Apparatus for bringing liquids in contact
    1.
    发明授权
    Apparatus for bringing liquids in contact 失效
    使液体接触的装置

    公开(公告)号:US4377344A

    公开(公告)日:1983-03-22

    申请号:US94803

    申请日:1979-11-15

    摘要: There is provided an apparatus for bringing into contact liquids at least one of which is viscous, the apparatus consisting essentially of a tubular container, a first nozzle from introducing a liquid in the upper portion of the container, at least one other nozzle lower than the first nozzle for introducing a different liquid, the tubular container being closeable at the tap thereof and downward from said other nozzle being constricted breast shaped to form a discharge opening, said other nozzles are preferably of polished steel, said other nozzles consist essentially of at least one tangential spray means arranged in at least one row, said other nozzles being slightly above said constriction and being directed in the direction of the upper closeable device or said first nozzle and wherein the discharge opening can discharge into another container which is permanently or detachably connected to the tubular container, said further container can be provided with means for establishing reduced pressure or superatmospheric pressure.

    摘要翻译: 提供了一种用于使其至少一个粘性的接触液体的装置,该装置基本上由管状容器组成,第一喷嘴从容器的上部引入液体,至少另一个喷嘴低于 用于引入不同液体的第一喷嘴,所述管状容器在其龙头处可封闭并且从所述另一个喷嘴向下收缩成乳房形状以形成排出口,所述其它喷嘴优选为抛光钢,所述其它喷嘴至少基本上由 一个切向喷雾装置设置在至少一排中,所述其它喷嘴略微高于所述收缩部分并且被引向所述上部可关闭装置或所述第一喷嘴的方向,并且其中所述排放口可以排放到永久地或可分离地连接的另一个容器中 所述另外的容器可以设置有用于建立r的装置 压力或超大气压。

    Process for bringing liquids into contact
    2.
    发明授权
    Process for bringing liquids into contact 失效
    使液体接触的过程

    公开(公告)号:US4413021A

    公开(公告)日:1983-11-01

    申请号:US408923

    申请日:1982-08-17

    摘要: There is provided an apparatus for bringing into contact liquids at least one of which is viscous, the apparatus consisting essentially of a tubular container, a first nozzle from introducing a liquid in the upper portion of the container, at least one other nozzle lower than the first nozzle for introducing a different liquid, the tubular container being closeable at the tap thereof and downward from said other nozzle being constricted breast shaped to form a discharge opening, said other nozzles are preferably of polished steel, said other nozzles consist essentially of at least one tangential spray means arranged in at least one row, said other nozzles being slightly above said constriction and being directed in the direction of the upper closeable device or said first nozzle and wherein the discharge opening can discharge into another container which is permanently or detachably connected to the tubular container, said further container can be provided with means for establishing reduced pressure or superatmospheric pressure.

    摘要翻译: 提供了一种用于使其至少一个粘性的接触液体的装置,该装置基本上由管状容器组成,第一喷嘴从容器的上部引入液体,至少另一个喷嘴低于 用于引入不同液体的第一喷嘴,所述管状容器在其龙头处可封闭并且从所述另一个喷嘴向下收缩成乳房形状以形成排出口,所述其它喷嘴优选为抛光钢,所述其它喷嘴至少基本上由 一个切向喷雾装置设置在至少一排中,所述其它喷嘴略微高于所述收缩部分并且被引向所述上部可关闭装置或所述第一喷嘴的方向,并且其中所述排放口可以排放到永久地或可分离地连接的另一个容器中 所述另外的容器可以设置有用于建立r的装置 压力或超大气压。

    Process for the production of suspension or solution of cyanuric
chloride in organic solvents (II)
    3.
    发明授权
    Process for the production of suspension or solution of cyanuric chloride in organic solvents (II) 失效
    生产氰尿酰氯悬浮液或有机溶剂溶液的方法(二)

    公开(公告)号:US4269979A

    公开(公告)日:1981-05-26

    申请号:US94874

    申请日:1979-11-16

    摘要: Finely divided suspensions of cyanuric chloride in organic solvents which are practically water free are prepared at high mixing velocities and low temperatures by introducing liquid cyanuric chloride through a nozzle in the upper portion of the mixing apparatus in countercurrent flow to upwardly flowing solvent introduced from at least one lower nozzle above a breast shaped constriction in the lower open portion of the apparatus. In this way the chamber walls are always covered with an unbroken layer of liquid. The process can be carried out at normal, reduced or elevated pressure. At reduced pressure by evaporation of the solvent there is simultaneously a cooling of the system.

