Process for separating butanol and dibutyl ether by means of
dual-pressure distillation
    21.
    发明授权
    Process for separating butanol and dibutyl ether by means of dual-pressure distillation 失效
    通过双压蒸馏分离丁醇和二丁醚的方法

    公开(公告)号:US5985100A

    公开(公告)日:1999-11-16

    申请号:US11700

    申请日:1998-02-17

    CPC classification number: C07C41/42 C07C29/80 Y10S203/20

    Abstract: Butanol and dibutyl ether are separated from a mixture containing water, dibutyl ether and n-butanol, 2-butanol and/or isobutanol by a process in whicha) the mixture is introduced into a first distillation column, essentially butanol is separated off at the bottom of this distillation column and the mixture taken off at the top of the distillation columnb) is introduced into a second distillation column and essentially dibutyl ether is separated off at the bottom of this second distillation column and the mixture formed at the top of the second distillation column is removed,c) the second distillation column being operated at a higher pressure than the first distillation column and at least one of the two mixtures taken off via the top of the distillation columns being subjected to phase separation, only the organic phase separated off being fed to the second distillation column in the case of phase separation downstream of the first distillation column, and separation into an aqueous and an organic phase also being effected in the case of phase separation downstream of the second distillation column, a part stream being recycled from the top or rectification section of the second distillation column to the first distillation column.

    Abstract translation: PCT No.PCT / EP96 / 03762 Sec。 371日期1998年2月17日 102(e)1998年2月17日PCT 1995年8月26日PCT PCT。 公开号WO97 / 08120 日期1997年3月6日丁醇和二丁醚由含有水,二丁醚和正丁醇,2-丁醇和/或异丁醇的混合物分离,其中a)将混合物引入第一蒸馏塔,基本上为丁醇 在该蒸馏塔的底部分离,将在蒸馏塔b)顶部排出的混合物引入第二蒸馏塔中,并且在该第二蒸馏塔的底部基本上分离出二丁基醚,并形成混合物 在第二蒸馏塔的顶部被除去,c)第二蒸馏塔在比第一蒸馏塔高的压力下操作,并且通过蒸馏塔的顶部排出的两种混合物中的至少一种经受相分离 在第一蒸馏塔下游相分离的情况下,仅分离出分离的有机相进入第二蒸馏塔,分离 在第二蒸馏塔下游的相分离的情况下也进行水和有机相的离子化,将一部分物流从第二蒸馏塔的顶部或精馏段再循环到第一蒸馏塔。

    Separation of ortho-, meta- and para-tolunitrile from ternary mixtures
of the isomers
    22.
    发明授权
    Separation of ortho-, meta- and para-tolunitrile from ternary mixtures of the isomers 失效
    从异构体的三元混合物中分离出邻位,间位和对 - 甲苯腈

    公开(公告)号:US5002639A

    公开(公告)日:1991-03-26

    申请号:US566677

    申请日:1990-08-13

    CPC classification number: C07C253/34

    Abstract: A process for the separation of ortho-, meta- and para-tolunitrile from ternary mixtures of isomers entails removing ortho-tolunitrile from these mixtures by distillation under pressures of from 10.sup.2 and 10.sup.5 Pa and with a reflux ratio of from 1:1 to 200:1, and distilling the remaining binary mixture of meta- and para-tolunitrile to concentrate to more than 75 mol-% para-tolunitrile, and freezing out the paratolunitrile at below 26.degree. C., and a process for the preparation of suitable ternary mixtures of isomers entails isomerization of pure ortho-, meta- or para-tolunitrile or mixtures thereof at from 380.degree. to 580.degree. C. on zeolite catalysts.

