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Sulfur Recovery Using the Modified Claus Process

机译:使用改进的克劳斯工艺回收硫

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摘要

The goal of the project was to remove sulfur from a waste stream of hydrogen sulfide and carbon dioxide. This was accomplished through a modified form of the Claus process. The Claus process combusts hydrogen sulfide and oxygen to produce a specific level of sulfur dioxide. The Claus reaction then catalytically reacts the two sulfur compounds to form elemental sulfur and water. The elemental sulfur is condensed out of the process to be sold, while the remaining gas is vented to the atmosphere. This vented gas met all EPA laws regarding sulfur emissions limits, and released only 1.4 kg per day of sulfur compounds. The primary improvements from the standard Claus process were the addition of desiccators and the development of a heat exchanger network. The desiccators remove water, one of the products of the reaction, in order to improve conversion in the process. The heat exchanger network reduces the reliance on utilities and water usage to maintain desired temperatures. Overall, the project was determined to have a $1.63 million net present value, making it an economically sound proposal.
机译:该项目的目标是从硫化氢和二氧化碳的废物流中去除硫。这是通过修改克劳斯程序的形式来实现的。 Claus工艺燃烧硫化氢和氧气以产生特定水平的二氧化硫。然后,克劳斯反应使两种硫化合物催化反应,形成元素硫和水。元素硫从过程中冷凝出来出售,而其余气体则排放到大气中。这种排出的气体符合所有有关硫排放限制的EPA法律,并且每天仅释放1.4千克的硫化合物。标准克劳斯工艺的主要改进是增加了干燥器并开发了热交换器网络。干燥器除去水,该水是反应的产物之一,以提高过程中的转化率。热交换器网络减少了对公用事业和用水的依赖,以维持所需的温度。总体而言,该项目的净现值为163万美元,是一项经济上合理的建议。

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