    摘要翻译: 通过在混合装置的上部通过喷嘴将液体氰尿酰氯引入到至少从上至下引入的向上流动的溶剂的逆流中,以高混合速度和低温制备几乎不含水的有机溶剂中的氰尿酰氯悬浮液 在设备的下部开口部分的乳房形收缩部之上的一个下部喷嘴。 以这种方式,室壁总是被不间断的液体覆盖。 该方法可以在正常的,降低的或升高的压力下进行。 在减少溶剂蒸发的同时,同时冷却系统。

    Process for the production of suspension or solutions of cyanuric
chloride in organic solvents (I)
    4.
    发明授权
    Process for the production of suspension or solutions of cyanuric chloride in organic solvents (I) 失效
    用于生产氰尿酰氯在有机溶剂中的悬浮液或溶液的方法(I)

    公开(公告)号:US4271297A

    公开(公告)日:1981-06-02

    申请号:US94872

    申请日:1979-11-16

    摘要: Suspension or solutions of cyanuric chloride in water containing organic solvents are prepared at high mixing velocities and low temperatures with resulting low degree of hydrolysis by introducing liquid cyanuric chloride through a nozzle in the upper portion of the mixing apparatus in countercurrent flow to upwardly flowing solvent introduced from at least one lower nozzle above a breast shaped constriction in the lower, open portion of the apparatus. In this way the chamber walls are always covered with an unbroken layer of liquid. The process can be carried out at normal, reduced or elevated pressure. At reduced pressure by evaporation of the solvent there is simultaneously a cooling of the system.

    摘要翻译: 在高混合速度和低温下制备氰尿酰氯悬浮液或溶液,并通过在混合装置的上部引入液态氰尿酰氯通过向上流动的溶剂的逆向流动引入液体氰尿酰氯,从而导致低水解度 从装置的下部开放部分中的乳房形收缩件上方的至少一个下部喷嘴。 以这种方式,室壁总是被不间断的液体覆盖。 该方法可以在正常的,降低的或升高的压力下进行。 在减少溶剂蒸发的同时,同时冷却系统。

    Process for the production of solutions or suspensions of cyanuric
chloride in aqueous organic solvents
    5.
    发明授权
    Process for the production of solutions or suspensions of cyanuric chloride in aqueous organic solvents 失效
    用于生产氰尿酰氯在含水有机溶剂中的溶液或悬浮液的方法

    公开(公告)号:US4017413A

    公开(公告)日:1977-04-12

    申请号:US632952

    申请日:1975-11-18

    IPC分类号: C07D251/28 B01F3/08

    CPC分类号: C07D251/28

    摘要: There is provided a process for the production of a solution or suspension of cyanuric chloride in a water containing organic solvent wherein the liquid cyanuric chloride and the organic-aqueous solvent are mixed together while being agitated, the liquid cyanuric chloride at a temperature between its melting point and 200.degree. C. is led into the flowing organic-aqueous solvent with a velocity of Vcy (in kg per hour) wherein ##EQU1## where P is the desired concentration of cyanuric chloride in the solution or suspension to be produced in weight %, P.sub.LM is the concentration of cyanuric chloride in the solvent used which also includes O,V.sub.lm is the velocity of the solvent added in kg/h,And P.sub.LM, V.sub.LM and T.sub.LM, the temperature of the added solvent, are so selected that the expression ##EQU2## does not exceed the boiling temperature in .degree. C. of the solvent used and wherein C.sub.p (LM) and C.sub.p (Cy) signify the specific heat capacities in cal. x g.sup.-.sup.1 .times. (.degree.degree C).sup.-.sup.1 of the solvent and cyanuric chloride respectively, whereupon in a given case within at most 3 minutes after bringing the cyanuric chloride and solvent into contact the flowing mixture is cooled to the desired storage temperature.

