Method and device for the distillative processing of 1,6-hexanediol, 1,5-pentanediol and caprolactone
    1.
    发明授权
    Method and device for the distillative processing of 1,6-hexanediol, 1,5-pentanediol and caprolactone 有权
    1,6-己二醇,1,5-戊二醇和己内酯的蒸馏加工方法和装置

    公开(公告)号:US07329330B2

    公开(公告)日:2008-02-12

    申请号:US10451738

    申请日:2002-01-08

    IPC分类号: B01D3/14 B01D3/42 C07C29/80

    摘要: A process for working up by distillation the crude products obtained in the process according to DE-A 196 07 954 and containing 1,6-hexanediol (HDO), 1,5-pentanediol (PDO) or caprolactone (CLO) in order to obtain the corresponding pure products, the working-up by distillation being carried out in each case in a dividing wall column (TK) in which a dividing wall (T) is arranged in the longitudinal direction of the column with formation of an upper common column region (1), a lower common column region (6), a feed section (2, 4) having a rectification section (2) and stripping section (4), and a take-off section (3, 5) having a stripping section (3) and rectification section (5), with feeding of the respective crude product HDO, PLO or CLO in the middle region of the feed section (2, 4) and removal of the high boiler fraction (C) from the bottom of the column, of the low boiler fraction (A) via the top of the column and of the medium boiler fraction (B) from the middle region of the take-off section (3, 5), or in thermally coupled columns.

    摘要翻译: 通过蒸馏处理根据DE-A 196 07954的方法获得的含有1,6-己二醇(HDO),1,5-戊二醇(PDO)或己内酯(CLO)的粗产物的方法,以获得 相应的纯产品,在各种情况下在分隔壁塔(TK)中进行蒸馏处理,其中分隔壁(T)沿塔的纵向方向排列,形成上共同区域 (1),较低的公共列区域(6),具有整流部分(2)和汽提部分(4)的进料部分(2,4)和具有汽提部分的取出部分(3,5) (3)和整流部分(5),在进料部分(2,4)的中间区域供给相应的粗产物HDO,PLO或CLO,并将高沸点馏分(C)从底部 通过塔顶和中间锅炉馏分(B)从中间排出低沸点馏分(A) 起飞段(3,5)的区域,或热耦合柱。

    Dividing wall column
    2.
    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

    IPC分类号: B01D3/14 B01D3/16

    CPC分类号: B01D3/141 B01D3/146

    摘要: 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.

    摘要翻译: 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。

    Process for preparing higher unsaturated ketones
    4.
    发明授权
    Process for preparing higher unsaturated ketones 失效
    制备高级不饱和酮的方法

    公开(公告)号:US06300524B1

    公开(公告)日:2001-10-09

    申请号:US09440281

    申请日:1999-11-15

    IPC分类号: C07C4500

    摘要: The present invention relates to an improved process for preparing higher unsaturated ketones by reacting the corresponding &agr;,&bgr;-unsaturated alcohols with alkyl acetoacetates in a Carroll reaction , in a reactor system with fitted fractionation column, wherein A the &agr;,&bgr;-unsaturated alcohol is introduced into the reaction vessel together with the organic aluminum compound in the absence of effective amounts of a solvent, and the alkyl acetoacetate is metered into this mixture, B a reaction temperature which is as constant as possible at between 175° C. and 220° C., preferably between 180° C. and 200° C., is adjusted and C during the reaction the content of alkyl acetoacetate in the reaction mixture is adjusted to a value which is as constant as possible at between 1 and 3% by weight. It is advantageous in this process for the reaction temperature defined under B to be controlled by suitable variation of the heat input and/or by variation of the rate of addition of the alkyl acetoacetate, and for adequate mixing of the reaction mixture in the reaction vessel to be ensured This can be achieved with the aid of a stirrer, by pumping the reaction mixture through an external liquid circulation, by introducing the alkyl acetoacetate by means of a mixing nozzle or else by passing in a stream of inert gas. The process according to the invention is particularly suitable for the Carroll reaction of higher alcohols such as 3,7-dimethyl-1,6-octadien-3-ol (linalool), 3,7-dimethyl-1-octen-3-ol, 3,7,11-trimethyl-1,6,10-dodecatrien-3-ol (nerolidol), 3,7,11-trimethyl-1-dodecen-3-ol or 3,7,11-trimethyl-1,6-dodecadien-3-ol (dihydronerolidol).

    摘要翻译: 本发明涉及一种改进的制备高级不饱和酮的方法,该方法通过在具有合适分馏塔的反应器系统中,在卡罗尔反应中使相应的α,β-不饱和醇与烷基乙酰乙酸酯反应,其中引入α,β-不饱和醇 在没有有效量的溶剂的情况下,将有机铝化合物与有机铝化合物一起加入到反应容器中,并将乙酰乙酸烷基酯计量加入到该混合物中,B在175℃和220℃之间的反应温度尽可能恒定 在反应过程中,优选在180℃和200℃之间调节和C,将反应混合物中乙酰乙酸烷基酯的含量调节至1至3重量%之间尽可能恒定的值。 在该方法中,通过适当变化的热输入和/或通过烷基的加成速率的变化来控制在B下限定的反应温度, 乙酰乙酸酯,并使反应混合物在反应容器中充分混合以确保这可以借助于搅拌器,通过泵送反应混合物通过外部液体循环,通过引入烷基乙酰乙酸酯通过混合喷嘴 或者通过流入惰性气体流。根据本发明的方法特别适用于高级醇如3,7-二甲基-1,6-辛二烯-3-醇(芳樟醇),3, 7,7-二甲基-1-辛烯-3-醇,3,7,11-三甲基-1,6,10-十二碳三烯-3-醇(橙花叔醇),3,7,11-三甲基-1-十二碳烯-3-醇 或3,7,11-三甲基-1,6-十二碳二烯-3-醇(二氢吗啉醇)。

