PROCEDIMIENTO PARA ELIMINAR MERCAPTANOS DE CORRIENTES DE FLUIDOS QUE LOS CONTIENEN

    公开(公告)号:PE06042001A1

    公开(公告)日:2001-05-28

    申请号:PE0006882000

    申请日:2000-07-10

    Applicant: BASF AG

    CPC classification number: B01D53/1462 B01D53/1487 B01D53/1493 Y02C10/06

    Abstract: DONDE DICHO PROCEDIMIENTO COMPRENDE: i) PONER EN CONTACTO LA CORRIENTE DE FLUIDOS EN UNA ZONA DE ABSORCION O EXTRACCION CON UN LIQUIDO DE LAVADO, EL CUAL CONTIENE: a) POR LO MENOS DE 10% A 70% EN PESO DE UNA ALCANOLAMINA ALIFATICA C2-C12, TAL COMO TRIETANOLAMINA O METILDIETANOLAMINA; b) COMO MAXIMO 5% EN PESO DE UN SOLVENTE FISICO PARA MERCAPTANOS; Y, c) DE 0% A 20% EN PESO DE UNA AMINA PRIMARIA O SECUNDARIA COMO ACTIVADOR, TAL COMO ALCANOLAMINA PRIMARIA O SECUNDARIA O UN N-HETEROCICLO DE 5 o 6 MIEMBROS SATURADO; ALIMENTANDO SUFICIENTE LIQUIDO DE LAVADO A DICHA ZONA, PARA QUE POR LO MENOS CO2 Y H2S SEAN ELIMINADOS SUSTANCIALMENTE EN FORMA COMPLETA DE LA CORRIENTE DE FLUIDOS; Y, b) SEPARAR LA CORRIENTE DE FLUIDOS PURIFICADA Y EL LIQUIDO DE LAVADO CARGADO, Y RETIRARLOS DE DICHA ZONA

    12.
    发明专利
    未知

    公开(公告)号:DE19947845A1

    公开(公告)日:2001-04-12

    申请号:DE19947845

    申请日:1999-10-05

    Applicant: BASF AG

    Abstract: The invention relates to a method for removing COS from a stream of hydrocarbon fluid containing COS, in particular, from a stream of gas, such as for example, natural gas, synthesis gas from heavy oil or heavy residues or refinery gas, or from liquid or liquefied hydrocarbons, such as for example, LPG (Liquefied Petroleum Gas) or NGL (Natural Gas Liquids) and to a wash liquid for use in methods of this type. The stream of fluid is brought into direct contact with the inventive wash fluid in an absorption or extraction zone. Said wash fluid consists of an aqueous amine solution which contains 1.5 to 5 moles/l of an aliphatic alkanolamine having between 2 and 12 C atoms and 0.4 to 1.7 moles/l of a primary or secondary amine as the activator. Substantially all of the COS is removed from the stream of fluid using the inventive amine wash. The stream of fluid which has been substantially cleaned of COS and the wash fluid which is loaded with COS are subsequently separated from one another and both fluids are fed out of the absorption or extraction zone. The wash fluid can subsequently be regenerated in the known manner and can be fed back to the absorption or extraction zone.

    15.
    发明专利
    未知

    公开(公告)号:DE50008248D1

    公开(公告)日:2004-11-18

    申请号:DE50008248

    申请日:2000-07-14

    Applicant: BASF AG

    Abstract: The disclosure concerns a process for removing mercaptans from fluid streams comprising same, especially from hydrocarbon gas streams, for example natural gas, synthesis gas from heavy oil or heavy residues or refinery gas, or else from liquid hydrocarbons, for example LPG (liquefied petroleum gas). The invention comprises intimately contacting the fluid stream in an absorption or extraction zone with a scrubbing liquor comprising at least one aliphatic alkanolamine of 2-12 carbon atoms, the amount of wash liquor being supplied to the absorption or extraction zone being sufficient to remove at least CO2 and H2S essentially completely from the fluid stream, and separating the substantially decontaminated fluid stream and the contaminated wash liquor and discharging them from the absorption zone. The substantially complete removal of CO2 and H2S is accompanied by the removal from the gas, stream of a very large portion of the mercaptans as well, without a significant fraction of the hydrocarbon gases dissolving in the wash liquor.

    PROCEDIMIENTO PARA ELIMINAR MERCAPTANOS DE CORRIENTES DE FLUIDOS QUE LOS CONTIENEN

    公开(公告)号:PE20010604A1

    公开(公告)日:2001-05-28

    申请号:PE0006882000

    申请日:2000-07-10

    Applicant: BASF AG

    Abstract: DONDE DICHO PROCEDIMIENTO COMPRENDE: i) PONER EN CONTACTO LA CORRIENTE DE FLUIDOS EN UNA ZONA DE ABSORCION O EXTRACCION CON UN LIQUIDO DE LAVADO, EL CUAL CONTIENE: a) POR LO MENOS DE 10% A 70% EN PESO DE UNA ALCANOLAMINA ALIFATICA C2-C12, TAL COMO TRIETANOLAMINA O METILDIETANOLAMINA; b) COMO MAXIMO 5% EN PESO DE UN SOLVENTE FISICO PARA MERCAPTANOS; Y, c) DE 0% A 20% EN PESO DE UNA AMINA PRIMARIA O SECUNDARIA COMO ACTIVADOR, TAL COMO ALCANOLAMINA PRIMARIA O SECUNDARIA O UN N-HETEROCICLO DE 5 o 6 MIEMBROS SATURADO; ALIMENTANDO SUFICIENTE LIQUIDO DE LAVADO A DICHA ZONA, PARA QUE POR LO MENOS CO2 Y H2S SEAN ELIMINADOS SUSTANCIALMENTE EN FORMA COMPLETA DE LA CORRIENTE DE FLUIDOS; Y, b) SEPARAR LA CORRIENTE DE FLUIDOS PURIFICADA Y EL LIQUIDO DE LAVADO CARGADO, Y RETIRARLOS DE DICHA ZONA

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