PROCESS FOR PREPARING OLIGOMERS OF BUTENE DESCRIPTION

    公开(公告)号:MY166872A

    公开(公告)日:2018-07-24

    申请号:MYPI2014001284

    申请日:2012-10-25

    Applicant: BASF SE

    Abstract: A process for preparing oligomers by continuous oligomerization of butenes is described, wherein a) a feed stream (1) comprising I-butene and 2-butene in a total concentration of from 10 to 70% by weight and from 10 to 60% by weight of isobutane is reacted until more than 60% by weight of the I-butene comprised in the feed stream (1 ) but less than 50% by weight of the 2-butene comprised in feed stream (1) have been converted into oligomers. b) The oligomers obtained in a) are separated off and optionally passed to a further work-up and the remaining residual stream is fed to work-up by distillation. c) Isobutane is separated off by distillation from the residual stream, and d) the isobutane-depleted stream obtained after the work-up by distillation c) is reacted to form oligomers. (Sole Figure)

    METHOD FOR THERMAL INTEGRATION IN THE HYDROGENATION AND DISTILLATION OF C<sb>3</sb>-C<sb>20</sb> ALDEHYDES

    公开(公告)号:SG11201404813WA

    公开(公告)日:2014-10-30

    申请号:SG11201404813W

    申请日:2013-03-06

    Applicant: BASF SE

    Abstract: The present invention relates to a method for thermal integration in the production of saturated C3-C20 alcohols, in which a hydrogenation feed containing at least one C3-C20 aldehyde is hydrogenated in a hydrogenation zone in the presence of a hydrogen-containing gas, an output is discharged from the hydrogenation zone and subjected to distillation in at least one distillation column, wherein a fraction enriched with saturated C3-C20 alcohols is obtained.

    4.
    发明专利
    未知

    公开(公告)号:DE502006006352D1

    公开(公告)日:2010-04-15

    申请号:DE502006006352

    申请日:2006-09-25

    Applicant: BASF SE

    Abstract: Treatment of wastewater from an aldolization process, containing dissolved and/or dispersed organic impurities, comprises acidifying the wastewater to pH 0-6 and extracting it with an organic liquid produced by stripping the acidified or acidified and extracted wastewater, condensing the stripped compounds and phase-separating the condensate. An independent claim is also included for treatment of wastewater from an aldolization process, containing dissolved and/or dispersed organic impurities, by acidifying the wastewater to pH 0-6, extracting it with an organic liquid and removing volatile organic impurities and a stripping apparatus, where the organic liquid is a low boiler fraction from the distillation of a crude alcohol produced by hydrogenating an aldehyde, the alcohol/aldehyde being n-butanol/n-butyraldehyde, isobutanol/isobutyraldehyde, n-pentanol/n-valeraldehyde, n- and isopentanol/n- and isovaleraldehyde, 2-ethylhexanol/2-ethylhexenal and/or 2-propylheptanol/2-propylheptenal.

    5.
    发明专利
    未知

    公开(公告)号:AT459580T

    公开(公告)日:2010-03-15

    申请号:AT06793779

    申请日:2006-09-25

    Applicant: BASF SE

    Abstract: Treatment of wastewater from an aldolization process, containing dissolved and/or dispersed organic impurities, comprises acidifying the wastewater to pH 0-6 and extracting it with an organic liquid produced by stripping the acidified or acidified and extracted wastewater, condensing the stripped compounds and phase-separating the condensate. An independent claim is also included for treatment of wastewater from an aldolization process, containing dissolved and/or dispersed organic impurities, by acidifying the wastewater to pH 0-6, extracting it with an organic liquid and removing volatile organic impurities and a stripping apparatus, where the organic liquid is a low boiler fraction from the distillation of a crude alcohol produced by hydrogenating an aldehyde, the alcohol/aldehyde being n-butanol/n-butyraldehyde, isobutanol/isobutyraldehyde, n-pentanol/n-valeraldehyde, n- and isopentanol/n- and isovaleraldehyde, 2-ethylhexanol/2-ethylhexenal and/or 2-propylheptanol/2-propylheptenal.

