Top speed limiter for an internal combustion engine
    51.
    发明授权
    Top speed limiter for an internal combustion engine 失效
    内燃机的最高限速器

    公开(公告)号:US4375207A

    公开(公告)日:1983-03-01

    申请号:US179184

    申请日:1980-08-18

    CPC分类号: G05D13/04 F02D31/009

    摘要: The maximum speed in an internal combustion engine is limited by circuitry which can be adjusted to conditions requiring a lower-than-normal top speed, for example during initial delivery to the customer and during the break-in period of the engine. The top speed limiter includes a comparator for suppressing or altering the fuel injection pulses. As a feature of the invention, the reference signal applied to the comparator and representing the top engine speed can be changed either manually or on the basis of elapsed time or mileage.

    摘要翻译: 内燃机中的最大速度受电路的限制,该电路可以被调节到需要低于正常最高速度的条件,例如在初始传送给客户期间以及在发动机的进入期间。 最高限速器包括用于抑制或改变燃料喷射脉冲的比较器。 作为本发明的特征,施加到比较器并且表示顶部发动机转速的参考信号可以手动地或者基于经过的时间或里程来改变。

    Method for producing alkyl aromatic compounds
    54.
    发明授权
    Method for producing alkyl aromatic compounds 失效
    烷基芳族化合物的制备方法

    公开(公告)号:US07652183B2

    公开(公告)日:2010-01-26

    申请号:US10552434

    申请日:2004-04-14

    IPC分类号: C07C2/66

    摘要: In a process for the preparation of alkylaromatic compounds by reacting C3-30-olefins, or alcohols from which C3-30-olefins are formed under the reaction conditions, with an aromatic hydrocarbon in the presence of an alkylation catalyst, the reaction is carried out in a reactor cascade of at least two reactors, where each of the reactors comprises the alkylation catalyst, at least 80% of the aromatic hydrocarbon are fed into the first reactor of the reactor cascade, and at least 40% of the olefins are intermediately fed in after the first reactor.

    摘要翻译: 在烷基芳族化合物的制备方法中,在烷基化催化剂的存在下,使C3-30-烯烃或在反应条件下由C 3-30-烯烃形成的醇与芳烃反应,进行反应 在至少两个反应器的反应器级联中,其中每个反应器包含烷基化催化剂,至少80%的芳族烃进料到反应器级联的第一反应器中,并且至少40%的烯烃被中间进料 在第一反应堆之后。

    Method for producing alkylaryl compounds
    56.
    发明申请
    Method for producing alkylaryl compounds 审中-公开
    烷基芳基化合物的制备方法

    公开(公告)号:US20070142258A1

    公开(公告)日:2007-06-21

    申请号:US10583140

    申请日:2004-12-17

    IPC分类号: C09D9/00

    摘要: 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).

    摘要翻译: 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。

    Method for the single-step production of polytetrahydrofuran and tetrahydrofuran copolymers
    59.
    发明授权
    Method for the single-step production of polytetrahydrofuran and tetrahydrofuran copolymers 失效
    单步生产聚四氢呋喃和四氢呋喃共聚物的方法

    公开(公告)号:US06716937B2

    公开(公告)日:2004-04-06

    申请号:US10312851

    申请日:2003-01-02

    IPC分类号: C08F244

    CPC分类号: C08G65/30 C08G65/20

    摘要: 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.

    摘要翻译: 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。