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    • 55. 发明申请
    • Method for producing alkylaryl compounds
    • 烷基芳基化合物的制备方法
    • US20070142258A1
    • 2007-06-21
    • US10583140
    • 2004-12-17
    • Ulrich SteinbrennerThomas HeidemannMichael RoperJurgen StephanThomas NarbeshuberJurgen TropschNils BottkeRegina Benfer
    • Ulrich SteinbrennerThomas HeidemannMichael RoperJurgen StephanThomas NarbeshuberJurgen TropschNils BottkeRegina Benfer
    • C09D9/00
    • C07C6/04C07C2/08C07C2/66C07C5/2506C07C303/06C11D1/22C11D11/04C07C309/31C07C11/02C07C11/10C07C15/107
    • The preparation of alkylaryl compounds takes place by a) reaction of a C4/C5-olefin mixture over a metathesis catalyst to prepare a C4-8-olefin mixture comprising 2-pentene, and optional removal of the C4-8-olefin mixture, b) removal of from 5 to 100% of the 2-pentene present in stage a) and subsequent reaction over an isomerization catalyst to give a mixture of 2-pentene and 1-pentene which is returned to stage a), c) dimerization of the C4-8-olefin mixture obtained in stage b) following removal in the presence of a dimerization catalyst to give a mixture containing C8-16-olefins, removal of these C8-16-olefins and optional removal of a partial stream thereof, d) reaction of the c8-16-olefin mixtures obtained in stage c) or of the partial stream with an aromatic hydrocarbon in the presence of an alkylation catalyst to form alkyl aromatic compounds where, prior to the reaction, 0 to 60% by weight, based on the c8-16-olefin mixtures obtained in stage c), of linear olefins may additionally be added, e) optional sulfonation of the alkyl aromatic compounds obtained in stage d) and neutralization to give alkylarylsulfonates, where, prior to the sulfonation, 0 to 60% by weight, based on the alkyl aromatic compounds obtained in stage d), of linear alkylbenzenes may additionally be added if no admixing has taken place in stage d), f) optional mixing of the alkylarylsulfonates obtained in stage e) with 0 to 60% by weight, based on the alkylarylsulfonates obtained in stage e), of linear alkylarylsulfonate, if no admixing has taken place in stages d) and e).
    • 烷基芳基化合物的制备通过以下步骤进行:a)在复分解催化剂上使C 4-14 C 5 -C 5 - 烯烃混合物反应以制备C 4-8 - 其包含2-戊烯,任选地除去C 4-18α-烯烃混合物,b)除去在步骤a)中存在的5-100%的2-戊烯, 并随后在异构化催化剂上反应,得到2-戊烯和1-戊烯的混合物,将其返回到a)步骤,c)在步骤b中获得的C 4-18α-烯烃混合物的二聚反应 ),在二聚催化剂存在下除去,得到含有C 8-16 - 烯烃的混合物,除去这些C 8-16 - 烯烃并任选地除去 其部分流,d)在烷基化催化剂存在下,将阶段c)或部分流中获得的C 8-16 - α-烯烃混合物与芳族烃反应,形成烷基芳族化合物,其中 在反应之前,0至60重量%,b 在阶段c)中得到的C 8-16α-烯烃混合物中,可以另外加入线性烯烃,e)任选的在步骤d)中获得的烷基芳族化合物磺化,中和得到烷基芳基磺酸盐 ,其中在磺化之前,如果在步骤d)中没有混合,则可以另外加入基于直链烷基苯中得到的直链烷基苯0至60重量%,f)任选混合 如果在阶段d)和e)中没有混合,则在阶段e)中获得的烷基芳基磺酸盐以0至60重量%的量计,基于阶段e)中得到的烷基芳基磺酸盐,为直链烷基芳基磺酸盐。
    • 58. 发明授权
    • Method for the operation of a fuel metering system on a direct injection internal combustion engine
    • 在直喷式内燃机上运行燃料计量系统的方法
    • US06823844B2
    • 2004-11-30
    • US10030634
    • 2002-06-04
    • Ulrich SteinbrennerKlaus JoosThomas Frenz
    • Ulrich SteinbrennerKlaus JoosThomas Frenz
    • F02M3704
    • F02M63/0295F02D41/3836F02M63/0225
    • The present invention relates to a method for operating a fuel metering system (11) of a direct-injection internal combustion engine, having a fuel supply container, at least one prefeed pump a high-pressure pump assembly having at least two high-pressure pumps for pumping fuel out of the low-pressure region into at least one high-pressure reservoir, a control unit for regulating an injection pressure prevailing in the high-pressure reservoir, and having fuel injection valves for injecting fuel out of the high-pressure reservoir into combustion chambers of the engine. In order especially in engines with large displacement and in engines with more than four cylinders to assure reliable supply of fuel to the combustion chambers, it is proposed that the fuel metering system has one fuel circuit for metering fuel into all the combustion chambers of the engine, and all the high-pressure pumps are disposed in the fuel circuit, and that all the high-pressure pumps are triggered independently of one another via a common pressure regulating circuit.
