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    • 4. 发明授权
    • Substituted benzophenone dicarboxylic acids
    • 取代的二苯甲酮二羧酸
    • US5073552A
    • 1991-12-17
    • US576849
    • 1990-09-04
    • Mark W. BeltzVenkataraman Ramachandran
    • Mark W. BeltzVenkataraman Ramachandran
    • C07C205/38C07C217/90
    • C07C217/90C07C205/38
    • Substituted benzophenones are disclosed having the following formula ##STR1## where R.sub.A and R.sub.B are each independently COOH, C.sub.1 to C.sub.12 linear or branched alkyl or taken together to form an anhydride ring, R is nitro or amino unsubstituted or substituted with at least one C.sub.1 to C.sub.6 linear or branched alkyl, phenyl or substituted phenyl, the substituents being one or more C.sub.1 to C.sub.6 linear or branched alkyl or C.sub.6 to C.sub.10 aryl, Y and Y' are the same or different and are a chemical bond ##STR2## and m is 0 or 1 with the proviso that both R.sub.A and R.sub.B can not be hydrogen.Processes to produce these benzophenones are also disclosed.
    • 公开了具有下列结构式的取代的二苯甲酮,其中RA和RB各自独立地为COOH,C1至C12直链或支链烷基或一起形成酸酐环,R为硝基或未取代的氨基或被至少一个C1至 C6直链或支链烷基,苯基或取代的苯基,取代基是一个或多个C 1至C 6直链或支链烷基或C 6至C 10芳基,Y和Y'相同或不同,并且是化学键。 )2,C(CF 3)2或Si(CH 3)2,m为0或1,条件是RA和RB都不能为氢。 还公开了制备这些二苯甲酮的方法。
    • 8. 发明授权
    • Process for purifying a 2,6-dialkylphenol
    • 纯化2,6-二烷基苯酚的方法
    • US5705039A
    • 1998-01-06
    • US542612
    • 1995-10-13
    • Sam F. ClarkeVenkataraman RamachandranJ. Steve StatonPaul L. Wiggins
    • Sam F. ClarkeVenkataraman RamachandranJ. Steve StatonPaul L. Wiggins
    • B01D3/14C07C37/74B01D3/00C07C37/68
    • B01D3/146C07C37/685C07C37/74Y10S203/07Y10S203/09
    • Impure 2,6-diisopropylphenol (DIP) is purified by use of a distillation process in which a single distillation column is used. The process comprises: (a) subjecting the impure DIP to a first continuous distillation in the column in an inert environment to distill off lower boiling components and produce first column bottoms enriched in DIP; (b) collecting, cooling and storing the first column bottoms while continuously maintaining them in an inert environment; (c) discontinuing the first continuous distillation; (d) subjecting the first column bottoms to a second continuous distillation in an inert environment in the same column to produce a second overhead distillate composed of purified DIP. The process avoids the formation in the distilling mixtures of dose boiling impurities due to seepage of air through standard pipe flanges and fittings and consequent oxidation reactions which occur under the conditions needed for batch distillations conducted in typical industrial distillation facilities. These impurities include 2,6-diisopropylbenzoquinone, 2-isopropyl-6-isopropenylphenol, 2,6-diisopropenylphenol and 2,2-dimethyl-4-isopropyl-1,3-benzodioxole. The capital investment needed for a conventional continuous distillation facility is also avoided.
    • 不纯的2,6-二异丙基苯酚(DIP)通过使用其中使用单个蒸馏塔的蒸馏方法纯化。 该方法包括:(a)使惰性DIP在惰性环境中在柱中进行第一次连续蒸馏以蒸馏掉低沸点组分并产生富含DIP的第一塔底物; (b)收集,冷却和储存第一塔底,同时将其保持在惰性环境中; (c)停止第一次连续蒸馏; (d)在同一塔的惰性环境中对第一塔底部进行第二次连续蒸馏以产生由纯化的DIP组成的第二塔顶馏出物。 该过程避免了在典型工业蒸馏设备中进行的批次蒸馏所需的条件下,由于通过标准管道法兰和配件的空气渗漏导致的沸腾杂质的蒸馏混合物中的形成以及随之而来的氧化反应。 这些杂质包括2,6-二异丙基苯醌,2-异丙基-6-异丙烯基苯酚,2,6-二异丙烯基苯酚和2,2-二甲基-4-异丙基-1,3-苯并间二氧杂环戊烯。 也避免了常规连续蒸馏设备所需的投资。