    摘要翻译: 提供了一种在含有有机溶剂的水中制备氰尿酰氯的溶液或悬浮液的方法,其中液体氰尿酰氯和有机 - 水溶剂在搅拌下混合在一起,液态氰尿酰氯在其熔融 点和200℃以Vcy速度(以kg /小时计)流入有机 - 水溶剂,其中P是待生成的溶液或悬浮液中所需浓度的氰尿酰氯,其重量% PLM是所用溶剂中氰尿酰氯的浓度,其还包括O,VLM是以kg / h加入的溶剂的速度,而PLM,VLM和TLM,加入的溶剂的温度如此选择,使得表达式 &lt; IMAGE&gt;不超过使用的溶剂的沸点(℃),其中Cp(LM)和Cp(Cy)表示比热容。 xg <1>(℃C)-1的溶剂和氰尿酰氯,因此在给出的情况下,在将氰尿酰氯和溶剂接触之前的最多3分钟内,将流动的混合物冷却至所需的 储存温度。

    Preparation of .epsilon.-caprolactone
    6.
    发明授权
    Preparation of .epsilon.-caprolactone 失效
    ε-己内酯的制备

    公开(公告)号:US4341709A

    公开(公告)日:1982-07-27

    申请号:US150260

    申请日:1980-05-15

    CPC分类号: C07D315/00

    摘要: A process for the preparation of .epsilon.-caprolactone comprising:(a) reacting cyclohexanone with a solution of perpropionic acid in an organic solvent at a molar ratio of cyclohexanone;perpropionic acid of about 1.1-5:1 at a temperature of about 10.degree. to 80.degree. C. to form a reaction mixture consisting essentially of .epsilon.-caprolactone, propionic acid and organic solvent,(b) distilling the reaction mixture from (a) in a first distillation unit to obtain a distillate comprising the organic solvent and a distillation residue,(c) introducing the distillation residue from (b) at a point into a second distillation unit to obtain a distillate comprising propionic acid and unreacted cyclohexanone, removing from the second distillation unit, separately from one another and at a point below the point of introduction into the second distillation unit, .epsilon.-caprolactone and any high-boiling constituents, and,(d) distilling in a third distillation unit the distillate from (c) to obtain a distillate consisting essentially of propionic acid and a distillation residue comprising a mixture of propionic acid and cyclohexanone.

    摘要翻译: 一种制备ε-己内酯的方法,包括:(a)使环己酮与过丙酸在有机溶剂中的溶液以环己酮的摩尔比约1.1-5:1的约0.1〜5:1的摩尔比在约10℃〜 形成基本上由ε-己内酯,丙酸和有机溶剂组成的反应混合物,(b)在第一蒸馏单元中将反应混合物从(a)中蒸馏,得到包含有机溶剂和蒸馏残余物的馏出物 (c)在一点将来自(b)的蒸馏残余物引入第二蒸馏单元以获得包含丙酸和未反应的环己酮的馏出物,从第二蒸馏单元彼此分离并在低于 引入第二蒸馏装置,ε-己内酯和任何高沸点组分,和(d)在第三蒸馏装置中蒸馏出馏出物(c)得到 基本上由丙酸组成的馏出物和包含丙酸和环己酮的混合物的蒸馏残渣。

    Working up of the residual gases resulting from the production of
cyanuric chloride
    8.
    发明授权
    Working up of the residual gases resulting from the production of cyanuric chloride 失效
    处理由产生氰尿酰氯产生的残留气体

    公开(公告)号:US4434148A

    公开(公告)日:1984-02-28

    申请号:US81555

    申请日:1979-10-03

    CPC分类号: C01C3/004 C07D251/28

    摘要: The residual gases obtained in the production of cyanuric chloride having a pressure of 1-5 bar (absolute) preferably 1-4 bar, are worked up by leading them into the lower portion of a column, reacted in the column with at least the equivalent amount of hydrogen cyanide to form cyanogen chloride and led in countercurrent flow to the water charged to the upper portion of the column whereupon the aqueous solution of cyanogen chloride formed is withdrawn from the lower portion of the column and preferably is returned into the production portion of the plant for recovery of the cyanogen chloride while the purified waste gas of the column leaves in the upper portion of the column.

