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    • 2. 发明授权
    • Production process for pyromellitic dianhydride
    • 均苯四甲酸二酐的制备方法
    • US6153767A
    • 2000-11-28
    • US270742
    • 1999-03-16
    • Toshio SaganeTsukasa TakahashiYasuhisa Emoto
    • Toshio SaganeTsukasa TakahashiYasuhisa Emoto
    • B01J8/06B01J23/22B01J27/18B01J27/198B01J35/00C07C51/265C07D493/04
    • C07C51/265B01J23/002B01J23/22B01J27/1817B01J27/198B01J35/0006B01J8/06B01J2523/00
    • Provided is a process for producing pyromellitic dianhydride by feeding 1,2,4,5-tetraalkylbenzene to a fixed bed multitubular type reactor charged with a catalyst layer to carry out catalytic vapor phase oxidation. This process is characterized by dividing the catalyst layer into at least two layers to charge a layer at an outlet side of reaction gas and a layer at an inlet side of raw material mixed gas with the following catalyst A and catalyst B respectively or dividing the catalyst layer into at least three layers to charge a layer at an outlet side of reaction gas, an intermediate layer and a layer at an inlet side of raw material mixed gas with the following catalyst A, catalyst B and catalyst C respectively:catalyst A: a catalyst containing V.sub.a (A).sub.b P.sub.c Ag.sub.d (B).sub.e O.sub.x, wherein (A) represents at least one element selected from Mo and W; (B) represents at least one element selected from alkaline metals and alkaline earth metals; a to e each represent an atomic number thereof,catalyst B: a catalyst containing V.sub.a Ti.sub.b (C).sub.c (D).sub.d Ce.sub.e O.sub.x wherein (C) represents at least one element selected from rare earth elements (excluding cerium); (D) represents at least one element selected from P, Sb, Hf, Nb, T, B and S; a to e and x each represent an atomic number thereof, andcatalyst C: a catalyst containing V.sub.a (E).sub.b (F).sub.c (G).sub.d O.sub.x, wherein (E) represents at least one element selected from alkaline metals; (F) represents at least one element selected from P and Cu; (G) represents at least one element selected from silver, sulfur, tantalum, boron, tungusten, and molybdenum; a to d and x each represent an atomic number thereof.
    • 本发明提供了一种通过将1,2,4,5-四烷基苯供给到装有催化剂层的固定床多管式反应器中进行催化气相氧化来制备均苯四酸二酐的方法。 该方法的特征在于将催化剂层分成至少两层,以分别将催化剂A和催化剂B分别装入反应气体的出口侧的层和原料混合气入口侧的层,或分离催化剂 层至少三层,以分别在反应气体的出口侧,原料混合气体的中间层和入口侧的层与以下催化剂A,催化剂B和催化剂C分别充电:催化剂A:a 含有Va(A)bPcAgd(B)eOx的催化剂,其中(A)表示选自Mo和W中的至少一种元素; (B)表示选自碱金属和碱土金属中的至少一种元素; a至e各自表示其原子序数,催化剂B:含有VaTib(C)c(D)dCeeO x的催化剂,其中(C)表示选自稀土元素(不包括铈)中的至少一种元素; (D)表示选自P,Sb,Hf,Nb,T,B和S中的至少一种元素; a至e和x各自表示其原子序数,催化剂C:含有Va(E)b(F)c(G)dOx的催化剂,其中(E)表示选自碱金属的至少一种元素; (F)表示选自P和Cu中的至少一种元素; (G)表示选自银,硫,钽,硼,钨和钼中的至少一种元素; a至d和x各自表示其原子序数。
    • 3. 发明授权
    • Process for producing pyromellitic anhydride
    • 制备均苯四酸酐的方法
    • US06452021B1
    • 2002-09-17
    • US09963402
    • 2001-09-27
    • Tsukasa TakahashiYasuhisa EmotoEtsushige Matsunami
    • Tsukasa TakahashiYasuhisa EmotoEtsushige Matsunami
    • C07D30777
    • C07C51/235C07C63/307
    • The present invention has for its object to provide a production method of pyromellitic anhydride of high purity in good yield at low cost by catalytic gas-phase oxidation of a 2,4,5-trialkylbenzaldehyde with the aid of a suitable catalyst system. The present invention relates to a production method of pyromellitic anhydride comprising a step for catalytic gas-phase oxidation of a 2,4,5-trialkylbenzaldehyde with a molecular oxygen-containing gas in which said step for catalytic gas-phase oxidation is carried out in the presence of a catalyst such that a specific surface area of the catalytic active component thereof is not greater than 50 m2/g or in the presence of a catalyst containing vanadium as well as molybdenum and/or tungsten as a catalytic active component.
    • 本发明的目的是通过合适的催化剂体系,通过2,4,5-三烷基苯甲醛的催化气相氧化,以低成本提供高纯度的均苯四酸酐的制备方法。 本发明涉及1,2,4,5-苯四酸酐的制备方法,其包括用含有分子氧的气体催化气相氧化2,4,5-三烷基苯甲醛的步骤,其中所述催化气相氧化步骤在存在下进行 的催化剂,使得其催化活性组分的比表面积不大于50m 2 / g,或者在含有钒的催化剂以及钼和/或钨作为催化活性组分的存在下。