发明名称 Process for the production of sulfuric acid
摘要 Process of producing sulfuric acid from feed gases containing 0.1-30% SO<SUB>2 </SUB>comprising the steps of: (a) passing the feed gas to a first catalytic conversion step in which SO<SUB>2 </SUB>is oxidized to SO<SUB>3 </SUB>over one or more catalyst beds, (b) cooling the SO<SUB>3</SUB>-containing gas from said first contacting step by passing said gas to an intermediate condensing stage withdrawing a gas containing unconverted SO<SUB>2 </SUB>and unabsorbed SO<SUB>3 </SUB>and withdrawing a product stream of concentrated sulfuric acid, (c) reheating said gas containing unconverted SO<SUB>2 </SUB>and unabsorbed SO<SUB>3</SUB>, (d) passing the gas from step (c) to a second catalytic conversion step, in which unconverted SO<SUB>2 </SUB>is oxidized to SO<SUB>3 </SUB>over one or more catalyst beds, (e) cooling the gas from step (d) to a temperature of 0 to 100° C. above the acid dew point of said gas, (f) passing the gas from step (e) with a molar ratio of H<SUB>2</SUB>O to SO<SUB>3 </SUB>of at least 1.05 calculated under the assumption that SO<SUB>3 </SUB>is not hydrated to H<SUB>2</SUB>SO<SUB>4</SUB>, and acid dew point of below about 240° C. to a final wet condensing stage, in which the remaining sulfuric acid is condensed by cooling of said gas by indirect or direct heat exchange with a cooling medium, (g) providing in the gas, prior to conducting step (f), a content of 10<SUP>10 </SUP>to 10<SUP>13 </SUP>solid particles per Nm<SUB>3 </SUB>per vol % SO<SUB>3 </SUB>calculated under the assumption that SO<SUB>3 </SUB>is not hydrated to H<SUB>2</SUB>SO<SUB>4</SUB>, (h) withdrawing from the final wet condensing stage of step (f) a stream of 70-98 wt % sulfuric acid.
申请公布号 US2007110663(A1) 申请公布日期 2007.05.17
申请号 US20050273333 申请日期 2005.11.15
申请人 CHRISTENSEN KURT A 发明人 CHRISTENSEN KURT A.
分类号 C01B17/69 主分类号 C01B17/69
代理机构 代理人
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