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How Do Claus Catalysts Really Work?

机译:克劳斯催化剂如何真正发挥作用?

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This paper highlights some of the salient and practically important issues of catalyticconversion of H2S and SO S SO2 in the catalytic converter train of a Claus plant. In particular, theissue of sulfate formation on alumina is investigated as it relates to CS2 conversion, testing ofcatalysts for CS2 conversion activity, influence of HS/SO2 ratio on CS2 conversion andcatalyst fouling by BTX. The use of titania for CS2 conversion is also examined.Overall, it has been shown that the formation of sulfate on alumina is directly related to theoxidizing properties of alumina or titania and the chemistry of H2S/2 conversion overthese materials. Although sulfate is formed by O2 ingress into a converter, it will also bepresent on any Claus catalyst as a result of the Anatural@ chemistry of H2S/SO2 conversion.Hence, the presence of sulfate on a catalyst is not reason enough to decide on changing out acatalyst.An understanding of the occurrence of natural sulfate has enabled development of a robustcatalyst testing procedure which allows steady-state CS2 conversion to be evaluated quicklyand reliably. Also, it has been shown that the HS/SO2 ratio is an important parameteraffecting the catalyst sulfate levels and degree of CS2 conversion attainable in the plant.Importantly, high HS/SO2 ratios give greater CS2 conversion. These factors have importantramifications with respect to evaluation of plant performance data.BTX fouling has been shown to be a general consequence of catalyst sulfate leading to thepractical step that BTX would be dealt with most successfully upstream of the convertertrain.As is well known, titania is a superior material for CS2 conversion. Sulfate is also formed ontitania but it appears to have no influence on CS2 conversion at temperatures >320 320oC.Appreciable CS2 conversion can also be attained on titania at second converter conditions.The oxidizing properties of alumina and a chemical analysis of the initial steps of H2Soxidation by O2 has allowed us to develop a new process for the catalytic conversion of H2Sto hydrogen and sulfur. This type of process has the potential to radically alter the paradigmfor sulfur recovery from H2S.
机译:本文重点介绍了催化领域的一些突出和实际重要的问题 克劳斯工厂的催化转化器中H2S和SO S SO2的转化。特别是 研究了氧化铝上硫酸盐形成的问题,因为它与CS2的转化有关, CS2转化活性的催化剂,HS / SO2比对CS2转化的影响以及 BTX对催化剂的污染。还检查了二氧化钛用于CS2转化的用途。 总的来说,已经表明,氧化铝上硫酸盐的形成直接与氧化铝的形成有关。 氧化铝或二氧化钛的氧化性质和H2S / 2转化的化学反应 这些材料。尽管硫酸盐是通过O2进入转化器而形成的,但也可能是 由于H2S / SO2转化的Anatural @化学作用而存在于任何克劳斯催化剂上。 因此,催化剂上硫酸盐的存在不足以决定改变催化剂的存在。 催化剂。 对天然硫酸盐的发生的了解使得能够开发出一种健壮的 催化剂测试程序,可快速评估稳态CS2转化率 和可靠。同样,已经表明HS / SO2比是一个重要的参数 影响工厂中催化剂硫酸盐含量和CS2转化度。 重要的是,高HS / SO2比可提供更高的CS2转化率。这些因素很重要 关于评估工厂绩效数据的后果。 已证明BTX结垢是催化剂硫酸盐导致 转换器上游最成功处理BTX的实际步骤 火车。 众所周知,二氧化钛是CS2转化的优良材料。硫酸盐也形成在 二氧化钛,但在温度> 320 320oC时,似乎对CS2的转化没有影响。 在第二转化器条件下,二氧化钛也可实现明显的CS2转化。 氧化铝的氧化性能和H2S初始步骤的化学分析 O2的氧化使我们开发了H2S催化转化的新方法 氢和硫。这种类型的过程有可能从根本上改变范式 用于从H2S中回收硫。

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