METHOD FOR PROCESSING NAPHTHA
    4.
    发明申请
    METHOD FOR PROCESSING NAPHTHA 审中-公开
    一种用于处理石脑油

    公开(公告)号:WO2004069962A8

    公开(公告)日:2005-08-18

    申请号:PCT/EP2004000602

    申请日:2004-01-24

    CPC classification number: B01D61/362 C10G7/00 C10G7/08 C10G9/00 C10G31/11

    Abstract: Disclosed is a method for processing naphtha, according to which a) naphtha or a stream generated from naphtha in a preprocessing step is divided into a stream A that is stripped of aromatics and a stream B which is enriched with aromatics in a membrane unit, the aromatics concentration in stream A ranging from 2 to 12 percent by weight (step a); b) partial stream A is directed at least in part into a steam cracker (step b); c) partial stream B is directed at least in part into a unit in which said stream B is divided into a stream C or several streams C' C'', C''',..., which has/have a lower aromatics content than stream B, and a stream D or several streams D', D'', D''',..., which has/have a higher aromatics content than stream B, by means of a thermal process (step c); d) stream C or at least one of the streams C', C'', C''' is delivered as a whole or in part to the feed for the steam cracker or directly to the steam cracker (step d).

    Abstract translation: 一种用于石脑油的后处理,其中a)石脑油或在膜单元中芳烃的贫流A石脑油料流的前处理工序和芳烃富流B中产生的电流被分离,过程,其中的芳族化合物重量浓度在流A的2至12 .-%是(步骤a),b)将部分流一个是至少部分地在蒸汽裂化器(部分流b的步骤c是b))的至少部分地在其通过热过程以相反的分离的单元中执行执行 当前B芳烃的贫流C或多个流C'C“”,C“”“ ...,各自的下芳族化合物含量低于流B包括,并且在过电流乙芳烃富集流D或多个流D” ,D“”,D“”“ ...每个都具有具有如流B(步骤c)的芳族化合物的含量较高,d)中的流C或流C的至少一个”,C‘’,C‘’” 每个完全OD 它部分供给到进料至蒸汽裂化器或蒸汽裂化器本身(步骤d)。

    8.
    发明专利
    未知

    公开(公告)号:DE10305060A1

    公开(公告)日:2004-08-19

    申请号:DE10305060

    申请日:2003-02-07

    Applicant: BASF AG

    Abstract: Process for the work-up of naphtha, wherein a) naphtha or a stream produced from naphtha in a pretreatment step is separated in a membrane unit into a stream A which is depleted in aromatics and a stream B which is enriched in aromatics, with the aromatics concentration in stream A being from 2 to 12% by weight (step a), b) at least part of the substream A is fed to a steam cracker (step b), c) at least part of the substream B is fed to a unit in which it is separated by means of a thermal process into a stream C which has a lower aromatics content than stream B or a plurality of streams C', C'', C''' . . . which each have lower aromatics contents than stream B and a stream D which has a higher aromatics content than stream B or a plurality of streams D', D'', D''' . . . which each have higher aromatics contents than stream B (step c), and d) the stream C or at least one of the streams C', C'', C''', in each case in part or in its entirety, is added to the feed to the steam cracker or fed into the steam cracker itself (step d).

    Crosslinkable copolyimide consisting mainly of repeating units derived from dianhydrides useful as membranes for separating various materials at high feed pressures with high selectivity and high permeability

    公开(公告)号:DE10247417A1

    公开(公告)日:2004-04-22

    申请号:DE10247417

    申请日:2002-10-11

    Abstract: A crosslinkable copolyimide consisting mainly of repeating units derived from dianhydrides of given formula and containing primary amine groups, where these are in the ortho, meta, or para positions to the ether function is new. A crosslinkable copolyimide consisting mainly of repeating units derived from dianhydides of formula:(A), diamines of formula (I), diamines of formula (II): where the amino groups are in the ortho, meta, or para position, and 1 or 2 aromatic nucleus H atoms can be substituted by 1-4X alkyl, and diamines of formula (III):and containing primary amine groups, where these are in the ortho, meta, or para positions to the ether function. R1 = COOH or SO3H. Independent claims are included for: (1) membranes obtained from the crosslinked copolyimides; (2) chromatography columns containing the crosslinked copolyimides as the stationary phase; (3) a method of separating alcohols from mixtures with organic compounds of lower polarity than the alcohol, for separation of ammonia or amines from mixtures with organic compounds of lower polarity than ammonia, and for separation of water, ammonia, H2S, or organic compounds from mixtures with nitrogen or air, separation of olefins or dienes from mixtures with hydrocarbons of higher degree of saturation than the olefin or diene, e.g. separation of olefin/alkane using the membranes described or chromatography columns; (4) an olefin/alkane mixture enriched in olefin compared with the starting mixture by means of a membrane as described, and an alkane enriched stream separated, at a pressure on the membrane feed side higher than 6 bar.

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