Dividing-wall column with feed in whole or in part in the vaporous state and/or side stream take off in whole or in part in the vaporous state
    5.
    发明授权
    Dividing-wall column with feed in whole or in part in the vaporous state and/or side stream take off in whole or in part in the vaporous state 有权
    全部或部分进料在蒸发态和/或侧流中的分隔壁塔全部或部分脱气

    公开(公告)号:US07264696B2

    公开(公告)日:2007-09-04

    申请号:US11384370

    申请日:2006-03-21

    IPC分类号: B01D3/42

    摘要: A dividing-wall column having a dividing wall which is essentially disposed along the long direction of the column is proposed, which divides the column interior into a feed part, a take off part, an upper shared column part and a lower shared column part, with feed in whole or in part in the vaporous state of a mixture to be separated between the upper region of the feed part and the lower region of the feed part and/or side stream take off in whole or in part in the vaporous state between the upper region of the take off part and the lower region of the take off part, where if feed is in whole or in part in the vaporous state the cross-sectional area of the upper region of the feed part is increased by plane-parallel displacement of the dividing wall toward the upper region of the take off part, and/or if the side stream take off is in whole or in part in the vaporous state, the cross-sectional area of the lower region of the take off part is increased by displacement of the dividing wall toward the lower region of the feed part, in such a manner that the F factor is substantially the same in all column regions.

    摘要翻译: 提出了具有分隔壁的分隔壁,该分隔壁基本上沿着塔的长方向设置,其将塔内部分为进料部分,脱落部分,上共享塔部分和下共享塔部分, 在进料部分的上部区域和进料部分的下部区域和/或侧馏分之间在蒸气状态下的全部或部分蒸气状态下的进料全部或部分地在蒸气状态之间分离, 取出部分的上部区域和脱落部分的下部区域,如果进料全部或部分处于气态,则进料部分的上部区域的横截面面积被平面平行地增加 分流壁向脱气部的上部区域的位移,和/或侧流的脱落全部或部分处于蒸发状态,脱落部的下部区域的截面积为 由分界位移增加 壁朝向馈送部分的下部区域,使得F因子在所有列区域中基本相同。

    Continuous process for producing pseudoinones and ionones
    9.
    发明申请
    Continuous process for producing pseudoinones and ionones 有权
    连续生产假戊烯酮和紫罗兰酮的方法

    公开(公告)号:US20060014984A1

    公开(公告)日:2006-01-19

    申请号:US10533969

    申请日:2003-10-28

    IPC分类号: C07C45/72

    摘要: The invention relates to a continuous process for producing pseudoionones of general formulas (I) and (I′) as well as isomers thereof, whereby: R1 represents CH3 or (a); R2 and R3 represent hydrogen, CH3 or C2H5, and; R4 and R5 represent hydrogen or CH3. These pseudoionones are produced by reacting an aldehyde of formula (II) with an excess of a ketone of general formula (III), whereby R1, R2 and R3 have the aforementioned meanings, in the presence of water and alkali hydroxide at an increased temperature and in a homogeneous solution. The inventive process is characterized in that: a) the intermixing of the homogeneous solution consisting of aldehyde, ketone and aqueous alkali lye occurs at a temperature ranging from 10 to 120° C.; b) the undissolved water and alkali hydroxide contained in the reaction mixture are subsequently separated out; c) while avoiding back mixing, the homogeneous reaction mixture is then guided through a reactor, which permits a residence time ranging from 2 to 300 minutes, at a temperature that is 10 to 120° C. higher than the boiling point of the lowest-boiling component and under a vapor pressure p ranging from 106 to 107 Pa; d) the reaction mixture is cooled by expansion; e) ketone is removed from the reaction mixture using vapor flowing in the opposite direction and; f) the raw product is dried and rid from excessive aldehyde and secondary components via a rectification column.

