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High temperature gas desulfurization with elemental sulfur production

机译:高温气体脱硫并产生单质硫

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摘要

Preliminary results on the use of cerium oxide as a high-temperature desulfurization sorbent are pressented.The primary advantage of cerium over current zinc-based sorbents is the potential to produce elemental sulfur during the regeneration phase of the process.Although CeO_2 is less effective for H_2S removal during sulfidation,the sulfided product,Ce_2O_2S,will react with SO_2 to produce elemental sulfur directly.Rapid and complete regeneration is possible over the range of 500 to 700 degC,and only elemental sulfur is formed.Elemental sulfur concentrations(considered as S_2)as large as 20mol% have been droduced in the regeneration product.The sorbent has been subjected to ten sulfidation-regeneration cycles using a laboratory-scale fixed-bed reactor with negligible activity loss Effectively complete conversion of CeO_2 to Ce_2O_2S during sulfidation and subsequent regeneration to CeO_2 was achieved ineach cycle.A two-stage desulfurization process using CeO_2 for bulk H_2S removal followed by a zinc sorben polishing step has been proposed to meet specifications of the integrated gasification combined cycle(IGCC) process.Economic comparison with a single-stage dusulfurization process using zinc sorbent followed by elemental sulfur recovery using the direct sulfur recovery process(DSRP) shows that the two-stage cerium process may be less costly if the cerium sorbent is sufficiently durable.
机译:迫切需要使用氧化铈作为高温脱硫吸附剂的初步结果。与目前的锌基吸附剂相比,铈的主要优点是在该过程的再生阶段可能产生元素硫。硫化过程中除去H_2S,硫化产物Ce_2O_2S与SO_2直接反应生成单质硫。在500-700℃范围内可以快速,完全地再生,仅形成单质硫。单质硫的浓度(称为S_2)吸附剂在再生产物中的含量高达20mol%。吸附剂已使用实验室规模的固定床反应器进行了十次硫化再生循环,活性损失可忽略不计在硫化和后续再生过程中有效地将CeO_2完全转化为Ce_2O_2S在每个循环中都实现了对CeO_2的脱除。利用CeO_2进行两步脱硫的过程有人建议采用锌吸附剂抛光步骤以满足整体气化联合循环(IGCC)工艺的要求。采用锌吸附剂的单级二硫化工艺与直接硫回收工艺(DSRP)进行元素硫的经济比较结果表明,如果铈吸附剂具有足够的耐久性,则两阶段铈工艺的成本可能更低。

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