    Abstract translation: 从异构体的三元混合物中分离原始,间位和对 - 仲腈的方法需要通过在102和105Pa的压力下回流,从1:1至200的回流比从这些混合物中除去邻 - :1,并蒸馏剩余的元 - 和对 - 仲腈的二元混合物以浓缩至大于75mol%的对 - 仲腈,并在低于26℃下冷冻副产物腈,以及制备合适的三元 异构体的混合物需要在380-580℃下对沸石催化剂上的纯邻位,间位或对 - 甲苯腈或其混合物异构化。

    PLANETARY ROLLER EXTRUDER
    23.
    发明申请

    公开(公告)号:US20180281263A1

    公开(公告)日:2018-10-04

    申请号:US15935206

    申请日:2018-03-26

    Applicant: Harald RUST

    Inventor: Harald RUST

    Abstract: A planetary roller extruder. The abstract of the disclosure is submitted herewith as required by 37 C.F.R. § 1.72(b). As stated in 37 C.F.R. § 1.72(b): A brief abstract of the technical disclosure in the specification must commence on a separate sheet, preferably following the claims, under the heading “Abstract of the Disclosure.” The purpose of the abstract is to enable the Patent and Trademark Office and the public generally to determine quickly from a cursory inspection the nature and gist of the technical disclosure. The abstract shall not be used for interpreting the scope of the claims. Therefore, any statements made relating to the abstract are not intended to limit the claims in any manner and should not be interpreted as limiting the claims in any manner.

    Non-chemical, mechanical procedure for the devulcanization of scrap rubber and/or elastomers and apparatus therefor
    24.
    发明授权
    Non-chemical, mechanical procedure for the devulcanization of scrap rubber and/or elastomers and apparatus therefor 有权
    用于废橡胶和/或弹性体的脱硫的非化学,机械方法及其设备

    公开(公告)号:US08957119B2

    公开(公告)日:2015-02-17

    申请号:US13558880

    申请日:2012-07-26

    Applicant: Harald Rust

    Inventor: Harald Rust

    Abstract: Method of devulcanizing rubber and/or elastomers without the need for a chemical agent, in which method the vulcanized rubber and/or elastomers are fed into a planetary roller extruder, which planetary roller extruder has a housing, a central spindle, two groups of planetary roller spindles, and a dispersion ring disposed about the central spindle and between the two groups of planetary spindles. Mechanical and thermal stress is generated on the vulcanized rubber and/or elastomers by kneading and/or crushing the vulcanized rubber and/or elastomers using the central spindle and the planetary spindles, and by forcing the vulcanized rubber and/or elastomers through the dispersion ring, which is designated to substantially restrict passage of the vulcanized rubber and/or elastomers therethrough. The mechanical and thermal stress alone is sufficient to break or destroy the molecular chains or bonds of the vulcanized rubber and/or elastomers.

    Abstract translation: 将橡胶和/或弹性体脱硫而不需要化学试剂的方法,其中将硫化橡胶和/或弹性体进料到行星辊挤出机中,该行星辊式挤出机具有壳体,中心心轴,两组行星 辊心轴,以及围绕中心心轴和两组行星主轴之间布置的分散环。 在硫化橡胶和/或弹性体上通过使用中心心轴和行星心轴捏合和/或破碎硫化橡胶和/或弹性体并通过迫使硫化橡胶和/或弹性体通过分散环产生机械和热应力 ,其被指定为基本上限制硫化橡胶和/或弹性体通过其的通道。 单独的机械和热应力足以破坏或破坏硫化橡胶和/或弹性体的分子链或键。

    Dividing wall column
    26.
    发明授权
    Dividing wall column 失效
    分隔墙柱

    公开(公告)号:US06958111B2

    公开(公告)日:2005-10-25

    申请号:US09847299

    申请日:2001-05-03

    CPC classification number: B01D3/141 B01D3/146

    Abstract: In a dividing wall column comprising as segments a) an upper column region (6), b) an inflow section (7), c) an offtake section (8) and d) a lower column region (9), the inflow section b) (7) and the offtake section c) (8) are separated from one another laterally by a dividing wall (10) fixed in the column and the dividing wall (10) is located between the upper column region a) (6) and the lower column region d) (9). The present invention provides for the dividing wall (10) to be constructed at least partly of an elastic material, the dividing wall (10) to have a slightly overdimensional width and the dividing wall (10) to be fixed in the column by the dividing wall exercising an elastic recovery force on the interior wall of the column. The dividing wall can easily be installed in, in particular, relatively small columns.

