MECHANICAL ACTIVATION OF BIOMASS FOR HYDROTHERMAL LIQUEFACTION

    公开(公告)号:US20230348792A1

    公开(公告)日:2023-11-02

    申请号:US18140275

    申请日:2023-04-27

    Abstract: Methods for obtaining a biocrude intermediate by hydrothermal liquefaction of plant wastes are provided. Using a waste feed having a high cellulose content, the method involves grinding the waste feed to obtain a pulverized waste feed, and subjecting the pulverized waste feed to hydrothermal liquefaction at a temperature at or greater than at about 250° C. At this temperature or greater a catalyst is not necessary to obtain the biocrude. A lower temperature can be used, such as greater than about 150° C. in presence of a catalyst. The step of grinding the plant material, for example ball grinding, reduces particle size and crystallinity, and combined with the high temperature treatment improves the yield of biocrude. Biocrude can be upgraded to biofuel by high temperature hydrodeoxygenating in the presence of hydrogen. Plant wastes that would otherwise contribute green house gases are instead converted to fuels.

    Hydrothermal liquefaction for biomass

    公开(公告)号:US11286432B2

    公开(公告)日:2022-03-29

    申请号:US16583582

    申请日:2019-09-26

    Abstract: Catalyst composition and parameters for catalytic hydrothermal liquefaction of biomass to bio-oil fuels target municipal solid waste (MSW) rather than lignin rich plant waste typically sought for bio-oil production. An HTL (Hydrothermal Liquefaction) reactor generates bio-fuel from municipal solid waste (MSW), including receiving, in the HTL reactor, non-lignin based waste from a municipal processing stream, and adding a solvent for extracting sugars from green waste components of the municipal processing stream. The reactor extracts a liquid from the received waste, and converts water soluble products in the liquid into oil soluble products via C—C (carbon-to-carbon) coupling reactions. A catalyst added to the resulting aqueous stream recovers a beneficial oil product, and is optimized by tuning acid and base sites on the solid catalyst.

    WATER-ASSISTED ZEOLITE UPGRADING OF OILS

    公开(公告)号:US20210179950A1

    公开(公告)日:2021-06-17

    申请号:US17055014

    申请日:2019-05-15

    Abstract: A petroleum refining method for upgrading petroleum products improves the efficiency and reduces the costs of upgrading oils, such as lipids, bitumen, crude oil, fracking oils, synthetic oils, and other feeds, to produce useful fuels and chemical precursor streams. Usage of a specific type of zeolite (ZSM-5) catalyst, supercritical water to control coke formation, and a specific response to phase behavior and other catalytic effects optimize the process. A prescribed set of reactor conditions employing supercritical water increases activity of the catalyst in industrial reactions.

    Ethanol derived petrochemicals
    5.
    发明授权

    公开(公告)号:US11773331B2

    公开(公告)日:2023-10-03

    申请号:US17713818

    申请日:2022-04-05

    CPC classification number: C10G1/086 C10G1/065 C10G1/083 C10G2300/805

    Abstract: Methods are described herein for upgrading ad refining hydrocarbons, and producing at least one petrochemical product, the method including: preparing a reaction mixture by adding at least two of: a quantity of bioethanol, a quantity of hydrocarbon, and a quantity of water to a reactor containment; combining the reaction mixture with a quantity of catalyst in the reactor containment; applying reaction conditions to the reactor containment thereby generating supercritical conditions for the reaction mixture and obtaining a product mixture; and extracting at least one petrochemical product from the product mixture.

    Water-assisted zeolite upgrading of oils

    公开(公告)号:US11566186B2

    公开(公告)日:2023-01-31

    申请号:US17055014

    申请日:2019-05-15

    Abstract: A petroleum refining method for upgrading petroleum products improves the efficiency and reduces the costs of upgrading oils, such as lipids, bitumen, crude oil, fracking oils, synthetic oils, and other feeds, to produce useful fuels and chemical precursor streams. Usage of a specific type of zeolite (ZSM-5) catalyst, supercritical water to control coke formation, and a specific response to phase behavior and other catalytic effects optimize the process. A prescribed set of reactor conditions employing supercritical water increases activity of the catalyst in industrial reactions.

    ETHANOL DERIVED PETROCHEMICALS
    7.
    发明申请

    公开(公告)号:US20220325184A1

    公开(公告)日:2022-10-13

    申请号:US17713818

    申请日:2022-04-05

    Abstract: Methods are described herein for upgrading ad refining hydrocarbons, and producing at least one petrochemical product, the method including: preparing a reaction mixture by adding at least two of: a quantity of bioethanol, a quantity of hydrocarbon, and a quantity of water to a reactor containment; combining the reaction mixture with a quantity of catalyst in the reactor containment; applying reaction conditions to the reactor containment thereby generating supercritical conditions for the reaction mixture and obtaining a product mixture; and extracting at least one petrochemical product from the product mixture.

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