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    • 5. 发明授权
    • Catalyst comprising amorphous NiO on silica/alumina support
    • 包含在二氧化硅/氧化铝载体上的无定形NiO的催化剂
    • US5169824A
    • 1992-12-08
    • US644998
    • 1991-01-22
    • Ramzi Y. SalehStuart L. SoledNicholas C. Dispenziere
    • Ramzi Y. SalehStuart L. SoledNicholas C. Dispenziere
    • B01J23/755B01J37/02B01J37/03
    • B01J37/0217B01J23/755B01J37/031
    • The present invention provides for a catalyst composition which is effective for use in the production of dimer products and higher olefin products from lower olefins such as propylene and butene in high yields and with an average degree of branching in the dimer products of less than about 1.6 methyl groups per molecule, generally in the range of from about 1.0 to 1.4 methyl groups per molecule. The present invention also provides a process for producing such dimer and higher olefin products using the catalyst composition of this invention. The catalyst of the invention comprises an amorphous nickel oxide (NiO) present as a disperse substantial monolayer on the surfaces of a silica (SiO.sub.2) support, which support also contains minor amounts of an oxide of aluminum, gallium or indium such that the ratio of NiO to metal oxide present in the catalyst is within the range of from about 4:1 to about 100:1. The catalyst may be prepared by precipitating a water insoluble nickel salt onto the surfaces of a silica support which has been impregnated with the metal oxide or onto a silica-alumina support which has been dealuminized such that the resulting nickel oxide/alumina ratio will fall within the ranges set forth above. The catalyst may then be activated by calcination in the presence of oxygen at a temperature within the range of from about 500.degree. to 700.degree. C.
    • 本发明提供了一种催化剂组合物,其有效用于以高产率从低级烯烃如丙烯和丁烯生产二烯体产物和高级烯烃产物,并且二聚体产物中的平均支化度小于约1.6 每个分子的甲基基团,通常在每分子约1.0至1.4个甲基的范围内。 本发明还提供了使用本发明的催化剂组合物生产这种二聚物和较高级烯烃产物的方法。 本发明的催化剂包括在二氧化硅(SiO 2)载体的表面上作为分散实质单层存在的无定形氧化镍(NiO),该载体还含有少量的铝,镓或铟的氧化物, 存在于催化剂中的NiO与金属氧化物在约4:1至约100:1的范围内。 催化剂可以通过将水不溶性镍盐沉淀到已经浸渍有金属氧化物的二氧化硅载体的表面上或已经脱铝的二氧化硅 - 氧化铝载体上,使得所得到的氧化镍/氧化铝比落入 上述范围。 催化剂然后可以在氧的存在下在约500-700℃的温度下煅烧来活化。
    • 6. 发明授权
    • Aquathermolytic cleavage of ethers
    • 醚水解裂解
    • US5043486A
    • 1991-08-27
    • US572485
    • 1990-08-23
    • Michael SiskinGlen B. BronsRamzi Y. SalehStephen N. Vaughn
    • Michael SiskinGlen B. BronsRamzi Y. SalehStephen N. Vaughn
    • C07C29/10C07C31/02C07C31/10C07C31/12
    • C07C29/10
    • The present invention provides for a simplified process for converting ethers into their corresponding alcohols comprising forming an aqueous mixture of the ether and at least about 50% by weight water and heating the mixture under autogeneous pressure at a temperature of from about 250.degree. to 450.degree. C., more preferably from about 250.degree. C. up to the critical temperature of water which is about 374.degree. C. Heating is continued for a period of time sufficient to convert at least about 20% by weight of the ether, usually from about 5 up to about 120 minutes, depending on temperature and the amount of water present, and the identity of the starting ether feedstock.The process may be characterized as an aquathermolysis reaction wherein the reaction proceeds in water primarily through ionic routes rather than through free radical routes. Accordingly, relatively high conversion rates and good yields of alcohol and other reaction by-products may be obtained without the necessity of using a catalyst in the process.
    • 本发明提供了将醚转化成其相应的醇的简化方法,包括形成醚的水性混合物和至少约50重量%的水,并在约250-450℃的温度下在自主压力下加热混合物 更优选约250℃至约374℃的水的临界温度。继续加热足够的时间以使至少约20重量%的乙醚转化成通常为约 5至约120分钟,这取决于温度和存在的水的量以及起始醚原料的特性。 该方法可以表征为水解溶解反应,其中反应在水中主要通过离子路线而不是通过自由基途径进行。 因此,可以获得醇和其它反应副产物的相对高的转化率和良好的产率,而不需要在该方法中使用催化剂。