    摘要翻译: 在生产具有1-5巴(绝对)压力优选1-4巴的压力的氰尿酰氯中获得的残余气体通过将它们引入塔的下部来处理,在塔中反应至少具有相当于 氰化氢的量以形成氯化氰,并且逆流地流向加到塔上部的水,由此形成的氯化氢水溶液从柱的下部排出,优选返回到 用于回收氯化氰的设备,而塔的净化废气在塔的上部离开。

    Process for the production of hydrogen cyanide
    9.
    发明授权
    Process for the production of hydrogen cyanide 失效
    生产氰化氢的方法

    公开(公告)号:US4387081A

    公开(公告)日:1983-06-07

    申请号:US304049

    申请日:1981-09-21

    IPC分类号: B01J23/00 C01C3/02

    CPC分类号: C01C3/0233

    摘要: In order to be independent of the situation in regard to methane and natural gas and at the same time to obtain a heating gas there is employed in the hydrocyanic acid-methane-ammonia process (the BMA process) in place of methane an alkanol or alkanediol having 2-4 carbon atoms, preferably ethyl alcohol, and this is reacted with ammonia in a C:N ratio of 0.8:1 to 2:1. Optionally additional hydrogen can be present.

    摘要翻译: 为了独立于甲烷和天然气的情况,同时获得加热气体,采用氢氰酸 - 甲烷 - 氨法(BMA法)代替烷烃或链烷二醇 具有2-4个碳原子,优选乙醇,并且其与C:N比为0.8:1至2:1的氨反应。 可选地,可以存在另外的氢。

    Process for isolating propylene glycol diesters in the preparation of
propylene oxide
    10.
    发明授权
    Process for isolating propylene glycol diesters in the preparation of propylene oxide 失效
    在制备环氧丙烷中分离丙二醇二酯的方法

    公开(公告)号:US4159925A

    公开(公告)日:1979-07-03

    申请号:US858319

    申请日:1977-12-09

    摘要: Process for isolating propylene glycol diacarboxylates in the preparation of propylene oxide by reaction of propylene with a solution of percarboxylic acid in an organic solvent, the boiling point of which is lower than that of the carboxylic acid which corresponds to the percarboxylic acid used as the epoxidizing agent, and higher than that of propylene oxide, separation, by distillation, of the reaction mixture which essentially contains propylene oxide, the carboxylic acid corresponding to the percarboxylic acid used as the epoxidizing agent and one or more of the by-products propyleneglycol, propylene glycol monocarboxylate and propylene glycol dicarboxylate as well as propylene and the organic solvent, into a fraction containing propylene oxide and propylene and a fraction containing the carboxylic acid, the by-products mentioned and the organic solvent and further separation of the fractions into the individual components by distillation. The fraction containing the carboxylic acid, one or more of the by-products propylene glycol, propylene glycol monocarboxylate and propylene glycol dicarboxylate, and the organic solvent is distilled in a column at pressures of 1.5 to 6 bars and with an average residence time of 10 to 90 minutes in the sump. The organic solvent is removed as the top product and the carboxylic acid and the corresponding propylene glycol dicarboxylate is obtained as the sump product. From the sump product the propylene glycol dicarboxylate is isolated in a manner which is in itself known.

    摘要翻译: 通过丙烯与过羧酸在有机溶剂中的溶液反应制备环氧丙烷中的丙二醇二羧酸盐的分离方法,其沸点低于对应于用作环氧化物的过羧酸的羧酸 试剂,高于环氧丙烷,通过蒸馏分离基本上含有环氧丙烷的反应混合物,对应于用作环氧化剂的过羧酸的羧酸和一种或多种副产物丙二醇,丙烯 乙二醇单羧酸酯和丙二醇二羧酸酯以及丙烯和有机溶剂转化成含有环氧丙烷和丙烯的馏分和含有羧酸的馏分,所述副产物和有机溶剂,并将馏分进一步分离成单独组分 通过蒸馏。 将含有羧酸,一种或多种副产物丙二醇,丙二醇单羧酸酯和丙二醇二羧酸酯和有机溶剂的级分在1.5至6巴的压力下在柱中蒸馏,并且平均停留时间为10 在水槽中90分钟。 作为顶部产物除去有机溶剂,得到羧酸和相应的丙二醇二羧酸酯作为贮槽产物。 从贮槽产品中,以本身已知的方式分离丙二醇二羧酸酯。