glucose. The glucose is fermented to produce the fermentation product.

    LOW TEMPERATURE PRETREATMENT WITH SULFUR DIOXIDE

    公开(公告)号:US20200263209A1

    公开(公告)日:2020-08-20

    申请号:US16761192

    申请日:2018-11-09

    Abstract: A process for producing a fuel from lignocellulosic biomass is disclosed. The process includes obtaining a feedstock comprising lignocellulosic biomass, feeding the feedstock and sulfur dioxide into a pretreatment reactor, wherein a total amount of sulfur dioxide in the pretreatment reactor is greater than 70 wt % based on dry weight lignocellulosic biomass, and heating the feedstock and sulfur dioxide in the pretreatment reactor at one or more temperatures between 110° C. and 150° C. for more than 60 minutes.

    CONVERTING LIGNOCELLULOSIC FEEDSTOCK TO FUEL

    公开(公告)号:US20230340543A1

    公开(公告)日:2023-10-26

    申请号:US17998759

    申请日:2021-04-23

    Abstract: A process for converting lignocellulosic biomass to fuel, wherein lignocellulosic feedstock is soaked in a sulfuric acid solution to demineralize the feedstock, the demineralized feedstock is pretreated at a temperature between 150° C. and 230° C. and a pH between 1 and 2.5, at least part of the pretreated material is converted to a fermentation production such as ethanol, and at least a portion of a secondary stream, such as still bottoms from the distillation of ethanol, is converted to biogas by anaerobic digestion. Soaking the lignocellulosic feedstock in sulfuric acid solution reduces the amount of sulfuric acid required for the pretreatment, and thus the amount of sulfate carried downstream to the anaerobic digestion. This increases the biogas yield and/or xylose yield. A recycling process, wherein mineralized soaking liquid produced in the soaking process is fed to cation exchange to remove minerals, reduces excess waste of the sulfuric acid and water usage.

    Low temperature pretreatment with sulfur dioxide

    公开(公告)号:US11345935B2

    公开(公告)日:2022-05-31

    申请号:US16761192

    申请日:2018-11-09

    Abstract: A process for producing a fuel from lignocellulosic biomass is disclosed. The process includes obtaining a feedstock comprising lignocellulosic biomass, feeding the feedstock and sulfur dioxide into a pretreatment reactor, wherein a total amount of sulfur dioxide in the pretreatment reactor is greater than 70 wt % based on dry weight lignocellulosic biomass, and heating the feedstock and sulfur dioxide in the pretreatment reactor at one or more temperatures between 110° C. and 150° C. for more than 60 minutes.

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