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    Joint separation of acetylene and ethylene from cracked gases
    2.
    发明授权
    Joint separation of acetylene and ethylene from cracked gases 失效
    乙烯和乙烯从裂缝气体的联合分离

    公开(公告)号：US3635038A

    公开(公告)日：1972-01-18

    申请号：US3635038D

    申请日：1969-05-16

    Applicant: BASF AG

    Inventor： NAGEL OTTO ,  PLATZ ROLF ,  TAGLIEBER KURT ,  WEINFURTER KURT ,  WOLF DIETER

    IPC: C07C7/00 ,  F25J3/02 ,  F25J1/00 ,  F25J3/00

    CPC classification number: F25J3/0271 ,  C07C7/005 ,  F25J3/0219 ,  F25J3/0238 ,  F25J3/0242 ,  F25J2200/74 ,  F25J2205/04 ,  F25J2205/50 ,  F25J2210/12 ,  F25J2215/62 ,  F25J2245/02 ,  F25J2270/04 ,  F25J2270/12 ,  C07C11/24

    Abstract: A gas mixture (obtained by thermal cracking of hydrocarbons followed by quenching of the cracked gas and freed from carbon dioxide and water) is separated into a gas mixture containing hydrogen, carbon monoxide and methane and another gas mixture containing ethylene, acetylene and higher hydrocarbons by (a) cooling the gas mixture which is at superatmospheric pressure in at least one condensation stage to a temperature which is above the solidification temperature of acetylene mixed with the other condensed constituents, (b) separating the condensate thus obtained and subdividing it in a rectifying column into a first mixture containing C2 hydrocarbons and a second mixture containing C3 and higher hydrocarbons, and (c) freeing the residual gas remaining from (a) from residual acetylene and ethylene in a scrubber by treatment with some of the mixture consisting of C3 and higher hydrocarbons from (b).

    Abstract translation: 将气体混合物（通过烃的热裂化，然后淬灭裂化气体并从二氧化碳和水中除去）分离成含有氢气，一氧化碳和甲烷的气体混合物，以及含有乙烯，乙炔和高级烃的另一气体混合物 （a）在至少一个冷凝阶段将高于大气压的气体混合物冷却至高于其他冷凝组分混合的乙炔凝固温度的温度，（b）将由此获得的冷凝物分离，并将其细分为精馏 塔进入含有C 2烃和含有C 3和更高级烃的第二混合物的第一混合物，和（c）通过用一些由C 3和C 3组成的混合物处理将来自（a）残留的残余气体从残留的乙炔和乙烯中释出的第一混合物 （b）的高级烃。

    Production of pigmented resin powders
    3.
    发明授权
    Production of pigmented resin powders 失效
    着色树脂粉的生产

    公开(公告)号：US3879335A

    公开(公告)日：1975-04-22

    申请号：US28026272

    申请日：1972-08-14

    Applicant: BASF AG

    Inventor： STORCK GERHARD ,  DIEFENBACH HORST ,  MARX MATTHIAS ,  NAGEL OTTO ,  KUERTEN HERIBERT ,  WEINLE WERNER

    IPC: C08J3/12 ,  C09B63/00 ,  C09B67/00 ,  C09B67/06 ,  C09D5/03 ,  C08F45/06 ,  C08G51/04

    CPC classification number: C09D5/03 ,  C09B63/00 ,  C09B67/0003 ,  C09B67/0095

    Abstract: Production of pigmented resin powders by finely dispersing dispersions of pigments in solutions of polymeric materials in at least one organic solvent in water containing a protective colloid while supplying mixing energy, and removing the solvent. A preferred method is to introduce one or more jets of water containing protective colloid at the rate of 5 to 100 m/sec into animpulse exchange chamber together with the dispersion issuing in the immediate vicinity of the orifice(s), and to remove the solvent. The method avoids crosslinking and provides pigmented resin powders of consistently reproducible color which are suitable for conventional powdered-resin coating methods.

    Abstract translation: 通过将颜料的分散体在含有保护胶体的水中的至少一种有机溶剂中精细分散在聚合物材料的溶液中同时提供混合能量并除去溶剂来生产着色树脂粉末。 一种优选的方法是将一种或多种含有保护胶体的水，以5-100m / sec的速率引入到脉冲交换室中，同时在紧邻孔口处发出分散体，并除去溶剂 。 该方法避免交联，并提供适合于常规粉末 - 树脂涂覆方法的颜色一致的可再现颜色的着色树脂粉末。

    Production of alkynols and alkynediols
    5.
    发明授权
    Production of alkynols and alkynediols 失效
    生产烷基醇和烷基二醇

    公开(公告)号：US3723545A

    公开(公告)日：1973-03-27

    申请号：US921170

    申请日：1970-02-06

    Applicant: BASF AG

    Inventor： NAGEL OTTO ,  PLATZ ROLF ,  FUCHS WERNER

    IPC: B01J10/00 ,  B01J31/00 ,  C07B61/00 ,  C07C27/00 ,  C07C29/42 ,  C07C33/04 ,  C07C33/046 ,  C07C33/28 ,  C07C67/00 ,  C07C33/06

    CPC classification number: C07C29/42 ,  C07C33/046 ,  Y10S261/75

    Abstract: Production of alkynols and/or alkynediols by reaction of acetylene with aldehydes in a liquid reaction medium in the presence of a heavy metal acetylide as catalyst and in the presence or absence of basic reagents, at least one of the starting materials being introduced in gaseous form. The catalyst is suspended in the liquid medium and during the reaction a portion of the reaction medium is withdrawn and returned at the entry point below the level of the liquid of the gaseous starting material(s) at a speed of 5 to 100 meters per second into the reaction medium and is introduced into a chamber (located in the reaction medium and extending in the direction of the liquid returned) whose inlet opening has a mean diameter from twice to twenty times the mean diameter of the liquid nozzle and whose length is three to thirty times ints hydraulic diameter. The products are important intermediates for example for the production of solvents or may be used in electrolytic baths.

    Abstract translation: 在重金属乙炔化物作为催化剂的存在下，在液态反应介质中，乙炔与醛反应生成炔烃和/或炔二醇，在碱性试剂存在或不存在下，至少一种原料以气态形式引入 。 催化剂悬浮在液体介质中，并且在反应期间，反应介质的一部分以5至100米/秒的速度在气态起始材料液体的入口点下方返回 进入反应介质并引入到入口开口的平均直径为液体喷嘴的平均直径的二倍至二十倍的室（位于反应介质中并沿着返回的液体的方向延伸），其长度为三 至30倍液压直径。 该产品是重要的中间体，例如用于生产溶剂或可用于电解池。

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