    PROCEDIMIENTO PARA EL PROCESAMIENTO DE UNA DESCARGA DE HIDROFORMILACION LIQUIDA.

    公开(公告)号:ES2207608T5

    公开(公告)日:2009-06-15

    申请号:ES01911637

    申请日:2001-02-13

    Applicant: BASF SE

    Abstract: Procedimiento para el procesamiento de una descarga líquida de una hidroformilación continua, que contiene esencialmente aldehídos, subproductos de alto punto de ebullición, un catalizador de hidroformilación disuelto de forma homogénea, olefinas no reaccionadas, subproductos de bajo punto de ebullición y gas de síntesis disuelto, donde a) la descarga de hidroformilación líquida es expandida, en una primera etapa de expansión, a una presión que está entre 2 y 20 bares por debajo de la presión del reactor, siendo realizada una separación en una fase líquida y una fase gaseosa; y b) la fase líquida obtenida en la primera etapa de expansión es expandida, en una segunda etapa de expansión, a una presión que es menor que la presión de la primera etapa de expansión, siendo realizada una separación en una fase líquida, que contiene esencialmente subproductos de alto punto de ebullición de la hidroformilación, el catalizador de hidroformilación disuelto de forma homogénea y cantidades reducidas de producto de hidroformilación y olefina no reaccionada, y en una fase gaseosa, que contiene esencialmente la cantidad principal del producto de hidroformilación, olefina no reaccionada y subproductos de bajo punto de ebullición.

    PROCEDURE FOR MANUFACTURING OLIGOMERS OF BUTENE

    公开(公告)号:IN1057MUN2014A

    公开(公告)日:2015-05-01

    申请号:IN1057MUN2014

    申请日:2014-05-30

    Applicant: BASF SE

    Abstract: Procedure for manufacturing oligomers by continuous oligomerization of butenes characterized in that a) an initial stream is used which contains 1 butene and 2 butene at a total concentration of 10 to 70 wt% and 10 to 60 wt% of iso butane (called initial stream 1 hereafter) b) said initial stream 1 is converted until more than 60 wt% of the 1 butene contained in initial stream 1 but less than 50 wt% of the 2 butene contained in initial stream 1 are converted into oligomers c) the oligomers obtained in b) are separated and optionally fed to further processing and the remaining stream is fed to a distillation processing step d) iso butane is separated by distillation from the remaining steam e) the iso butane depleted stream (called initial stream 2 hereafter) obtained after the distillation processing step d) is converted into oligomers.

    10.
    发明专利
    未知

    公开(公告)号:AT505440T

    公开(公告)日:2011-04-15

    申请号:AT09159020

    申请日:2006-09-25

    Applicant: BASF SE

    Abstract: Treatment of wastewater from an aldolization process, containing dissolved and/or dispersed organic impurities, comprises acidifying the wastewater to pH 0-6 and extracting it with an organic liquid produced by stripping the acidified or acidified and extracted wastewater, condensing the stripped compounds and phase-separating the condensate. An independent claim is also included for treatment of wastewater from an aldolization process, containing dissolved and/or dispersed organic impurities, by acidifying the wastewater to pH 0-6, extracting it with an organic liquid and removing volatile organic impurities and a stripping apparatus, where the organic liquid is a low boiler fraction from the distillation of a crude alcohol produced by hydrogenating an aldehyde, the alcohol/aldehyde being n-butanol/n-butyraldehyde, isobutanol/isobutyraldehyde, n-pentanol/n-valeraldehyde, n- and isopentanol/n- and isovaleraldehyde, 2-ethylhexanol/2-ethylhexenal and/or 2-propylheptanol/2-propylheptenal.

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