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    SYSTEMS CAPABLE OF ADDING CELLULOSIC BIOMASS TO A DIGESTION UNIT OPERATING AT HIGH PRESSURES AND ASSOCIATED METHODS FORCELLULOSIC BIOMASS PROCESSING
    12.
    发明申请
    SYSTEMS CAPABLE OF ADDING CELLULOSIC BIOMASS TO A DIGESTION UNIT OPERATING AT HIGH PRESSURES AND ASSOCIATED METHODS FORCELLULOSIC BIOMASS PROCESSING 有权
    能够将细胞生物量添加到高压操作的消化单元和相关方法的体系生物质生物质处理

    公开(公告)号：US20150132201A1

    公开(公告)日：2015-05-14

    申请号：US14596805

    申请日：2015-01-14

    Applicant: SHELL OIL COMPANY

    Inventor： Juben Nemchand CHHEDA ,  Thomas Lamar FLOWERS ,  Joseph Broun POWELL

    IPC: B01J19/24

    CPC classification number: B01J19/245 ,  B01J19/24 ,  B01J2219/24 ,  C10G1/002 ,  C10G1/065 ,  C10G3/42 ,  C10G2300/1014 ,  C10L1/02 ,  C13K1/02 ,  Y02P30/20

    Abstract: When processing cellulosic biomass, it may be desirable for a digestion unit to operate without being fully depressurized for process efficiency purposes. Methods for processing cellulosic biomass may comprise providing a biomass conversion system comprising a pressurization zone and a digestion unit that are operatively connected to one another; providing cellulosic biomass at a first pressure; introducing at least a portion of the cellulosic biomass into the pressurization zone and pressurizing the pressurization zone to a second pressure higher than the first pressure; after pressurizing the pressurization zone, transferring at least a portion of the cellulosic biomass from the pressurization zone to the digestion unit, which is at a third pressure that is less than or equal to the second pressure but higher than the first pressure; and digesting at least a portion of the cellulosic biomass in the digestion unit to produce a hydrolysate comprising soluble carbohydrates.

    Abstract translation: 当处理纤维素生物质时，为了过程效率目的，消化单元可能需要操作而没有完全减压。 处理纤维素生物质的方法可以包括提供生物质转化系统，其包括可操作地彼此连接的加压区和消化单元; 在第一压力下提供纤维素生物质; 将至少一部分纤维素生物质引入加压区并将加压区加压至高于第一压力的第二压力; 在对加压区进行加压之后，将至少一部分纤维素生物质从加压区转移到消化单元，消化单元处于小于或等于第二压力但高于第一压力的第三压力; 并消化消化单元中的至少一部分纤维素生物质以产生包含可溶性碳水化合物的水解产物。

    PROCESS FOR THE RECOVERY OF FURFURAL
    13.
    发明申请
    PROCESS FOR THE RECOVERY OF FURFURAL 审中-公开

    公开(公告)号：US20190276422A1

    公开(公告)日：2019-09-12

    申请号：US16346317

    申请日：2017-10-30

    Applicant: SHELL OIL COMPANY

    Inventor： Juben Nemchand CHHEDA ,  Jean Paul Andre Marie Joseph Ghislain LANGE

    IPC: C07D307/50 ,  B01D3/36

    Abstract: Disclosed is a process for the extraction of furfural including: (a) subjecting a composition comprising furfural, water, at least one inorganic acid, at least one organic acid and a solvent mixture comprising an aromatic solvent and an oxygenate solvent, to a first separation step providing: (i) a first organic phase; (b) subjecting the first organic phase to a first distillation step providing: (i) a first top stream comprising furfural and a portion of the at least one organic acid; (c) subjecting the first top stream from step (b) to a second separation step providing: (i) a second top stream enriched with furfural; (d) subjecting the second top stream from step (c) to a second distillation step providing: (i) a third top stream comprising a furfural-water azeotrope, and (ii) a third bottom stream comprising furfural.

    PROCESS FOR THE RECOVERY OF FURFURAL
    14.
    发明申请
    PROCESS FOR THE RECOVERY OF FURFURAL 审中-公开

    公开(公告)号：US20190263767A1

    公开(公告)日：2019-08-29

    申请号：US16346398

    申请日：2017-10-30

    Applicant: SHELL OIL COMPANY

    Inventor： Juben Nemchand CHHEDA ,  Charu EHRENREICH-GUREJA ,  Jean Paul Andre Marie Joseph Ghislain LANGE

    IPC: C07D307/50 ,  C07D307/48

    Abstract: Disclosed is a process for the extraction of furfural which includes: (a) subjecting a composition comprising furfural, water, at least one acid and an aromatic solvent, with a boiling point higher than that of furfural, to a first separation step providing: (i) an organic phase, and (ii) an aqueous phase; (b) subjecting the aqueous phase of step (a) to a first distillation step to provide: (i) a first in top stream comprising a furfural-water azeotrope; (c) subjecting the first top stream of step (b) to a second separation step to provide: (i) a second top stream comprising a portion of the furfural-water azeotrope; (d) subjecting the second top stream of step (c) to a second distillation step to provide: (i) a third top stream enriched with the furfural-water azeotropic mixture; (e) subjecting the organic phase of step (a) to a third distillation step to provide: a fourth top stream comprising furfural.