    摘要翻译: 本发明涉及用于生产通式(I)和(I')的假阳离子及其异构体的连续方法,其中:R 1表示CH 3或( 一个); R 2和R 3代表氢,CH 3或C 2 H 5, ,和 R 4和R 5代表氢或CH 3。 这些假性离子是通过使式(II)的醛与过量的通式(III)的酮反应制得的,其中R 1,R 2和R 2 在水和碱金属氢氧化物的存在下,在升高的温度下和均匀的溶液中具有上述含义。 本发明的方法的特征在于:a)由醛,酮和碱性碱液组成的均匀溶液的混合在10至120℃的温度下进行; b)随后将反应混合物中所含的未溶解的水和氢氧化碱分离出来; c)同时避免反混合,然后将均匀的反应混合物引导通过反应器,其允许停留时间为2至300分钟,温度高于最低浓度的沸点为10至120℃, 沸腾成分,并且在10 -6至10 7 Pa范围内的蒸汽压力p; d)反应混合物通过膨胀冷却; e)使用沿相反方向流动的蒸汽从反应混合物中除去酮; f)将原料干燥并通过精馏塔除去过量的醛和次要组分。

    Continuous process for producing pseudoionones and ionones
    10.
    发明授权
    Continuous process for producing pseudoionones and ionones 有权
    连续生产假阳离子和紫罗兰酮的方法

    公开(公告)号:US07141698B2

    公开(公告)日:2006-11-28

    申请号:US10533969

    申请日:2003-10-28

    IPC分类号: C07C45/72

    摘要: The invention relates to a continuous process for producing pseudoionones of general formulas (I) and (I′) as well as isomers thereof, whereby: R1 represents CH3 or (a); R2 and R3 represent hydrogen, CH3 or C2H5, and; R4 and R5 represent hydrogen or CH3. These pseudoionones are produced by reacting an aldehyde of formula (II) with an excess of a ketone of general formula (III), whereby R1, R2 and R3 have the aforementioned meanings, in the presence of water and alkali hydroxide at an increased temperature and in a homogeneous solution. The inventive process is characterized in that: a) the intermixing of the homogeneous solution consisting of aldehyde, ketone and aqueous alkali lye occurs at a temperature ranging from 10 to 120° C.; b) the undissolved water and alkali hydroxide contained in the reaction mixture are subsequently separated out; c) while avoiding back mixing, the homogeneous reaction mixture is then guided through a reactor, which permits a residence time ranging from 2 to 300 minutes, at a temperature that is 10 to 120° C. higher than the boiling point of the lowest-boiling component and under a vapor pressure p ranging from 106 to 107 Pa; d) the reaction mixture is cooled by expansion; e) ketone is removed from the reaction mixture using vapor flowing in the opposite direction and; f) the raw product is dried and rid from excessive aldehyde and secondary components via a rectification column

    摘要翻译: 本发明涉及用于生产通式(I)和(I')的假阳离子及其异构体的连续方法,其中:R 1表示CH 3或( 一个); R 2和R 3代表氢,CH 3或C 2 H 5, ,和 R 4和R 5代表氢或CH 3。 这些假性离子是通过使式(II)的醛与过量的通式(III)的酮反应制得的,其中R 1,R 2和R 2 在水和碱金属氢氧化物的存在下,在升高的温度下和均匀的溶液中具有上述含义。 本发明的方法的特征在于:a)由醛,酮和碱性碱液组成的均匀溶液的混合在10至120℃的温度下进行; b)随后将反应混合物中所含的未溶解的水和氢氧化碱分离出来; c)同时避免反混合,然后将均匀的反应混合物引导通过反应器,其允许停留时间为2至300分钟,温度高于最低浓度的沸点为10至120℃, 沸腾成分,并且在10 -6至10 7 Pa范围内的蒸汽压力p; d)反应混合物通过膨胀冷却; e)使用沿相反方向流动的蒸汽从反应混合物中除去酮; f)将原料干燥并通过精馏塔除去过量的醛和次要组分