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The effect of methanol in the first catalytic converter of the Claus sulfur recovery unit

机译:甲醇在克劳斯硫磺回收装置的第一个催化转化器中的作用

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Methanol is commonly used as a hydrate inhibitor in gathering and transportation systems for natural gas streams containing H2S. While efforts are made to prevent carryover, some residual methanol can end up reaching downstream facilities. If residual methanol is still present in an acid gas stream after amine separation from sales gas, it normally undergoes quantitative conversion to CO and H-2 in the front-end thermal reactor of the Claus sulfur recovery unit. However, if the Claus sulfur recovery unit is operating in a split-flow configuration in such a scenario, some acid gas, and the corresponding methanol, bypasses the thermal reactor and gets introduced directly to the first catalytic converter. While the fate of methanol in the thermal reactor of a Claus sulfur recovery unit has been established, an understanding of methanol reactivity and influence within the first catalytic converter is lacking. To shed light on this issue, we have performed a series of laboratory experiments, simulating field conditions, that elucidate the effect of methanol in the first catalytic converter of a Claus sulfur recovery unit, which can contain titania (TiO2) and/or alumina (Al2O3) catalysts. The results obtained identify that methanol is converted to CS2, via a CH3SH intermediate, which is then hydrolyzed to form H2S and CO2. Strategically designed experiments support this methanol conversion mechanism over both Al2O3 and TiO2. Although catalyst discoloration was observed in some experiments with methanol, no significant catalyst deactivation was observed, where CS2 conversion was monitored as a method for assessing activity once steady-state had been reached. Results from catalyst surface area analyses agreed with these observations. Finally, it was also found that there was no change in the carbon content of the sulfur formed during experiments where methanol was present when compared to control experiments without methanol addition to the feed.
机译:甲醇通常在含H2S天然气流的收集和运输系统中用作水合物抑制剂。在尽力防止残留的同时,一些残留的甲醇可能最终到达下游设施。如果从销售气体中分离胺后,酸性气体流中仍残留甲醇,则通常在克劳斯硫磺回收装置的前端热反应器中将其定量转化为CO和H-2。但是,如果在这种情况下克劳斯硫磺回收装置以分流配置运行,则某些酸性气体和相应的甲醇将绕过热反应器,并直接引入第一催化转化器。虽然已经确定了克劳斯硫磺回收装置热反应器中甲醇的结局,但仍缺乏对甲醇反应性和第一催化转化器内影响的了解。为了阐明这一问题,我们进行了一系列实验室实验,模拟了现场条件,阐明了甲醇在克劳斯硫磺回收装置的第一个催化转化器中的作用,该催化器可以包含二氧化钛(TiO2)和/或氧化铝( Al2O3)催化剂。获得的结果表明,甲醇通过CH3SH中间体转化为CS2,然后水解形成H2S和CO2。战略性设计的实验支持了Al2O3和TiO2上这种甲醇转化机理。尽管在某些使用甲醇的实验中观察到催化剂变色,但未观察到明显的催化剂失活,一旦达到稳态,就将CS2转化率作为评估活性的方法进行监测。催化剂表面积分析的结果与这些观察结果一致。最后,还发现与未向进料中添加甲醇的对照实验相比,在存在甲醇的实验过程中形成的硫的碳含量没有变化。

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