    METHODS AND SYSTEMS FOR PROCESSING CELLULOSIC BIOMASS
    17.
    发明申请
    METHODS AND SYSTEMS FOR PROCESSING CELLULOSIC BIOMASS 审中-公开
    用于处理细胞生物质的方法和系统

    公开(公告)号：US20160184796A1

    公开(公告)日：2016-06-30

    申请号：US14980427

    申请日：2015-12-28

    Applicant: SHELL OIL COMPANY

    Inventor： Joseph Broun POWELL ,  Glenn Charles KOMPLIN ,  Juben Nemchand CHHEDA

    IPC: B01J19/24 ,  B01D3/14 ,  B01D11/04

    CPC classification number: B01J19/24 ,  B01D3/143 ,  B01D3/148 ,  B01D11/04 ,  B01D11/0488 ,  B01J2219/24 ,  C10G1/002 ,  C10G1/065 ,  C10G1/083 ,  C10G3/50 ,  C10G2300/1014 ,  D21C3/20 ,  D21C3/222 ,  D21C11/0007 ,  D21C11/0042 ,  Y02P30/20

    Abstract: Separation of a product of digestion of cellulosic biomass solids may be challenging due to the various components contained therein. Methods and systems for processing cellulosic biomass, particularly a reaction product of a hydrothermal reaction containing lignin-derived products, such as phenolics, comprise providing the reaction product to a separation zone comprising a liquid-liquid extraction or phase separation unit. The liquid-liquid extraction or phase separation unit can provide an aqueous portion and a non-aqueous portion, where these portions can be separated into various fractions individually. For example, desirable compounds in the aqueous portion and non-aqueous portion can be recovered from the portions individually and optionally combined to be further processed into a fuels product. Heavier components in the aqueous portion and non-aqueous portion can be recovered from the portions individually and used in the process, such as phenolics that can be used as a digestion solvent.

    Abstract translation: 纤维素生物质固体的消化产物的分离可能是由于其中所含的各种组分而具有挑战性的。 用于处理纤维素生物质的方法和系统，特别是含有木质素衍生产物如酚醛的水热反应的反应产物包括将反应产物提供到包括液 - 液萃取或相分离单元的分离区。 液 - 液萃取或相分离装置可提供含水部分和非水部分，其中这些部分可分别分成各种馏分。 例如，水性部分和非水部分中的期望的化合物可以从这些部分单独回收并任选地组合以进一步加工成燃料产物。 水性部分和非水部分中的较重组分可以单独回收并在该方法中使用，例如可用作消化溶剂的酚类。

    METHODS AND SYSTEMS FOR PROCESSING CELLULOSIC BIOMASS
    18.
    发明申请
    METHODS AND SYSTEMS FOR PROCESSING CELLULOSIC BIOMASS 有权
    用于处理细胞生物质的方法和系统

    公开(公告)号：US20160097000A1

    公开(公告)日：2016-04-07

    申请号：US14868542

    申请日：2015-09-29

    Applicant: SHELL OIL COMPANY

    Inventor： Joseph Broun POWELL ,  Juben Nemchand CHHEDA ,  Lamar Lane JOFFRION ,  Philip Walter ANDERSON

    IPC: C10G3/00 ,  C10G1/00 ,  C10G1/08

    CPC classification number: C10G3/50 ,  C08H6/00 ,  C08H8/00 ,  C08L97/005 ,  C10G1/002 ,  C10G1/065 ,  C10G1/083 ,  C10G1/086 ,  C10G3/42 ,  C10G3/56 ,  C10G3/57 ,  C10G2300/1014 ,  C10G2300/4081 ,  C10G2300/802 ,  C10G2300/805 ,  D21C3/20 ,  D21C3/222 ,  D21C11/0007 ,  Y02P30/20

    Abstract: Digestion of cellulosic biomass solids may be complicated by release of lignin therefrom. Methods and systems for processing a reaction product containing lignin-derived products, such as phenolics, can comprise hydrotreating the reaction product to convert the lignin-derived products to desired higher molecular weight compounds. The methods can further include separating the higher molecular weight compounds from unconverted products, such as unconverted phenolics, and recycling the unconverted phenolics for use as at least a portion of the digestion solvent and for further conversion to desired higher molecular weight compounds with additional hydrotreatment. The methods and systems can further include generating hydrogen with the further hydrotreatment.

    Abstract translation: 纤维素生物质固体的消化可能由于从其中释放木质素而变得复杂。 用于处理含有木质素衍生产物如酚类的反应产物的方法和系统可以包括加氢处理反应产物以将木质素衍生产物转化为所需的较高分子量化合物。 该方法还可以包括从未转化的产物（例如未转化的酚类）分离较高分子量的化合物，以及将未转化的酚类物质再循环用作消化溶剂的至少一部分，并进一步转化为具有额外加氢处理的所需较高分子量化合物。 所述方法和系统可进一步包括用进一步加氢处理产生氢气。

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