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    • 32. 发明授权
    • Preparation of alkenes and cycloalkenes
    • 烯烃和环烯烃的制备
    • US4570025A
    • 1986-02-11
    • US744703
    • 1985-06-14
    • Gerhard P. NowackMarvin M. Johnson
    • Gerhard P. NowackMarvin M. Johnson
    • B01J27/16C07C5/05C07C5/03
    • B01J27/16C07C5/05C07C2523/44C07C2527/167
    • In one embodiment, an alkadiene and/or alkatriene is contacted with a free hydrogen containing gas in the presence of a catalyst composition comprising (a) palladium metal and (b) aluminum phosphate, so as to form primarily an alkene. In another embodiment, a cycloalkadiene and/or cycloalkatriene is contacted with a free hydrogen containing gas in the presence of a catalyst composition comprising (a) palladium metal and (b) aluminum phosphate, so as to form primarily a cycloalkene. The preferred cycloalkadiene is 1,5-cyclooctadiene, and the preferred cycloalkene is cyclooctene. Optionally, an alkali metal alkoxide, e.g. lithium methoxide, and/or carbon monoxide can be present during the hydrogenation reactions to improve the selectivity to alkenes and cycloalkenes, respectively.
    • 在一个实施方案中,在包含(a)钯金属和(b)磷酸铝的催化剂组合物的存在下,使烯二烯和/或亚三烯与含游离氢的气体接触,以便主要形成烯烃。 在另一个实施方案中,在包含(a)钯金属和(b)磷酸铝的催化剂组合物存在下,将环二烯和/或环亚烷基三烯与含游离氢的气体接触,以便主要形成环烯烃。 优选的环二烯是1,5-环辛二烯,优选的环烯是环辛烯。 任选地,可以使用碱金属醇盐。 在氢化反应期间可以存在甲醇锂和/或一氧化碳,以分别提高对烯烃和环烯烃的选择性。
    • 38. 发明授权
    • De-ashing lubricating oils
    • 脱灰润滑油
    • US4247389A
    • 1981-01-27
    • US92138
    • 1979-11-07
    • Marvin M. JohnsonGerhard P. NowackDonald C. Tabler
    • Marvin M. JohnsonGerhard P. NowackDonald C. Tabler
    • C10G29/00C10G29/02C10G67/02C10M175/00C10N40/00C10N40/08C10N40/25C10M11/00
    • C10M175/0016C10G2400/10
    • A process for the production of an essentially ash-free oil stock from a lubricating oil containing ash-forming components comprising(a) contacting said lubricating oil with an aqueous ammonium salt treating agent;(b) removing a major portion of the water from the mixture resulting from combining said aqueous solution and said lubricating oil;(c) heating at least a portion of the product resulting from step (b) at a temperature in the range of about 320.degree. to about 420.degree. C. for a period of time sufficient to decompose at least a portion of any ammonium salts of sulfonic acid and dialkyldithiophosphoric acid that are contained therein;(d) cooling the product from step (c) to a temperature in the range of about 150.degree. to about 180.degree. C.; and(e) separating the solids from the product of step (d), optionally with subsequent hydrotreating and stripping of the oil thus obtained.
    • 一种从含有成灰组分的润滑油中生产基本上不含灰分的油料的方法,包括(a)使所述润滑油与铵盐处理剂接触; (b)从混合所述水溶液和所述润滑油得到的混合物中除去大部分水; (c)将步骤(b)产生的产物的至少一部分在约320℃至约420℃的温度范围内加热足够的时间以分解至少一部分任何铵盐 磺酸和二烷基二硫代磷酸; (d)将步骤(c)中的产物冷却至约150至约180℃的温度; 和(e)从步骤(d)的产物中分离固体,任选地随后加氢处理和汽提如此获得的油。