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    • 5. 发明授权
    • Conversion of alkanes to oxygenates
    • 烷烃转化为含氧化合物
    • US07064238B2
    • 2006-06-20
    • US10750984
    • 2004-01-02
    • John J. Waycuilis
    • John J. Waycuilis
    • C07C41/01C07C29/00
    • C07C29/124C07B41/00C07C41/01C07C43/043C07C31/04C07C31/08
    • A process is provided for converting an alkane to an oxygenated product by passing an alkane gas over a first fixed bed containing a higher valence bromide salt to produce an alkyl bromide, a hydrobromic acid, and a lower valence bromide salt. The alkyl bromide and hydrobromic acid are conveyed as a gas to a second fixed bed containing a metal oxide and are passed over the second fixed bed to produce the first bromide salt and the oxygenated product. The metal oxide in the second fixed bed is regenerated by passing oxygen over the second fixed bed producing the metal oxide and bromine. The bromine is conveyed as a gas from the second fixed bed to the first fixed bed. The first bromide salt of the first fixed bed is regenerated by passing the bromine over the first fixed bed producing the first bromide salt.
    • 提供了一种通过使烷烃气体通过含有较高价溴化物盐的第一固定床将烷烃转化为氧化产物以产生烷基溴,氢溴酸和低价溴化物盐的方法。 将烷基溴和氢溴酸作为气体输送到含有金属氧化物的第二固定床,并通过第二固定床以产生第一溴化物盐和氧化产物。 第二固定床中的金属氧化物通过使氧气通过第二固定床而再生,产生金属氧化物和溴。 溴作为气体从第二固定床输送到第一固定床。 第一固定床的第一溴化物盐通过将溴通过第一固定床而再生,产生第一溴化物盐。
    • 6. 发明授权
    • Hydrocarbon gas conversion system and process for producing a synthetic
hydrocarbon liquid
    • 碳氢化合物气体转化系统和合成烃液体的制造方法
    • US6130259A
    • 2000-10-10
    • US135821
    • 1998-08-18
    • John J. Waycuilis
    • John J. Waycuilis
    • C01B3/38C07C1/04F23C6/04F23R3/34F23R3/36C07C27/06
    • C01B3/382C10G2/32F23C6/047F23R3/346F23R3/36C01B2203/0244C01B2203/0415C01B2203/062C01B2203/0844C01B2203/0883C01B2203/0894C01B2203/1052C01B2203/1241C01B2203/127C01B2203/1276C01B2203/141C01B2203/142C01B2203/148C01B2203/1604C01B2203/82C01B2203/84F23C2201/301Y02P20/123Y02P20/124
    • A system and process are provided for converting a light hydrocarbon gas to a synthetic heavier hydrocarbon liquid. The system includes an autothermal reformer, a Fischer-Tropsch reactor and a Brayton cycle that are structurally and functionally integrated. In the practice of the process, a mixture of a hydrocarbon feed gas, a compressed air feed and process steam is fed to the autothermal reformer to produce a synthesis gas. The synthesis gas is fed to the Fischer-Tropsch reactor where it is catalytically reacted to produce heavy hydrocarbons. The outlet from the Fischer-Tropsch reactor is separated into water, a low heating value tail gas, and the desired hydrocarbon liquid product. The water is pressurized and heated to generate process steam. The tail gas is heated and fed with compressed air and steam to the Brayton cycle having a combustor and a series of power turbines and compressors. The tail gas and air feed are burned in the combustor to produce a combustion gas that is used to drive a power turbine linked by a shaft to an air compressor, thereby driving the air compressor. The system further includes a plurality of heat exchangers that enable heat to be recovered from the outlet of the autothermal reformer. The recovered heat is used to make the process steam as well as to preheat the hydrocarbon feed gas before it is fed to the autothermal reformer, preheat the synthesis gas before it is fed to the Fischer-Tropsch reactor and preheat the tail gas before it is fed to the combustor.
    • 提供了一种用于将轻烃气体转化为合成较重烃液体的系统和方法。 该系统包括结构和功能集成的自热重整器,费 - 托反应器和布雷顿循环。 在该方法的实践中,将烃​​进料气体,压缩空气进料和工艺蒸汽的混合物供给到自热重整器以产生合成气。 将合成气送入费 - 托反应器,在其中催化反应生成重质烃。 费 - 托反应器的出口被分离成水,低热值尾气和所需的烃液体产物。 水被加压和加热以产生工艺蒸汽。 尾气被加热,并将压缩空气和蒸汽送入具有燃烧器和一系列动力涡轮机和压缩机的布雷顿循环。 尾气和空气进料在燃烧器中燃烧以产生用于将由轴连接的动力涡轮机驱动到空气压缩机的燃烧气体,从而驱动空气压缩机。 该系统还包括多个热交换器,其使热能够从自热重整器的出口回收。 回收的热量用于制造工艺蒸汽,以及在将烃进料气体进料到自热重整器之前对其进行预热,在将合成气送入费 - 托反应器之前对其进行预热,并在尾气预热之前预热尾气 进料到燃烧器。