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    • 4. 发明授权
    • Method for isolating olefins from polyolefin plants
    • 从聚烯烃工厂中分离烯烃的方法
    • US06462150B1
    • 2002-10-08
    • US09913074
    • 2001-08-09
    • Stefan BitterlichKaspar EvertzManfred HeckerHans-Jacob Feindt
    • Stefan BitterlichKaspar EvertzManfred HeckerHans-Jacob Feindt
    • C08F234
    • C08F6/001B01J8/007B01J8/24C07C7/005C07C11/02
    • The present invention relates to a method for the isolation of olefins from a gas mixture comprising one or more olefins, inert gas and catalyst poison, where the gas mixture is fed to a separation unit (18) and separated into olefin and inert gas. The method according to the invention has the special feature that an apparatus (17) is installed upstream or downstream of the separation unit (18) and that i) in the case of an upstream apparatus (17), the catalyst poison is at least partially removed from the gas mixture, and ii) in the case of a downstream apparatus (17), the catalyst poison is at least partially removed from the separated-off olefin. The olefins here are preferably isolated from a gas mixture formed as offgas in catalytic gas-phase polymerization for the preparation of polyolefins. The recovery of the olefins from the offgas is of economic importance.
    • 本发明涉及从包含一种或多种烯烃,惰性气体和催化剂毒物的气体混合物中分离烯烃的方法,其中气体混合物被供给到分离单元(18)并分离成烯烃和惰性气体。 根据本发明的方法具有以下特征:设备(17)安装在分离单元(18)的上游或下游,并且在上游设备(17)的情况下,催化剂毒物至少部分地被去除 在下游装置(17)的情况下,催化剂毒物至少部分地从分离的烯烃中除去。这里的烯烃优选与催化气体 - 气体中的废气形成的气体混合物分离, 用于制备聚烯烃的相聚合。 从废气中回收烯烃是经济重要的。
    • 5. 发明授权
    • Method for processing naphtha
    • 石脑油加工方法
    • US07459072B2
    • 2008-12-02
    • US10544427
    • 2004-01-24
    • Stefan BitterlichHartwig VossGunter SchuchRudolf SinnenHeinrich LaibPeter Paessler
    • Stefan BitterlichHartwig VossGunter SchuchRudolf SinnenHeinrich LaibPeter Paessler
    • C10G9/00C10G7/00C10G7/08C10G31/11C07C4/02
    • B01D61/362C10G7/00C10G7/08C10G9/00C10G31/11
    • 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).
    • 用于处理石脑油的方法,其中a)在预处理步骤中将石脑油或由石脑油产生的物流在膜单元中分离成贫的芳烃流A和富含芳族化合物的物流B, 流A中的芳族化合物浓度为2至12重量%(步骤a),b)将至少部分分流A送入蒸汽裂解器(步骤b),c)将至少部分子流B送入 其中通过热处理将其分离成具有比流B或多个流C',C“,C”的较低芳烃含量的流C的单元。 。 。 其具有比流B更低的芳烃含量和具有比流B或多个流D',D“,D”'更高的芳族化合物含量的流D. 。 。 它们各自具有比物流B更高的芳烃含量(步骤c),以及d)在各种情况下部分或全部,流C或者流C',C“,C”'中的至少一个是 添加到蒸汽裂化器的进料中或者进入蒸汽裂化器本身(步骤d)。
    • 7. 发明申请
    • Method for processing naphtha
    • 石脑油加工方法
    • US20060081500A1
    • 2006-04-20
    • US10544427
    • 2004-01-24
    • Stefan BitterlichHartwig VobGunter SchuchRudolf SinnenHeinrich LaibPeter Pabler
    • Stefan BitterlichHartwig VobGunter SchuchRudolf SinnenHeinrich LaibPeter Pabler
    • C10G9/36C07C4/02
    • B01D61/362C10G7/00C10G7/08C10G9/00C10G31/11
    • 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).
    • 用于处理石脑油的方法,其中a)在预处理步骤中将石脑油或由石脑油产生的物流在膜单元中分离成贫的芳烃流A和富含芳族化合物的物流B, 流A中的芳族化合物浓度为2至12重量%(步骤a),b)将至少部分分流A送入蒸汽裂解器(步骤b),c)将至少部分子流B送入 其中通过热处理将其分离成具有比流B或多个流C',C“,C”的较低芳烃含量的流C的单元。 。 。 其具有比流B更低的芳烃含量和具有比流B或多个流D',D“,D”'更高的芳族化合物含量的流D. 。 。 它们各自具有比物流B更高的芳烃含量(步骤c),以及d)在各种情况下部分或全部,流C或者流C',C“,C”'中的至少一个是 添加到蒸汽裂化器的进料中或者进入蒸汽裂化器本身(步骤d)。