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    • 3. 发明授权
    • Olefin epoxidation of olefins in a polar medium
    • 烯烃在极性介质中的烯烃环氧化
    • US4891437A
    • 1990-01-02
    • US133664
    • 1987-12-16
    • Edward T. MarquisKenneth P. KeatingJohn F. KniftonWilliam A. SmithJohn R. SandersonJonathan Lustri
    • Edward T. MarquisKenneth P. KeatingJohn F. KniftonWilliam A. SmithJohn R. SandersonJonathan Lustri
    • C07D301/19C07D303/04
    • C07D301/19C07D303/04
    • A hydroperoxide charge stock (t-butyl hydroperoxide or t-amyl hydroperoxide) is reacted with a C.sub.3 to C.sub.20 olefin charge stock in liquid phase in a reaction zone in the presence of a catalytically effective amount of a soluble molybdenum catalyst to form a product olefin epoxide corresponding to the olefin charge stock and a product alcohol corresponding to the hydroperoxide charge (t-butyl alcohol or t-amyl alcohol), which process is improved in accordance with the present invention by maintaining a reaction medium composed of more than 60 wt % of polar components (hydroperoxide charge stock, product alcohol and product epoxide) in the reaction zone by charging to the reaction zone at least about a 30 wt % solution of the hydroperoxide charge stock in the corresponding product alcohol and charging said olefin charge stock to said reaction zone in an amount relative to the amount of said charged solution of charged hydroperoxide in product alcohol sufficient to provide a ratio of from about 0.5 to about 2 moles of charged olefin per mole of charged hydroperoxide.The preferred olefin charge stock is propylene and the preferred hydroperoxide charge stock is t-butyl hydroperoxide. The corresponding epoxide in this situation is propylene oxide and the corresponding product alcohol is t-butyl alcohol.
    • 在催化有效量的可溶性钼催化剂的存在下,将氢过氧化物电荷原料(叔丁基过氧化氢或叔戊基过氧化氢)与液相中的C3至C20烯烃加料原料在反应区中反应以形成产物烯烃 对应于烯烃电荷原料的环氧化物和对应于氢过氧化物电荷的产物醇(叔丁醇或叔戊醇),根据本发明,通过保持由60重量%以上的反应介质组成的反应介质, 的反应区中的极性组分(氢过氧化物电荷原料,产物醇和产物环氧化物)通过向反应区中加入至少约30重量%的氢过氧化物电荷原料在相应产物醇中的溶液,并将所述烯烃电荷原料装入所述 反应区的量相对于产物醇中充入的氢过氧化物的所述带电溶液的量足以提供从ab的比例 每摩尔加入的氢过氧化物中含有0.5至约2摩尔的带电烯烃。 优选的烯烃电荷原料是丙烯,优选的氢过氧化物电荷原料是叔丁基过氧化氢。 在这种情况下相应的环氧化物是环氧丙烷,相应的产物醇是叔丁醇。
    • 6. 发明授权
    • Synthesis of ammonium molybdate/alkanol complexes
    • 钼酸铵/烷醇络合物的合成
    • US4650886A
    • 1987-03-17
    • US804131
    • 1985-12-06
    • Edward T. MarquisJohn R. SandersonKenneth P. KeatingWilliam A. Smith
    • Edward T. MarquisJohn R. SandersonKenneth P. KeatingWilliam A. Smith
    • B01J31/18B01J31/22C07D301/19C07F11/00
    • C07D301/19B01J31/2208B01J31/2226B01J2231/72B01J2531/64
    • Storage stable solutions of molybdenum/alkanol complexes in the alkanol are prepared by reacting an ammonium molybdate with an amount of a straight chain or branched chain C.sub.6 -C.sub.13 alkanol, within the range of about 7 to about 20 moles of alkanol per gram atom of molybdenum sufficient to form a storage stable molybdenum/alkanol complex. The complex-forming reaction is initiated in the presence of about 1 to about 4 moles of added water per gram atom of molybdenum and is conducted at a temperature of about 120.degree. to about 190.degree. C. for a period of time, normally about 3 to about 8 hours, sufficient to substantially completely remove ammonia and water to provide a liquid reaction product comprising said solution of molybdenum/alkanol complex dissolved in unreacted alkanol and containing about 0.001 to about 0.1 wt. % of water. The reaction product is filtered to provide a clarified storage stable solution of the molybdenum/alkanol complex.
