年产3万吨环氧乙烷工艺设计Processdesignofethyleneoxidewithannualoutputof30kt目录TOC\o"1-3"\h\z\uHYPERLINK\l"_Toc388446396"摘要：PAGEREF_Toc388446396\hIHYPERLINK\l"_Toc388446397"Abstract:PAGEREF_Toc388446397\hIIHYPERLINK\l"_Toc388446398"引言PAGEREF_Toc388446398\h1HYPERLINK\l"_Toc388446399"第一章工艺概述PAGEREF_Toc388446399\h2HYPERLINK\l"_Toc388446400"1.1环氧乙烷的性质PAGEREF_Toc388446400\h2HYPERLINK\l"_Toc388446401"1.1.1环氧乙烷的物理性质PAGEREF_Toc388446401\h2HYPERLINK\l"_Toc388446402"1.1.2环氧乙烷的化学性质PAGEREF_Toc388446402\h2HYPERLINK\l"_Toc388446403"1.2MACROBUTTONAcceptAllChangesInDocMACROBUTTONAcceptAllChangesInDoc环氧乙烷在国民经济中的地位和作用PAGEREF_Toc388446403\h2HYPERLINK\l"_Toc388446404"1.3MACROBUTTONAcceptAllChangesInDoc环氧乙烷在国内外的发展动向PAGEREF_Toc388446404\h3HYPERLINK\l"_Toc388446405"1.3.1生产技术PAGEREF_Toc388446405\h3HYPERLINK\l"_Toc388446406"1.3.2技术发展动向PAGEREF_Toc388446406\h3HYPERLINK\l"_Toc388446407"1.4环氧乙烷的市场需求状况PAGEREF_Toc388446407\h4HYPERLINK\l"_Toc388446408"1.5生产方法的评述及选择PAGEREF_Toc388446408\h4HYPERLINK\l"_Toc388446409"1.5.1氯醇法PAGEREF_Toc388446409\h4HYPERLINK\l"_Toc388446410"1.5.2直接氧化法PAGEREF_Toc388446410\h4HYPERLINK\l"_Toc388446411"1.6环氧乙烷的生产原理PAGEREF_Toc388446411\h5HYPERLINK\l"_Toc388446412"1.6.1氧化反应原理PAGEREF_Toc388446412\h5HYPERLINK\l"_Toc388446413"1.6.2二氧化碳脱除原理PAGEREF_Toc388446413\h6HYPERLINK\l"_Toc388446414"1.7设计方案简介PAGEREF_Toc388446414\h6HYPERLINK\l"_Toc388446415"1.8生产中注意事项PAGEREF_Toc388446415\h10HYPERLINK\l"_Toc388446416"第二章物料衡算PAGEREF_Toc388446416\h11HYPERLINK\l"_Toc388446417"2.1物性数据PAGEREF_Toc388446417\h11HYPERLINK\l"_Toc388446418"2.2设计依据PAGEREF_Toc388446418\h11HYPERLINK\l"_Toc388446419"2.3循环系统的物料衡算PAGEREF_Toc388446419\h12HYPERLINK\l"_Toc388446420"2.3.1计算依据PAGEREF_Toc388446420\h12HYPERLINK\l"_Toc388446421"2.3.2混合器PAGEREF_Toc388446421\h13HYPERLINK\l"_Toc388446422"2.3.3反应器PAGEREF_Toc3