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    • 1. 发明授权
    • Production of mixtures of methylenedianiline and its higher homologues using calcined metal oxide-silica catalysts
    • 使用煅烧金属氧化物 - 二氧化硅催化剂生产亚甲基二苯胺及其高级同系物的混合物
    • US08558027B2
    • 2013-10-15
    • US13058603
    • 2009-08-14
    • Heiko WeinerDavid C. MolzahnRobert J. Gulotty, Jr.
    • Heiko WeinerDavid C. MolzahnRobert J. Gulotty, Jr.
    • C07C211/00
    • C07C209/78B01J21/12B01J35/002B01J37/0009B01J37/033B01J37/036B01J37/08C07C211/50
    • The present disclosure relates to compositions, systems, and methods of forming an amine (e.g., methylenedianiline (MDA)) using an acid catalyst including, for example, a metal oxide-silica catalyst calcined at temperature(s) of about ≧500° C. to form a solid acid silica-metal oxide catalyst. A metal oxide of a solid acid silica-metal oxide catalyst may comprise alumina. A process for making a solid acid silica-metal oxide catalyst may comprise calcining an amorphous alumina-silica material at temperature(s) of about ≧500° C. and/or under an anhydrous and/or inert atmosphere. A rearrangement reaction of the condensation product of aniline and formaldehyde in the presence of a solid acid silica-metal oxide catalyst may yield more MDA and/or more desirable isomer(s) of MDA than reactions performed with a corresponding catalyst calcined at temperature(s) of less than 500° C.
    • 本公开内容涉及使用酸催化剂形成胺(例如亚甲基二苯胺(MDA))的组合物,体系和方法,所述酸催化剂包括例如在大约> 500℃的温度下煅烧的金属氧化物 - 二氧化硅催化剂 C.形成固体酸二氧化硅 - 金属氧化物催化剂。 固体二氧化硅 - 金属氧化物催化剂的金属氧化物可以包含氧化铝。 制备固体酸性二氧化硅 - 金属氧化物催化剂的方法可以包括在约> = 500℃的温度和/或在无水和/或惰性气氛下煅烧无定形氧化铝 - 二氧化硅材料。 在固体酸二氧化硅 - 金属氧化物催化剂存在下,苯胺和甲醛的缩合产物的重排反应可以产生更多的MDA和/或更理想的MDA异构体,而不是用相对应的在 )小于500℃
    • 6. 发明授权
    • Catalytic reforming of alkyleneamines to linearly-extended
polyalkylenepolyamines
    • 将亚烷基胺催化重整成线性延伸的聚亚烷基多胺
    • US5118850A
    • 1992-06-02
    • US611244
    • 1990-11-09
    • Robert G. BowmanDavid C. MolzahnGeorge E. Hartwell
    • Robert G. BowmanDavid C. MolzahnGeorge E. Hartwell
    • C07C209/64
    • C07C209/64
    • A process for reforming alkyleneamines to predominantly linearly-extended polyalkylenepolyamines comprising contacting an alkyleneamine or mixture thereof with a catalyst under conditions such that a mixture of polyalkylenepolyamines enriched in linearly-extended products is formed, said catalyst containing at least one compound selected from the group consisting of (a) Group VB metal oxides, (b) Group VB metal phosphates, (c) silicates of Groups IIA, IIIB, IVB, VB, and the lanthanide and actinide metals, and (d) tungsten oxdies, with the proviso that the silicates and tungsten oxides are essentially free of aluminum. For example, ethylenediamine is contacted with a catalyst of niobium phosphate or niobic acid under reaction conditions to yield predominantly non-cyclic polyethylenepolyamines.
    • 一种将亚烷基胺重整为线性延伸的聚亚烷基多胺的方法,包括在形成富含线性延伸产物的多亚烷基多胺的混合物的条件下使亚烷基胺或其混合物与催化剂接触,所述催化剂含有至少一种选自以下的化合物: (a)VB族金属氧化物,(b)VB族金属磷酸盐,(c)IIA,IIIB,IVB,VB族和镧系元素和锕系金属的硅酸盐,(d)钨氧化物,条件是 硅酸盐和钨氧化物基本上不含铝。 例如,乙二胺在反应条件下与磷酸铌或铌酸的催化剂接触,主要产生非环状聚亚乙基多胺。
    • 9. 发明申请
    • PROCESS FOR THE CONVERSION OF ALIPHATIC CYCLIC AMINES TO ALIPHATIC DIAMINES
    • 脂肪酸环糊精转化成脂肪酸的方法
    • US20120116122A1
    • 2012-05-10
    • US13383525
    • 2010-07-30
    • Shawn D. FeistDaniel A. HickmanErich J. MolitorDavid C. MolzahnStacie SanthanyAbraham D. Schuitman
    • Shawn D. FeistDaniel A. HickmanErich J. MolitorDavid C. MolzahnStacie SanthanyAbraham D. Schuitman
    • C07C209/62C07C211/12C07C211/18
    • C07C209/62C07C211/12C07C211/18C07C2601/14
    • The instant invention is a process for the conversion of aliphatic cyclic amines to aliphatic diamines. The process for conversion of aliphatic cyclic amines to aliphatic diamines comprises the steps of: (1) selecting one or more cyclic amines; (2) contacting said one or more cyclic amines with ammonia and hydrogen, optionally water, and optionally one or more solvents in the presence of one or more heterogeneous metal based catalyst systems at a temperature in the range of from 120° C. to about 250° C. and a pressure in the range of from 700 to 3500 psig for a period in the range of at least one hour or more in one or more reactor systems; (3) forming a product mixture comprising one or more aliphatic diamine, optionally a portion of said one or more cyclic amines, optionally a portion of said ammonia, optionally a portion of said hydrogen, optionally water, and optionally a portion of said one or more solvents; (4) removing said product mixture from the reactor system; (5) removing at least a portion of said portion of ammonia, said portion of hydrogen, or mixture thereof from said product mixture via distillation; (6) removing at least a portion of said portion of water via distillation; (7) removing at least a portion of said portion of one or more optional solvents via distillation; (8) removing at least a portion of said portion of one or more cyclic amines; (9) thereby separating said one or more aliphatic diamines from said product mixture; and (10) thereby converting said one or more cyclic amines to one or more aliphatic diamines.
    • 本发明是将脂族环胺转化为脂族二胺的方法。 将脂族环胺转化为脂肪族二胺的方法包括以下步骤:(1)选择一种或多种环胺; (2)在一种或多种非均相金属基催化剂体系的存在下,在120℃至约20℃的温度下,使所述一种或多种环胺与氨和氢,任选的水,以及任选的一种或多种溶剂接触。 250℃,压力范围为700-300psig,在一个或多个反应器系统中至少1小时以上; (3)形成包含一种或多种脂族二胺,任选地一部分所述一种或多种环胺,任选地一部分所述氨,任选地一部分所述氢,任选的水,以及任选地一部分所述一种或多种 更多溶剂; (4)从反应器系统中除去所述产物混合物; (5)通过蒸馏从所述产物混合物中除去所述部分氨,所述部分氢或其混合物的至少一部分; (6)通过蒸馏除去所述部分水的至少一部分; (7)通过蒸馏除去一种或多种任选溶剂的所述部分的至少一部分; (8)除去一种或多种环胺的所述部分的至少一部分; (9),从而将所述一种或多种脂族二胺与所述产物混合物分离; 和(10),从而将所述一种或多种环胺转化为一种或多种脂族二胺。