    • 通过使钼酸铵与一定量的直链或支链C 6 -C 13烷醇在约7至约20摩尔的链烷醇/克原子钼的范围内反应来制备钼/烷醇配合物在烷醇中的储存稳定溶液 足以形成储存稳定的钼/烷醇络合物。 络合物形成反应在每克原子钼约1至约4摩尔加入水存在下开始,并在约120℃至约190℃的温度下进行一段时间,通常约3 至约8小时,足以基本上完​​全除去氨和水,以提供液体反应产物,其包含溶解在未反应的链烷醇中的钼/烷醇络合物溶液,并含有约0.001至约0.1wt。 %的水。 将反应产物过滤以提供钼/烷醇复合物的澄清储存稳定溶液。
    • 8. 发明授权
    • Synthesis of molybdenum oxide/alkanol complexes
    • 氧化钼/烷醇络合物的合成
    • US4654427A
    • 1987-03-31
    • US804132
    • 1985-12-06
    • Edward T. MarquisJohn R. SandersonKenneth P. KeatingWilliam A. Smith
    • Edward T. MarquisJohn R. SandersonKenneth P. KeatingWilliam A. Smith
    • B01J31/22C07D301/19C07F11/00
    • C07D301/19B01J31/2208B01J31/2226B01J2231/72B01J2531/64
    • Storage stable solutions of molybdenum/alkanol complexes in the alkanol are prepared by reacting a molybdenum oxide and ammonium hydroxide and an amount of a straight chain or branched chain C.sub.6 -C.sub.13 alkanol, within the range of about 10 to about 55 moles of alkanol per gram atom of molybdenum sufficient to form a storage stable molybdenum/alkanol complex. The complex-forming reaction is initiated in the presence of about 1 to about 4 moles of water per gram atom of molybdenum and about 0.5 to about 10 moles of ammonia per gram atom of molybdenum, the water and ammonia preferably being added in the form of concentrated ammonium hydroxide. The reaction is conducted at a temperature of about 120.degree. to about 190.degree. C. for a period of time, normally about 3 to about 8 hours, sufficient to substantially completely remove ammonia and water to provide a liquid reaction product comprising said solution of molybdenum/alkanol complex dissolved in unreacted alkanol and containing about 0.001 to about 0.1 wt. % of water. The reaction product is filtered to provide a clarified storage stable solution of the molybdenum/alkanol complex having a dissolved molybdenum content of about 3 to about 10.5 wt. %.
    • 钼/烷醇配合物在烷醇中的储存稳定溶液是通过使氧化钼和氢氧化铵与一定量的直链或支链C 6 -C 13烷醇在约10-约55摩尔的链烷醇/克 足以形成储存稳定的钼/烷醇络合物的钼原子。 在约1至约4摩尔水/克原子钼和约0.5至约10摩尔氨/克原子钼的存在下引发络合物形成反应,优选以水和氨的形式加入水和氨 浓氢氧化铵。 反应在约120℃至约190℃的温度下进行一段时间,通常约3至约8小时,足以基本上完​​全除去氨和水,以提供包含所述钼溶液的液体反应产物 /链烷醇络合物溶解在未反应的链烷醇中并含有约0.001至约0.1wt。 %的水。 将反应产物过滤以提供溶解的钼含量为约3至约10.5重量%的钼/烷醇络合物的澄清储存稳定溶液。 %。