    Abstract translation: 在分隔壁柱中,包括a)上列区域(6),b)流入部分(7),c)脱出部分(8)和d)下部列区域(9),流入部分b )(7)和收拢部分c)(8)通过固定在塔中的分隔壁(10)横向隔开,分隔壁(10)位于上列区域a)(6)和 下列区域d)(9)。 本发明提供了至少部分地由弹性材料构成的分隔壁(10),该分隔壁(10)具有稍微过度的宽度,并且该分隔壁(10)通过分开固定在该塔中 墙壁在柱的内壁上弹性恢复力。 分隔壁可以容易地安装在特别是相对较小的柱中。

    Method for the production of cyclohexanol from benzene
    28.
    发明授权
    Method for the production of cyclohexanol from benzene 失效
    从苯生产环己醇的方法

    公开(公告)号:US06943274B2

    公开(公告)日:2005-09-13

    申请号:US10505705

    申请日:2003-02-28

    CPC classification number: C07C29/04 C07C2601/14 C07C35/08

    Abstract: A process for preparing cyclohexanol from benzene by: a) preparing cyclohexene by hydrogenating benzene in the presence of a catalyst, and b) preparing cyclohexanol by hydrating the cyclohexene in the presence of a catalyst, comprises: carrying out steps a) and b) in a reaction facility which has a bottom region at the lower end, a top region at the upper end, and a reaction zone between the top region and the bottom region which contains the catalyst according to steps a) and b), evaporating a portion of the benzene using the heat of reaction in the reaction zone, condensing it in the top region and returning it to the reaction zone, and withdrawing a reaction mixture containing cyclohexanol in the bottom region.

    Abstract translation: 一种通过以下步骤由苯制备环己醇的方法:a)在催化剂存在下,通过氢化苯来制备环己烯,和b)通过在催化剂存在下使环己烯水合制备环己醇,包括:进行步骤a)和b) 具有下端的底部区域,上端的顶部区域和顶部区域和底部区域之间的反应区域的反应设备,其包含根据步骤a)和b)的催化剂,蒸发一部分 苯在反应区中使用反应热,在顶部区域冷凝并将其返回到反应区,并在底部区域中抽出含有环己醇的反应混合物。

    Preparation of 1,3-diols
    29.
    发明授权
    Preparation of 1,3-diols 失效
    1,3-二醇的制备

    公开(公告)号:US06380443B1

    公开(公告)日:2002-04-30

    申请号:US09677862

    申请日:2000-10-03

    Abstract: A process for preparing 1,3-diols having 6 or more carbon atoms comprises a) provision of at least one alkanal having at least three carbon atoms; b) thermal treatment of the alkanal in the absence of a basic catalyst; c) hydrogenation of the aldol addition product formed in step b); and d) isolation of the 1,3-diol obtained. The process of the present invention makes it possible to prepare 1,3-diols simply and inexpensively.

    Abstract translation: 制备具有6个或更多个碳原子的1,3-二醇的方法包括:a)提供至少一种具有至少三个碳原子的链烷烃; b)在没有碱性催化剂的情况下热处理链烷烃; c)步骤b)中形成的醛醇加成产物的氢化; 和d)所获得的1,3-二醇的分离。本发明的方法使得可以简单且廉价地制备1,3-二醇。

    Isolation of &agr;-ethynyl carbinols by distillation
    30.
    发明授权
    Isolation of &agr;-ethynyl carbinols by distillation 失效
    通过蒸馏分离α-乙炔基甲醇

    公开(公告)号:US06316680B1

    公开(公告)日:2001-11-13

    申请号:US09455161

    申请日:1999-12-06

    CPC classification number: C07C29/80 C07C33/042 C07C33/048

    Abstract: In a process for isolating &agr;-ethynyl carbinols from the liquid reaction mixture from the addition of acetylene onto &agr;,&bgr;-unsaturated carbonyl compounds by distillation, the distillation is carried out continuously, the feed stream is introduced into the middle section of a distillation column (K), the major part of the water is distilled off azeotropically together with the solvent at the top of the column, and the &agr;-ethynyl carbinol target product is taken off below the feed point to the column.

    Abstract translation: 在通过蒸馏从乙炔加入到α,β-不饱和羰基化合物中的液体反应混合物中分离α-乙炔基甲醇的方法中,蒸馏连续进行,将进料流引入蒸馏塔的中间部分 (K)中,将大部分水与塔顶部的溶剂一起共沸蒸馏,并将α-乙炔基甲醇目标产物从柱的进料点以下取出。

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