REMOVAL OF UNWANTED MINERAL OIL HYDROCARBONS

    公开(公告)号:US20240182812A1

    公开(公告)日:2024-06-06

    申请号:US18556600

    申请日:2021-09-14

    IPC分类号: C11B3/12 C11B3/00 C11B3/14

    CPC分类号: C11B3/12 C11B3/001 C11B3/14

    摘要: Present invention relates to a process for reducing the content of MOSH and/or MOAH from vegetable lauric oil, wherein the process is comprising the step of subjecting vegetable lauric oil to a short-path evaporation, that is performed at a pressure of below 1 mbar, at a temperature in a range of 180 to 270° C., and with a feed rate per unit area of evaporator surface of the shorth-path evaporation equipment in a range of from 10 to 400 kg/h·m2. It relates to the use of short-path evaporation performed at a pressure below 1 mbar, at a temperature in a range of 180 to 270° C., and with a feed rate per unit area of evaporator surface of the shorth-path evaporation equipment in a range of from 10 to 400 kg/h·m2, for reducing the content of MOSH and/or MOAH from vegetable lauric oil.

    OILS WITHOUT UNWANTED CONTAMINANTS
    4.
    发明公开

    公开(公告)号:US20240117268A1

    公开(公告)日:2024-04-11

    申请号:US18392041

    申请日:2023-12-21

    发明人: Falk BRUSE

    摘要: The present invention relates to a process for preparing a refined vegetable oil. It relates to a process for reducing the content of free chloropropanols and chloropropanol fatty acid esters in a vegetable oil, and it is comprising the following steps in order: a) refining a vegetable oil, wherein the refining is comprising at least a deodorization step at a temperature below 230° C., and subjecting the refined vegetable oil to a short path evaporation, and collecting a vegetable oil having a content of free chloropropanols and chloropropanol fatty acid esters of not more than 500 ppb and a color expressed as its red component equal or below 3.0.

    PROCESS FOR REFINING CRUDE TALL OIL
    7.
    发明公开

    公开(公告)号:US20230407203A1

    公开(公告)日:2023-12-21

    申请号:US18208412

    申请日:2023-06-12

    IPC分类号: C11B3/12 C10G3/00

    摘要: The disclosure relates to a method for refining crude tall oil, wherein the method comprises first evaporating tall oil material (10) in a first evaporator (100) whereafter the first fraction (11) is fed to a first distilling column (200) and the second fraction (12) is fed to further evaporation. The condensate(s) recovered from the further evaporation(s) is fed to a second distilling column (300).
    The present disclosure further concerns the use of different fractions obtained by the method for the production of biofuels or components thereof.

    REMOVAL OF UNWANTED MINERAL OIL HYDROCARBONS

    公开(公告)号:US20230354857A1

    公开(公告)日:2023-11-09

    申请号:US18040178

    申请日:2021-07-28

    IPC分类号: C11B3/12 A23L5/20

    CPC分类号: A23L5/21 C11B3/12

    摘要: Present invention relates to a process for reducing the MOSH and/or MOAH content from vegetable lauric oil, comprising steps of: a) subjecting the vegetable lauric oil to a short-path evaporation, wherein the short-path evaporation is performed at a pressure of below 1 mbar, at an evaporator temperature in a range of from 150 to 200° C. and with a feed rate per unit area of evaporator surface of the shorth-path evaporation equipment in a range of from 10 to 50 kg/h.m2, b) Contacting the retentate vegetable lauric oil of step a) with an adsorbent, and c) Subjecting the bleached retentate vegetable lauric oil of step b) to a further refining step carried out in an oil refining equipment consisting of a stripping column with packing and not more than one oil collection tray or in a deodorizer, and obtaining a refined retentate vegetable lauric oil.

    REMOVAL OF UNWANTED MINERAL OIL HYDROCARBONS
    10.
    发明公开

    公开(公告)号:US20230348813A1

    公开(公告)日:2023-11-02

    申请号:US18040052

    申请日:2021-07-28

    摘要: Present invention relates to a process for reducing the content of MOSH and/or MOAH from vegetable liquid oil, wherein the process is comprising the step of subjecting vegetable liquid oil to a short-path evaporation, wherein the short-path evaporation is performed at a pressure of below 1 mbar, at an evaporator temperature in a range of from 200° C. to 300° C., and with a feed rate per unit area of evaporator surface of the shorth-path evaporation equipment in a range of from 30 to 220 kg/h·m2. Present invention further relates to the use of short-path evaporation performed at a pressure below 1 mbar, at an evaporator temperature of from 200 to 300° C., and a feed rate per unit area of evaporator surface of the shorth-path evaporation equipment in a range of from 30 to 220 kg/h·m2, for reducing the content of MOSH and/or MOAH from vegetable liquid oil.