System for Treating Renewable Feedstocks

    公开(公告)号:US20220127536A1

    公开(公告)日:2022-04-28

    申请号:US17647288

    申请日:2022-01-06

    Abstract: A system that includes a feedstock of a non-petroleum or renewable feedstock containing oxygen and contaminants of one or more of metals, gums, and resins that is introduced into the reactor at a flow velocity of from 20 ft/sec to 100 ft/sec. The feedstock is heated within the reactor to a temperature of from 700° F. to 1100° F. to remove and/or reduce the content of one or more of gums and resins in the fats and/or oils of the feedstock. The system further includes a reactor product that is formed in the reactor from the feedstock that has the one or more of gums and resins in the fats and/or oils of the feedstock removed and/or reduced and a heat exchanger to cool the reactor product. A separator unit separates and removes non-condensable gases, metals and water from the cooled reactor product. A final product of the system is separated from the non-condensable gases, metals and water from the cooled reactor product. The final product has an oxygen content that is 60% or less of that of the feedstock, and wherein the final product comprises 25 wt % or less of any triglycerides, monoglycerides, diglycerides, free fatty acids, phosphatides, sterols, tocopherols, tocotrienols, and fatty alcohols, from 5 wt % to 30 wt % naphtha, and 50 wt % or more diesel.

    Pyrolysis reactor system and method

    公开(公告)号:US11427762B2

    公开(公告)日:2022-08-30

    申请号:US16828303

    申请日:2020-03-24

    Abstract: A system for the pyrolysis of a pyrolysis feedstock utilizes a pyrolysis reactor for producing pyrolysis products from the pyrolysis feedstock to be pyrolyzed. An eductor condenser unit in fluid communication with the pyrolysis reactor is used to condense pyrolysis gases. The eductor condenser unit has an eductor assembly having an eductor body that defines a first flow path with a venturi restriction disposed therein for receiving a pressurized coolant fluid and a second flow path for receiving pyrolysis gases from the pyrolysis reactor The second flow path intersects the first flow path so that the received pyrolysis gases are combined with the coolant fluid. The eductor body has a discharge to allow the combined coolant fluid and pyrolysis gases to be discharged together from the eductor. A mixing chamber in fluid communication with the discharge of the eductor to facilitates mixing of the combined coolant fluid and pyrolysis gases, wherein at least a portion of the pyrolysis gases are condensed within the mixing chamber.

    Process for Hydroprocessing of Non-Petroleum Feedstocks

    公开(公告)号:US20210214618A1

    公开(公告)日:2021-07-15

    申请号:US17217585

    申请日:2021-03-30

    Abstract: A method of hydroprocessing is performed wherein non-petroleum feedstocks, such as those containing from about 10% or more olefinic compounds or heteroatom contaminants by weight, are treated in a first reaction zone to provide reaction products. The process involves introducing the feedstock along with diluents or a recycle and hydrogen in a first reaction zone and allowing the feed and hydrogen to react in a liquid phase within the first reaction zone to produce reaction products. The reaction products are cooled and/or water is removed from the reaction products. At least a portion of the cooled and/or separated reaction product are introduced as a feed along with hydrogen into a second reaction zone containing a hydroprocessing catalyst. The feed and hydrogen are allowed to react in a liquid phase within the second reaction zone to produce a second-reaction-zone reaction product.

    Process for Hydroprocessing of Non-Petroleum Feedstocks

    公开(公告)号:US20200087577A1

    公开(公告)日:2020-03-19

    申请号:US16694602

    申请日:2019-11-25

    Abstract: A method of hydroprocessing is performed wherein non-petroleum feedstocks, such as those containing from about 10% or more olefinic compounds or heteroatom contaminants by weight, are treated in a first reaction zone to provide reaction products. The process involves introducing the feedstock along with diluents or a recycle and hydrogen in a first reaction zone and allowing the feed and hydrogen to react in a liquid phase within the first reaction zone to produce reaction products. The reaction products are cooled and/or water is removed from the reaction products. At least a portion of the cooled and/or separated reaction product are introduced as a feed along with hydrogen into a second reaction zone containing a hydroprocessing catalyst. The feed and hydrogen are allowed to react in a liquid phase within the second reaction zone to produce a second-reaction-zone reaction product.

    Heavy Fuel Oil Product
    28.
    发明申请

    公开(公告)号:US20190338205A1

    公开(公告)日:2019-11-07

    申请号:US16511177

    申请日:2019-07-15

    Abstract: A heavy fuel oil product consists essentially of a hydroprocessed product of a high-sulfur-content feedstock that is at least one of A) a feedstock that is non-compliant with ISO 8217: 2017; B) a feedstock that is of non-merchantable quality as a residual marine fuel oil, and C) an intermediate product obtained by hydroprocessing a feedstock that is non-compliant with ISO 8217: 2017 so that the intermediate product is compliant with ISO 8217: 2017 but has a sulfur content of from 0.5 wt. % or more, the hydroprocessed product having a final sulfur content (ISO 14596 or ISO 8754) of less than 0.5 wt. %.

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