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    • 4. 发明授权
    • Method of producing alcohols
    • 醇的生产方法
    • US08227647B2
    • 2012-07-24
    • US12927936
    • 2010-11-30
    • Jorge MillerLuisa Kling Miller
    • Jorge MillerLuisa Kling Miller
    • C07C29/48C07C27/16
    • C07C29/095C07C17/10C07C67/11C07C19/075C07C31/04C07C69/06
    • A method comprising reacting an alkane gas with a halogen gas in a halogenations reactor to form a halogenation reaction product mixture comprising alkane halide and hydrogen halide mixture; mixing the halogenations reaction product mixture with a countercurrent flow of a metal organic salt thereby forming an extractor product mixture of a metal halide, organic salt, and organic acid separating the organic ester and organic acid mixture from the metal halide; oxygenating the metal halide to form a metal oxide and halide containing gasses; separating the metal oxide from the halide containing gasses; mixing the metal oxide with water to form a metal oxide slurry; mixing the metal oxide slurry with a countercurrent flow of the organic ester and organic acid mixture to form a raw product comprising alkanol, a metal organic salt is provided.
    • 一种方法,包括在卤化反应器中使烷烃气体与卤素气体反应以形成卤化反应产物混合物,其包含烷烃卤化物和卤化氢混合物; 将卤化反应产物混合物与金属有机盐的逆流混合,从而形成金属卤化物,有机盐和有机酸的萃取产物混合物,从有机酯和有机酸混合物中分离出金属卤化物; 使金属卤化物氧化以形成金属氧化物和含卤气的气体; 从含卤化物气体中分离金属氧化物; 将金属氧化物与水混合以形成金属氧化物浆料; 将金属氧化物浆料与有机酯和有机酸混合物的逆流混合以形成包含链烷醇,金属有机盐的粗产物。
    • 5. 发明申请
    • PROCESS AND PLANT FOR PRODUCING SYNTHESIS GAS
    • 生产合成气的工艺和设备
    • US20090105356A1
    • 2009-04-23
    • US12300683
    • 2007-05-10
    • Andreas BormannDierk Muller
    • Andreas BormannDierk Muller
    • C07C27/16C10J3/48
    • C01B3/382C01B2203/0233C01B2203/0244C01B2203/061C01B2203/068C01B2203/1241C01B2203/127C01B2203/141C01B2203/143
    • When producing synthesis gas from a starting material containing hydrocarbons, in particular natural gas, a feed stream of the starting material is divided into a first partial stream and a second partial stream. The first partial stream is supplied to a steam reformer (4), in which together with steam it is catalytically converted to a gas stream containing carbon oxides. Then, the first partial stream is again combined with the second partial stream and the combined gas stream is supplied to an autothermal reformer (7), in which together with gas rich in oxygen it is autothermally reformed to a synthesis gas in the presence of a cracking catalyst. Processing a starting material with a high content of higher hydrocarbons is made possible in that before the steam reformer (4) and before the autothermal reformer (7) the entire starting material is supplied to a pre-reformer (2) in which the starting material largely is liberated from higher hydrocarbons.
    • 当从含有烃,特别是天然气的原料生产合成气时,原料的进料流被分成第一部分流和第二部分流。 将第一部分流供应到蒸汽重整器(4),其中蒸汽与蒸汽一起被催化转化成含有碳氧化物的气流。 然后,将第一部分流再次与第二部分流合并,将合并的气流供应至自热重整器(7),其中与富含氧气的气体一起,在有气体的情况下自动重整成合成气 裂化催化剂。 加工具有高含量高烃的原料是可能的,因为在蒸汽重整器(4)之前和自热重整器(7)之前,将整个起始原料供应到预重整器(2),其中原料 主要是从高级碳氢化合物中释放出来的。