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    • 1. 发明申请
    • Apparatus and Methods for Non-Regenerative and Regenerative Hot Gas Sulfurization
    • 非再生和再生热气体硫化的装置和方法
    • US20080267848A1
    • 2008-10-30
    • US11718864
    • 2005-11-08
    • Maria F. StephanopoulosZheng WangMann Sakbodin
    • Maria F. StephanopoulosZheng WangMann Sakbodin
    • B01D53/48C01F17/00
    • H01M8/0675B01D53/52B01D53/96B01D2251/202B01D2251/204B01D2257/30B01D2259/4009B01J20/0207B01J20/0237B01J20/06B01J20/3433B01J20/3458C10K1/22C10K1/28C10K1/32C10L3/10
    • Disclosed is a doped cerium oxide sorbent that can effectively and regenerably remove H2S in the temperature range of about 500° C. to about 1000° C. Regenerable sorbents (e.g., ZnO, La2O3, CeO2) and methods of using them are disclosed that allow cyclic desulfurization from about 300-500° C., 350-450° C., and at about 400° C. In one embodiment, the present invention relates to a method of desulfurizing fuel gas comprising passing the fuel gas through the sorbent at a space velocity wherein the sulfur compounds are adsorbed substantially on the surface of the sorbent; and regenerating the sorbent by passing a regenerating gas through the sorbent, wherein substantially all of the sulfur compounds are desorbed from the sorbent surface. In a further embodiment, the method of desulfurizing fuel gas further comprises repeating the aforementioned steps while the fuel processor is in operation. In another embodiment, the step of passing the fuel gas may be preceded by reducing the sorbent by passing a reducing gas through the sorbent. In another embodiment, the sorbent may be fully sulfided, i.e., sulfided on its surface and bulk (internally).
    • 公开了一种掺杂的氧化铈吸附剂,其可以在约500℃至约1000℃的温度范围内有效地和可再生地除去H 2 S。可再生的吸附剂(例如ZnO, 公开了使用它们的方法,其允许循环脱硫约300-500℃,350-450℃ 在一个实施方案中,本发明涉及一种使燃料气体脱硫的方法,包括使燃料气体以空间速度通过吸附剂,其中硫化合物基本上吸附在吸附剂的表面上; 以及通过使再生气体通过吸附剂来再生吸附剂,其中基本上所有的硫化合物都从吸附剂表面脱附。 在另一个实施例中,燃料气体脱硫的方法还包括在燃料处理器运行时重复上述步骤。 在另一个实施方案中,通过燃料气体的步骤之前可以通过使还原气体通过吸附剂来还原吸附剂。 在另一个实施方案中,吸附剂可以完全硫化,即在其表面上硫化并且体积(内部)。