    • 本发明涉及一种用于操作直喷式内燃机的燃料计量系统(11)的方法,所述直喷式内燃机具有燃料供应容器,至少一个预制泵,具有至少两个高压泵的高压泵组件 用于将燃料从低压区域排出到至少一个高压储存器中;控制单元,用于调节高压储存器中的注入压力,并具有用于将燃料喷射出高压储存器的燃料喷射阀 进入发动机的燃烧室。 特别是在具有大排量的发动机和具有多于四个气缸的发动机中以确保燃料到燃烧室的可靠供应的情况下,建议燃料计量系统具有用于将燃料计量到发动机的所有燃烧室中的一个燃料回路 并且所有高压泵都设置在燃料回路中,并且所有高压泵通过公共压力调节电路彼此独立地被触发。
    • 59. 发明授权
    • Method for the single-step production of polytetrahydrofuran and tetrahydrofuran copolymers
    • 单步生产聚四氢呋喃和四氢呋喃共聚物的方法
    • US06716937B2
    • 2004-04-06
    • US10312851
    • 2003-01-02
    • Gerd BohnerThomas DomschkeRolf-Hartmuth FischerMartin HaubnerChristoph SigwartUlrich SteinbrennerChristian Tragut
    • Gerd BohnerThomas DomschkeRolf-Hartmuth FischerMartin HaubnerChristoph SigwartUlrich SteinbrennerChristian Tragut
    • C08F244
    • C08G65/30C08G65/20
    • A process for the single-stage preparation of polytetrahydrofuran and/or tetrahydrofuran copolymers having a mean molecular weight of from 650 to 5000 dalton by polymerization of tetrahydrofuran over a heterogeneous acid catalyst in the presence of at least one telogen and/or comonomer selected from the group consisting of alpha,omega-diols, water, polytetrahydrofuran having a molecular weight of from 200 to 700 dalton and cyclic ethers comprises a) separating off the catalyst and/or downstream products of the catalyst suspended and/or dissolved in the output from the polymerization, b) fractionating the resulting catalyst-free output from the polymerization in at least one distillation step to give a distillation residue comprising the polymerization product and at least one tetrahydrofuran fraction and returning at least part of the tetrahydrofuran fraction to the polymerization and c) separating low molecular weight polytetrahydrofuran and/or tetrahydrofuran copolymers having a mean molecular weight of from 200 to 700 dalton from the distillation residue from work-up step b) and isolating polytetrahydrofuran and/or tetrahydrofuran copolymers having a mean molecular weight of from 650 to 5000 dalton.
    • 一种通过在多相酸催化剂的存在下,在四氢呋喃和/或共聚单体的存在下,通过四氢呋喃聚合,单分级制备平均分子量为650-5000道尔顿的聚四氢呋喃和/或四氢呋喃共聚物的方法,该共聚单体选自 由α,ω-二醇,水,分子量为200至700道尔顿的聚四氢呋喃和环醚组成的组包括:a)将催化剂和/或催化剂的下游产物分离出悬浮和/或溶解在聚合物的输出中 b)在至少一个蒸馏步骤中将所得无催化剂的产物从聚合中分馏,得到包含聚合产物和至少一种四氢呋喃馏分的蒸馏残余物,并将至少部分四氢呋喃馏分返回到聚合反应中, 分子量的四氢呋喃和/或四氢呋喃共聚物 来自后处理步骤b)的蒸馏残余物的200至700道尔顿的颗粒重量,并分离平均分子量为650-5000道尔顿的聚四氢呋喃和/或四氢呋喃共聚物。