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Polishing H(2)S from coal gasification streams using a high temperature electrochemical membrane separation process.

机译:使用高温电化学膜分离工艺从煤气化流中抛光H(2)S。

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Coal may be used to generate electrical energy by any of several processes, most of which involve combustion or gasification. Combustion in a coal-fired boiler and power generation using a steam-cycle is the conventional conversion method; however total energy conversion efficiencies for this type of process are only slightly over 30%. Integration of a gas-cycle in the process (combined cycle) may increase the total conversion efficiency to 40%. Conversion processes based on gasification offer efficiencies above 50%.; H{dollar}sb2{dollar}S is the predominant gaseous contaminant in raw coal gas. Coal depending on the type and area of extraction can contain up to 5 wt% sulfur, which is converted to gaseous H{dollar}sb2{dollar}S during gasification. Problems arise due to the corrosive nature of H{dollar}sb2{dollar}S on metal components contained in these cycles. Because of this, H{dollar}sb2{dollar}S concentrations must be reduced to low levels corresponding to certain power applications. For example, an integrated coal gasification-combined cycle (IGCC) process producing electricity from coal at nearly 50% overall efficiency incorporates gas turbines that cannot tolerate H{dollar}sb2{dollar}S levels above 100 ppm. Coal gasification/Molten Carbonate Fuel-Cell (MCFC) systems, achieving conversion efficiencies around 60%, function properly only if H{dollar}sb2{dollar}S is below 1 ppm.; An advanced process for the separation of hydrogen sulfide (H{dollar}sb2{dollar}S) from coal gasification product streams through an electrochemical membrane is being perfected. H{dollar}sb2{dollar}S is removed from the syn-gas stream, split into hydrogen, which enriches the exiting syn-gas, and sulfur, which is condensed from an inert sweep gas stream. The process allows removal of H{dollar}sb2{dollar}S without cooling the gas stream and with negligible pressure loss through the separator. The process is made economically attractive by the lack of need for a Claus process for sulfur recovery. To this extent the project presents a novel concept for improving utilization of coal for more efficient power generation.
机译:煤可通过多种过程中的任何一种来产生电能,其中大多数涉及燃烧或气化。传统的转换方法是在燃煤锅炉中燃烧和使用蒸汽循环发电。但是,此类过程的总能量转换效率仅略高于30%。将气体循环集成到过程中(联合循环)可以将总转化效率提高到40%。基于气化的转化过程可提供50%以上的效率。 H {dollar} sb2 {dollar} S是原煤气中的主要气态污染物。煤取决于提取的类型和面积,最多可包含5 wt%的硫,硫在气化过程中会转化为气态H {sb2 {dollar} S。由于这些循环中所含的金属成分上的H {sb2} {b} {S}具有腐蚀性,因此产生了问题。因此,必须将H {sb2 {dollar} S的浓度降低到与某些电源应用相对应的低水平。例如,以总效率接近50%的效率从煤发电的集成煤气化联合循环(IGCC)工艺中,燃气轮机无法承受100 ppm以上的Hs(sb2s)。煤气化/熔融碳酸盐燃料电池(MCFC)系统,只有在H {dollar} sb2 {dollar} S低于1 ppm时,才能实现约60%的转换效率。完善了一种通过电化学膜从煤气化产物流中分离硫化氢(H {dollar} sb2 {dollar} S)的先进方法。从合成气流中除去H {sb2 {dollar} S,将其分解成氢气和硫,后者从惰性吹扫气流中冷凝,所述氢气富集排出的合成气,而硫则被富集。该方法允许在不冷却气流和通过分离器的压力损失可忽略的情况下除去Hsb2s。由于不需要用于回收硫的克劳斯方法,因此该方法在经济上具有吸引力。在这个程度上,该项目提出了一种新颖的概念,可以改善煤炭的利用,从而提高发电效率。

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