Process for preparing linear alpha-olefins using zirconium adducts as
catalysts
    1.
    发明授权
    Process for preparing linear alpha-olefins using zirconium adducts as catalysts 失效
    使用锆加合物作为催化剂制备线性α-烯烃的方法

    公开(公告)号:US4966874A

    公开(公告)日:1990-10-30

    申请号:US325878

    申请日:1989-03-20

    Abstract: Linear alpha-olefins are prepared by the oligomerization of ethylene using a two component catalyst system comprising (a) a soluble adduct of zirconium tetrahalide, the halogen being Br or Cl, with an organic compound selected from the group of esters, ketones, ethers, amines, nitriles, anhydrides, acid chlorides, amides or aldehydes, the organic compound having up to about 30 carbon atoms and (b) an alkyl metal selected from the group R.sub.2 AlX. RAlX.sub.2, R.sub.3 Al.sub.2 X.sub.3, R.sub.3 Al and R.sub.2 Zn where R is C.sub.1 -C.sub.20 alkyl and X is Cl or Br. ZrCl.sub.4 adducts with organic acetates are the preferred embodiments.

    Abstract translation: 通过使用双组分催化剂体系制备线性α-烯烃,所述双组分催化剂体系包含(a)四卤化锆的可溶性加合物,卤素为Br或Cl,以及选自酯,酮,醚, 胺,腈,酸酐,酰氯,酰胺或醛,具有至多约30个碳原子的有机化合物和(b)选自R2AlX的烷基金属。 RA1X2,R3Al2X3,R3Al和R2Zn,其中R是C1-C20烷基,X是Cl或Br。 ZrCl 4与有机乙酸酯的加合物是优选的实施方案。

    Liquid phthalic anhydride recovery process using a rectification tower
with benzoic acid control
    3.
    发明授权
    Liquid phthalic anhydride recovery process using a rectification tower with benzoic acid control 失效
    液体邻苯二甲酸酐回收工艺采用精馏塔采用苯甲酸控制

    公开(公告)号:US5730844A

    公开(公告)日:1998-03-24

    申请号:US758559

    申请日:1996-11-29

    CPC classification number: C07C51/43

    Abstract: A process for recovering phthalic anhydride as a liquid from a vapor phase oxidation product which comprises mixing the vapor phase oxidation product having a temperature of about 130.degree. C. or greater with a first stream comprising maleic anhydride, benzoic acid present in an amount of less than 8 mole %, based on the total concentration of the first stream, and at least one compound selected from the group consisting of: citraconic anhydride and phthalic anhydride, in a rectification tower such that a substantial portion of the phthalic anhydride contained within the vapor phase oxidation product transfers from the vapor phase to a liquid phase and a substantial portion of the by-products contained in the first stream which are more volatile than phthalic anhydride transfer from the liquid phase to the vapor phase and wherein a vapor-to-liquid weight ratio in the range between about 2 to 20 is exhibited within the rectification tower, thereby forming a liquid phase phthalic anhydride product having a phthalic anhydride concentration in the range between about 50-100 wt. %.

    Abstract translation: 从气相氧化产物中回收邻苯二甲酸酐作为液体的方法,该方法包括将具有约130℃或更高温度的气相氧化产物与包含马来酸酐的第一物流,一定量的苯甲酸 在精馏塔中,基于第一料流的总浓度和至少一种选自柠康酸酐和邻苯二甲酸酐的化合物的8摩尔%,使得大部分邻苯二甲酸酐包含在蒸气中 相氧化产物从蒸气相转移到液相,以及包含在第一物流中的大部分副产物,其比从邻苯二甲酸酐从液相转移到气相更易挥发,并且其中蒸气到液体 在精馏塔内表现出约2-20范围内的重量比,从而形成液相邻苯二甲酸酐 邻苯二甲酸酐浓度在约50-100wt。 %。

    Solvent assisted process for recovery of phthalic anhydride in the
liquid phase by distillation
    4.
    发明授权
    Solvent assisted process for recovery of phthalic anhydride in the liquid phase by distillation 失效
    通过蒸馏在液相中回收邻苯二甲酸酐的溶剂辅助方法

