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    • 42. 发明授权
    • Use of carbonates in metal ion extraction
    • 在金属离子萃取中使用碳酸盐
    • US5348712A
    • 1994-09-20
    • US15017
    • 1993-02-09
    • Edward T. MarquisMartin J. Plishka
    • Edward T. MarquisMartin J. Plishka
    • C22B3/26C22B3/36C22B11/00C22B43/00
    • C22B3/0036C22B11/04C22B3/0008Y02P10/234
    • It has been discovered that relatively large cyclic and open chain carbonates are extremely efficient in the selective extraction of metal ions, such as gold, silver, platinum and mercury from aqueous solution without the need for a potentially hazardous, organic solvent or use of a corrosive salt, such as NaCl. For example, 1,2-decane carbonate extracted >99.9% mercury, 99.76% gold, 97.5% silver and 79.0% platinum. The homologous 1,2-dodecane carbonate was found to extract 99.9% gold and silver from aqueous solution and 95.8% platinum. Didecyl carbonate extracted 77% gold from aqueous solution. The method of this invention is simpler than prior techniques and eliminates the need for potentially hazardous solvents (toxic, flammable and environmentally unfavorable) and corrosive additives, such as salt, NaCl, used as a salting agent in prior methods.
    • 已经发现,相对大的环状和开链碳酸酯在从水溶液中选择性提取金,离子,金,铂和汞等金属离子时是非常有效的,而不需要有潜在危险的有机溶剂或使用腐蚀性 盐,如NaCl。 例如,1,2-癸烷碳酸酯提取> 99.9%汞,99.76%金,97.5%银和79.0%铂。 发现同源的1,2-十二烷碳酸盐从水溶液中提取99.9%的金和银,并且95.8%的铂。 碳酸二癸酯从水溶液中提取77%的金。 本发明的方法比现有技术更简单,并且消除了在以前的方法中用作盐析剂的潜在危险溶剂(有毒,易燃和环境不利)和腐蚀性添加剂如盐,NaCl的需要。
    • 43. 发明授权
    • Molybdenum recovery
    • 钼回收
    • US5336790A
    • 1994-08-09
    • US154321
    • 1993-11-18
    • Edward T. MarquisHoward F. PaytonRobert A. Meyer
    • Edward T. MarquisHoward F. PaytonRobert A. Meyer
    • B01D3/00C22B34/34C07D301/19C07F11/00
    • C22B34/345Y02P10/23
    • A process for recovery of molybdenum from residual fractions derived from an epoxidation reaction of propylene with tertiary butyl hydroperoxide in liquid phase with tertiary butyl alcohol, in the presence of soluble molybdenum, which process comprises:Fractionating epoxidation reaction product for obtaining a liquid fraction containing essentially all molybdenum from the reaction product;Contacting the liquid fraction with anhydrous ammonia for forming a precipitate containing the major portion of the molybdenum and a liquid phase containing 500 ppm or less molybdenum;Separating the liquid phase from the precipitated solid;Evaporating the liquid phase under conditions of elevated temperatures and reduced pressure in the presence of 1 to 3% water for separation into an evaporator overhead vapor essentially free of molybdenum and an evaporator concentrate comprising essentially all of the molybdenum fed to the evaporator;Rapidly cooling evaporator concentrate from about evaporation temperature to about room temperature or less for converting the evaporator concentrate into a brittle, fracturable solid which is easier to accumulate and dispose of in an environmentally acceptable manner.
    • 在可溶性钼存在下,从丙烯与叔丁基氢过氧化物在液相中与叔丁基氢过氧化物的环氧化反应的残余馏分回收钼的方法,该方法包括:分馏环氧化反应产物,用于获得基本上含有 来自反应产物的所有钼; 将液体馏分与无水氨接触,形成含钼主要部分的沉淀物和含有500ppm以下钼的液相; 将液相与沉淀固体分离; 在1至3%的水存在下,在升高的温度和减压条件下蒸发液相,以分离成基本上不含钼的蒸发器塔顶蒸气和蒸发器浓缩物,其基本上包含进料到蒸发器的所有钼; 将蒸发器浓缩物从大约蒸发温度快速冷却至约室温或更低,以将蒸发器浓缩物转化成脆性,可破碎的固体,其易于以环境可接受的方式积聚和处理。
    • 45. 发明授权
    • Epoxidation process for manufacture of olefin oxide and alcohol
    • US5274138A
    • 1993-12-28
    • US6542
    • 1993-01-21
    • Kenneth P. KeatingEdward T. MarquisMark A. Mueller
    • Kenneth P. KeatingEdward T. MarquisMark A. Mueller
    • B01J31/22C07B61/00C07C29/132C07D301/14C07D301/19C07D303/04
    • C07D301/19C07C29/132Y02P20/52Y02P20/582
    • An epoxidation reaction wherein: an olefin and an organic hydroperoxide, preferably, propylene and tertiary butyl hydroperoxide are reacted in a primary reaction zone in a liquid phase with an organic solvent, preferably tertiary butyl alcohol, in the presence of a soluble molybdenum catalyst at a ratio of propylene to tertiary butyl hydroperoxide of from about 0.9:1 to about 3:1, at a reaction temperature from about 100.degree. C. to about 140.degree. C. and a residence time sufficient to convert about 85 to 95% of the tertiary butyl hydroperoxide and form a primary epoxidation zone reaction product; fractionating, in a primary fractionation zone, the primary zone reaction product into a primary distillate fraction comprising unreacted propylene and propylene oxide and into a primary heavy liquid fraction, comprising molybdenum catalyst, unreacted tertiary butyl hydroperoxide, tertiary butyl alcohol and side reaction products; reacting, in a secondary epoxidation reaction zone, the primary heavy liquid fraction with propylene in the liquid phase, with substantially no back mixing, at a molar ratio of propylene to unreacted tertiary butyl hydroperoxide of about 5:1 to about 10:1, a reaction temperature of about 110.degree. C. to about 140.degree. C. and a residence time sufficient for conversion of substantially all the tertiary butyl hydroperoxide and production of a secondary reaction zone product; fractionating the secondary reaction zone product, in a secondary distillation zone, into a secondary distillate fraction comprising unreacted propylene, and propylene oxide, and into a secondary heavy liquid fraction comprising molybdenum catalyst, tertiary butyl alcohol, and side reaction products; recovering the secondary heavy liquid product for recovery and/or disposal of molybdenum; and fractional distillation of the first distillate fraction and the second distillate fraction for recovery of propylene, and propylene oxide product.