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    • 1. 发明申请
    • Method for producing oligomers derived from butenes
    • 生产由丁烯衍生的低聚物的方法
    • US20050288471A1
    • 2005-12-29
    • US10533082
    • 2003-10-28
    • Stefan BitterlichHartwig VossGunter SchuchThomas Heidemann
    • Stefan BitterlichHartwig VossGunter SchuchThomas Heidemann
    • C07C2/24C07C7/13C08F10/00C08F110/10C08F210/10
    • C07C2/24C07C7/13C07C2523/755C07C11/08
    • The present invention relates to a process for preparing oligomers consisting mainly of repeating units derived from 1- or 2-butene from a hydrocarbon stream consisting substantially of branched and linear hydrocarbon compounds having 4 carbon atoms, and comprising olefinic branched and linear hydrocarbon compounds having 4 carbon atoms (C4 starting stream) by a. in step a), separating the C4 starting stream into a fraction consisting mainly of linear hydrocarbon compounds having 4 carbon atoms (l-C4 fraction) and a fraction consisting mainly of branched hydrocarbon compounds having 4 carbon atoms (b-C4 fraction), by contacting the C4 starting stream with a membrane which is easier to pass for linear hydrocarbon compounds having 4 carbon atoms than for branched hydrocarbon compounds having 4 carbon atoms, b. in step b), optionally after removing butanes, oligomerizing the olefinic hydrocarbon compounds having 4 carbon atoms present in the l-C4 fraction, c. in step c), subjecting the olefinic hydrocarbon compounds having 4 carbon atoms present in the b-C4 fraction to one of the following steps: c1. reaction with methanol to give methyl tert-butyl ether (step c1) c2. hydroformylation to give substantially isovaleraldehyde (step c2) c3. polymerization to polyisobutylene (step c3) c4. dimerization to 2,4,4-trimethyl-1-pentene (step c4) c5. alkylation, substantially to form saturated hydrocarbon compounds having 8 or 9 carbon atoms (step c5).
    • 本发明涉及一种制备低聚物的方法,所述低聚物主要由来自1-或2-丁烯的重复单元组成,所述烃流基本上由具有4个碳原子的支链和直链烃化合物组成的烃料流,并且包含具有4个碳原子的烯烃支链和直链烃化合物 碳原子(C 4 H 3起始物流)。 在步骤a)中,将C 4 S起始物流分离成主要由具有4个碳原子的直链烃化合物(1 C 4 H 3馏分)组成的馏分和主要由支链 通过使C 4-14原料流与容易通过具有4个碳原子的直链烃化合物的膜接触,使具有4个碳原子的烃化合物(bC 4 H 4) 对于具有4个碳原子的支链烃化合物,b。 在步骤b)中,任选地在除去丁烷之后,使存在于1-C 4 H 4馏分中的具有4个碳原子的烯烃化合物低聚,c。 在步骤c)中,将存在于b-C 4 S 4馏分中的具有4个碳原子的烯烃化合物进行以下步骤之一:c1。 与甲醇反应,得到甲基叔丁基醚(步骤c1)c2。 加氢甲酰化得到基本上异戊醛(步骤c2)c3。 聚合到聚异丁烯(步骤c3)c4。 二聚成2,4,4-三甲基-1-戊烯(步骤c4)c5。 烷基化,基本上形成具有8或9个碳原子的饱和烃化合物(步骤c5)。
    • 2. 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)。