    PROCESS FOR OBTAINING MALEIC ANHYDRIDE BY DISTILLATION
    7.
    发明申请
    PROCESS FOR OBTAINING MALEIC ANHYDRIDE BY DISTILLATION 有权
    通过蒸馏获得马来酸酐的方法

    公开(公告)号:US20100113805A1

    公开(公告)日:2010-05-06

    申请号:US12532660

    申请日:2008-03-19

    IPC分类号: C07D307/60

    摘要: What is described is a process for obtaining maleic anhydride by distillation from a solution of maleic anhydride in a high-boiling absorbent which has been obtained by gas phase oxidation of a hydrocarbon and at least partial absorption of the oxidation products into the absorbent, by i) introducing the solution into the side of a feed column with a rectifying section disposed above the feed point and a stripping section disposed below the feed point, ii) providing an upper combining column which communicates with the upper end of the rectifying section and a lower combining column which communicates with the lower end of the stripping section, iii) providing a draw column which communicates with the upper combining column and the lower combining column, iv) drawing maleic anhydride off as a side draw from the draw column, and drawing off compounds having a lower boiling point than maleic anhydride at the top of the upper combining column and the high-boiling absorbent at the bottom of the lower combining column. The maleic anhydride obtained as a side draw has a low content of acrylic acid and acetic acid.

    摘要翻译: 所描述的是通过蒸馏从马来酸酐在高沸点吸收剂中的溶液获得马来酸酐的方法,其通过烃的气相氧化和至少部分吸收氧化产物进入吸收剂中获得, 将溶液引入进料塔的侧面,其中设置在进料点上方的精馏部分和设置在进料点下方的汽提部分,ii)提供与精馏部分的上端连通的上部混合塔和下部 组合柱与汽提部分的下端连通,iii)提供与上部混合塔和下部混合塔连通的牵引柱,iv)将拉伸马来酸酐作为拉伸塔的牵引拉出,拉出 在上部混合塔的顶部具有比马来酸酐低的沸点的化合物和在底部o的高沸点吸收剂 f下组合列。 作为侧馏分获得的马来酸酐具有低含量的丙烯酸和乙酸。

    PROCESS FOR CONTINUOUS HYDROGENATION OR HYDROGENATING AMINATION
    8.
    发明申请
    PROCESS FOR CONTINUOUS HYDROGENATION OR HYDROGENATING AMINATION 有权
    连续加氢或加氢胺化的方法

    公开(公告)号:US20100081804A1

    公开(公告)日:2010-04-01

    申请号:US12090377

    申请日:2006-10-16

    IPC分类号: C07D265/30 C07C45/00

    摘要: A process is described for continuously hydrogenating unsaturated compounds, in which particles of a first hydrogenation catalyst are suspended in a liquid phase in which an unsaturated compound is dissolved, the liquid phase, in the presence of a hydrogenous gas at a first partial hydrogen pressure and at a first temperature, is conducted through a packed bubble column reactor in cocurrent counter to the direction of gravity, the effluent from the bubble column reactor is sent to a gas-liquid separation, the liquid phase is sent to a crossfiltration to obtain a retentate and a filtrate, the retentate is recycled into the bubble column reactor and the filtrate, in the presence of a hydrogenous gas at a second partial hydrogen pressure and at a second temperature, is passed over a bed of a second hydrogenation catalyst, wherein the second partial hydrogen pressure is at least 10 bar higher than the first partial hydrogen pressure.

    摘要翻译: 描述了在第一部分氢气压力下在氢气存在下将不饱和化合物连续氢化的方法,其中第一氢化催化剂的颗粒悬浮在其中溶解不饱和化合物的液相中,液相,以及 在第一个温度下,通过气泡塔反应器与重力方向并流,将来自泡罩塔反应器的流出物送入气液分离,将液相送至交叉过滤,得到滞留物 和滤液,将滞留物再循环到泡罩塔反应器中,并且在第二部分氢气压力和第二温度下在氢气存在下将滤液通过第二氢化催化剂床,其中第二 部分氢气压力比第一部分氢气压力高至少10巴。

    METHOD FOR PREVENTING FUMARIC ACID DEPOSITS IN THE PRODUCTION OF MALEIC ACID ANHYDRIDE
    9.
    发明申请
    METHOD FOR PREVENTING FUMARIC ACID DEPOSITS IN THE PRODUCTION OF MALEIC ACID ANHYDRIDE 审中-公开
    在制备马来酸酐时防止含氟酸沉积物的方法

    公开(公告)号:US20090143601A1

    公开(公告)日:2009-06-04

    申请号:US12300571

    申请日:2007-05-16

    IPC分类号: C07D307/60

    CPC分类号: C07C51/573 C07C57/145

    摘要: The present invention provides a process for preventing fumaric acid deposits in the preparation of maleic anhydride, comprising the following steps:a) absorption of a C4-dicarboxylic acid or of a derivative from a crude product mixture into an organic solvent or water as an absorbent,b) removal of the C4-dicarboxylic acid or of a derivative from the absorbent,the absorbent thus recovered being catalytically hydrogenated fully or partly and recycled fully or partly into the absorption stage (a).

    摘要翻译: 本发明提供了一种在制备马来酸酐中防止富马酸沉积的方法,包括以下步骤:a)将C4-二羧酸或衍生物从粗产物混合物中吸收到作为吸收剂的有机溶剂或水中 b)从吸收剂中除去C4-二羧酸或衍生物,这样回收的吸收剂被完全或部分催化氢化,或者完全或部分地再循环到吸收阶段(a)中。