    公开(公告)号:US5718808A

    公开(公告)日:1998-02-17

    申请号:US758558

    申请日:1996-11-29

    CPC classification number: C07C51/573

    Abstract: A process for recovering phthalic anhydride as a liquid from a vapor phase oxidation product which comprises mixing the vapor phase oxidation product having a temperature of about 130.degree. C. or greater with a first stream comprising a solvent having a boiling point in the range between about 150.degree. to 350.degree. C. and a freezing point of less than 40.degree. C., and, optionally, at least one by-product selected from the group consisting of: maleic anhydride, citraconic anhydride, benzoic acid and phthalic anhydride, in a contacting means such that a substantial portion of the phthalic anhydride contained within the vapor phase oxidation product transfers from the vapor phase to a liquid phase and a substantial portion of the first stream which are more volatile than phthalic anhydride transfer from the liquid phase to the vapor phase and wherein a vapor-to-liquid weight ratio in the range between about 2 to 20 is exhibited within the contacting means, thereby forming a liquid phase phthalic anhydride product having a phthalic anhydride concentration in the range between about 50-100 wt. %., preferably 90-100 wt. %, without the formation of an intermediate solid phase.

    Abstract translation: 从气相氧化产物中回收邻苯二甲酸酐作为液体的方法,其包括将具有约130℃或更高温度的气相氧化产物与包含沸点在约 150℃至350℃,冰点低于40℃,以及任选地至少一种副产物,其选自马来酸酐,柠康酸酐,苯甲酸和邻苯二甲酸酐,其中 接触方式使得气相氧化产物中所含的邻苯二甲酸酐的相当大部分从汽相转移到液相,并且大部分第一物流比邻苯二甲酸酐从液相转移到蒸汽更易挥发 相,并且其中在接触装置内显示约2-20范围内的气 - 液重量比,从而形成液相邻苯二甲酸 酸酐产物的邻苯二甲酸酐浓度在约50-100wt。 %,优选90-100wt。 %,而不形成中​​间固相。

    Optimized catalyst addition to enhance esterification catalyst performance
    7.
    发明授权
    Optimized catalyst addition to enhance esterification catalyst performance 失效
    优化催化剂加成酯化催化剂性能

    公开(公告)号:US06355817B1

    公开(公告)日:2002-03-12

    申请号:US09616329

    申请日:2000-07-15

    CPC classification number: C07C67/08 C07C69/80

    Abstract: The present invention provides a process for the production of an ester, including reacting an alcohol with a carbonyl-like compound in the presence of a first esterification catalyst; and adding a second esterification catalyst to the reaction mixture at some time after initiation of the esterification reaction. The staged addition of the esterification catalyst according to the present invention provides a reduced reaction time to achieve a targeted conversion to esters.

    Abstract translation: 本发明提供一种生产酯的方法,包括在第一酯化催化剂存在下使醇与羰基化合物反应; 并在酯化反应开始后的某个时间向反应混合物中加入第二酯化催化剂。 根据本发明的分级加成酯化催化剂提供了缩短的反应时间以实现酯的目标转化。

    Method for recovering phthalic anhydride/maleic anhydride mixtures by
distillation
    8.
    发明授权
    Method for recovering phthalic anhydride/maleic anhydride mixtures by distillation 失效
    通过蒸馏回收邻苯二甲酸酐/马来酸酐混合物的方法

    公开(公告)号:US5869700A

    公开(公告)日:1999-02-09

    申请号:US803681

    申请日:1997-02-21

    CPC classification number: C07C51/573

    Abstract: A process for recovering phthalic anhydride and maleic anhydride from a maleic anhydride-rich vapor phase oxidation product comprising the step of: contacting the vapor phase oxidation product with: (i) at least one by-product stream having a freezing point which is lower than the freezing point of pure phthalic anhydride; and/or (ii) a solvent having a boiling point in the range between about 150.degree. to 350.degree. C. and a freezing point of less than 40.degree. C.; wherein a vapor-to-liquid weight ratio in the range between about 2 to 20 is exhibited within the contacting means, thereby forming a liquid phase phthalic anhydride product having a phthalic anhydride concentration in the range between about 50-100 wt. % and a first vapor stream.

    Abstract translation: 一种从富含马来酸酐的气相氧化产物中回收邻苯二甲酸酐和马来酸酐的方法,包括以下步骤:使气相氧化产物与下列物质接触:(i)至少一种副产物流,其具有低于 纯邻苯二甲酸酐的凝固点; 和/或(ⅱ)沸点在约150至350℃之间且凝固点小于40℃的溶剂。 其中在所述接触装置内显示约2-20范围内的气 - 液重量比,由此形成邻苯二甲酸酐浓度在约50-100重量%之间的液相邻苯二甲酸酐产物。 %和第一蒸气流。

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