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    • 1. 发明申请
    • Process for preparing alkyl- or aryloxyacetaldehydes
    • 制备烷基或芳氧基乙醛的方法
    • US20010053852A1
    • 2001-12-20
    • US09897390
    • 2001-07-03
    • Karlheinz GiselbrechtRudolf Hermanseder
    • C07D237/02C07C045/42
    • C07C45/56C07C47/198C07C47/277
    • A process for preparing alkyl- or aryloxyacetaldehydes of the formula 1 where R can be an unsubstituted or mono- or polysubstituted alkyl, aryl, heteroaryl, alkaryl, alkylheteroaryl or aralkyl radical or an unsubstituted or mono- or polysubstituted heterocycle or alkyl heterocycle, which comprises reacting a compound of the formula RnullOMnullnull(II) where R is as defined above and M can be an alkali metal atom or an alkaline earth metal atom, with a compound of the formula 2 where R1 and R2 independently of one another are a C1-C6-alkyl radical or together are a C2-C6-alkylene radical and X is a halogen atom, to form the corresponding dialkylacetal of the formula 3 where R, R1 and R2 are as defined above, whereupon acetal cleavage is carried out to give the desired alkyl- or aryloxyacetaldehydes of the formula (I).
    • 制备下式的烷基 - 或芳氧基乙醛的方法,其中R可以是未取代的或单取代或多取代的烷基,芳基,杂芳基,烷芳基,烷基杂芳基或芳烷基或未取代或单取代或多取代的杂环或烷基杂环, 式(I)所示的化合物,其中R如上定义,M可以是碱金属原子或 碱土金属原子与下式的化合物反应,其中R 1和R 2彼此独立地为C 1 -C 6烷基或一起为C 2 -C 6亚烷基,X为卤素原子,形成相应的二烷基缩醛 其中R,R 1和R 2如上所定义,由此进行缩醛裂解,得到所需的式(I)的烷基 - 或芳氧基乙醛,
    • 3. 发明申请
    • Decomposition of cumene oxidation product
    • 异丙苯氧化产物的分解
    • US20020040165A1
    • 2002-04-04
    • US09865190
    • 2001-07-23
    • Richard R. HertzogStylianos SifniadesWilliam Bernard Fisher
    • C07C045/42C07C037/08
    • C07C1/20C07C37/08C07C45/53C07C15/44C07C49/08C07C39/04
    • A process for decomposing a cumene oxidation product mixture containing cumene hydroperoxide (CHP) and dimethylphenyl carbinol (DMPC) to produce phenol, acetone and alpha-methyl styrene (AMS) with enhanced safety of operation and reduced by-product formation which comprises the steps: (a) mixing the cumene oxidation product in a stirred or back-mixed reactor with an acid catalyst, with 10 to 100 percent acetone relative to the amount of acetone produced during the decomposition reaction, and with up to 4 weight percent additional amounts of water relative to the reaction mixture, at an average temperature between about 50null C. and about 90null C. for a time sufficient to lower the average CHP concentration of the reactor to between about 0.2 and about 3.0 weight percent, and wherein a portion of DMPC is converted to dicumyl peroxide (DCP); then (b) reacting the reaction mixture from step (a) at a temperature between about 120null C. and 150null C. under plug-flow conditions for a time sufficient to decompose substantially all residual CHP and at least 90 percent of the DCP formed in step (a).
    • 一种分解含有氢过氧化枯烯(CHP)和二甲基苯甲醇(DMPC)的枯烯氧化产物混合物以产生苯酚,丙酮和α-甲基苯乙烯(AMS)的方法,其具有更高的操作安全性和减少的副产物形成,其包括以下步骤: (a)相对于在分解反应期间产生的丙酮的量,将异丙苯氧化产物与搅拌或反向混合的反应器中的酸催化剂混合10至100%丙酮,并加入高达4重量%的附加量的水 相对于反应混合物,在约50℃至约90℃的平均温度下,足以将反应器的平均CHP浓度降低至约0.2至约3.0重量%的时间,并且其中一部分 DMPC转化为过氧化二异丙苯(DCP); 然后(b)使反应混合物从步骤(a)在约120℃和150℃之间的温度下在活塞流条件下反应足以分解基本上所有剩余CHP的时间和至少90%的DCP 在步骤(a)中形成。