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    • 5. 发明申请
    • PROCESS FOR PRODUCING n-BUTYLALKYL ETHERS
    • 工艺生产N- BUTYLALKYLETHERN
    • WO9812164A3
    • 1999-04-01
    • PCT/EP9704703
    • 1997-08-29
    • BASF AGKANAND JUERGENROEPER MICHAEL
    • KANAND JUERGENROEPER MICHAEL
    • B01J31/24C07B61/00C07C41/00C07C41/06C07C41/20C07C41/32C07C43/04
    • C07C41/06C07C41/20C07C41/32C07C41/54C07C43/15C07C43/04C07C43/303
    • In a process for producing n-butylalkyl ethers, (a) 1,3-butadiene or a butadiene-containing hydrocarbon mixture is reacted with an alcohol of formula ROH (I), in which the radical R is a C2-C20 alkyl or alkenyl group substituted or not with 1 to 2 C1-C10 alkoxy or hydroxy groups, a C6-C10 aryl or C7-C11 aralkyl group or a methyl group, at an increased temperature and pressure in the presence of a Brönsted acid or in the presence of a complex of an element of groups Ib, VIIb or VIIIb of the periodic table of elements with a phosphorus- or nitrogen-containing ligand, yielding a mixture of addition products of formulas (II) and (III); (b) the isomers are separated; (c) addition product III is isomerised into addition product II; (d) addition product II is hydrogenated in the presence of a homogeneous or heterogeneous transition metal element catalyst in the liquid phase or in the presence of a heterogeneous, transition metal element-containing catalyst in the gas phase, yielding n-butylalkyl ether of formula (IV).
    • 通过一种用于制备过程正Butylalkylethern:1)1,3-丁二烯或烃混合物与下式的醇含丁二烯的:ROH,其中R是未取代的或被1至2的C1〜C10烷氧基 或羟基取代的C2至C20烷基或链烯基,C6至C10芳基或C7-C11芳烷基团或甲基基团,在升高的温度和在布朗斯台德酸的或在存在升高的压力 从Ib族,VIIB或用含磷或含氮配体的元素的周期表VIIIb的元素的复合物的存在下反应得到下式的加合物(II)和混合物(III); b)分离的异构体; c)该加合物III异构化为加合物II和d)氢化所述加合物II在均相或非均相过渡金属元素催化剂的在液相中或在非均相,含过渡金属元素的催化剂的在气相存在下式的n Butylalkylether存在(IV) ,
    • 7. 发明申请
    • METHOD FOR PRODUCING ALKYLARYL COMPOUNDS
    • 用于生产烷CONNECTIONS
    • WO2005061447A3
    • 2007-01-04
    • PCT/EP2004014444
    • 2004-12-17
    • BASF AGBOTTKE NILSTROPSCH JUERGENNARBESHUBER THOMASSTEPHAN JUERGENROEPER MICHAELHEIDEMANN THOMASSTEINBRENNER ULRICHBENFER REGINA
    • BOTTKE NILSTROPSCH JUERGENNARBESHUBER THOMASSTEPHAN JUERGENROEPER MICHAELHEIDEMANN THOMASSTEINBRENNER ULRICHBENFER REGINA
    • C07C2/66C07C303/06C07C309/31C11D1/22C11D11/04
    • C07C6/04C07C2/08C07C2/66C07C5/2506C07C303/06C11D1/22C11D11/04C07C309/31C07C11/02C07C11/10C07C15/107
    • The production of alkylaryl compounds comprises the following stages: a) reaction of a C4/C5 olefin mixture on a metathesis catalyst to produce a C 4-8 olefin mixture containing 2-pentene and the optional isolation of the C 4-8 olefin mixture; b) isolation of between 5 and 100 % of the 2-pentene obtained in step a) and subsequent reaction on an isomerisation catalyst to form a mixture of 2-pentene and 1-pentene, which is returned to stage a); c) dimerisation of the C 4-8 olefin mixture obtained in stage b) after the isolation process, to form a mixture containing C 8-16 olefins, isolation of the C 8-16 olefins and optional isolation of a partial stream of the latter; d) reaction of the C 8-16 olefin mixtures obtained in stage c) or the partial stream with an aromatic hydrocarbon in the presence of an alkylation catalyst, to form alkyl aromatic compounds, whereby prior to the reaction an additional 0 to 60 wt. % linear olefins, in relation to the C 8-16 olefin mixtures obtained in stage c), can be added; e) optional sulphonation of the alkyl aromatic compounds obtained in stage d) and neutralisation to form alkylaryl sulphonates, whereby prior to the sulphonation an additional 0 to 60 wt. % linear alkyl benzols, in relation to the alkyl aromatic compounds obtained in stage d), can be added, provided that there were no admixtures in stage d); f) optional mixing of the alkylaryl sulphonates obtained in stage e) with between 0 and 60 wt. %, linear alkylaryl sulphonates, in relation to the alkylaryl sulphonates obtained in stage e), provided that there were no admixtures in stages d) and e).
    • 烷基芳基化合物通过C4 / C5烯烃混合物的超过一个C含有2-戊烯 4-8 烯烃混合物的制备复分解催化剂的C 的)反应,和可选地移除该制剂 4-8 烯烃混合物,b)中的5%至100%的分离在步骤a)所得2-戊烯和异构化催化剂的2-戊烯与1-戊烯的混合物随后的反应,在阶段a) 再循环,C)C的分离之后,在步骤b中得到的二聚) 4-8 在二聚催化剂存在下烯烃混合物,得到含烯烃-C 8-16 混合物, 的C 8-16 烯烃,和任选除去一个部分流体,D)在步骤C中获得的化合物反应)C 8-16 烯烃混合物或所述部分与芳族料流的分离 在烷基化催化剂的存在下烃以形成烷基芳香族Ve的 rbindungen,其中烯烃,e)可以反应,0〜60重量%之前添加到直链烯烃,基于在步骤c得到的)C在磺化 8-16,任选地 获得步骤d)的烷基芳族化合物中和以得到烷基芳基磺酸盐,其中之前的磺化,0至60重量%,基于在步骤d)中获得的烷基,可被加入到直链烷基苯的芳族化合物中,如果在步骤d没有掺合)下进行 中,f)如果到60重量%)的0)在步骤e中得到的烷基芳基磺酸盐的适当的混合,基于在步骤e烷芳基磺酸盐所获得的),线性烷基芳基磺酸盐,如果在步骤没有外加剂d)和e被执行。