年产5.5万吨1,4-丁二醇项目目录TOC\o"1-3"\h\z\uHYPERLINK\l"_Toc325794253"第一章总论PAGEREF_Toc325794253\h1HYPERLINK\l"_Toc325794254"1.1项目概况PAGEREF_Toc325794254\h1HYPERLINK\l"_Toc325794255"1.2设计依据PAGEREF_Toc325794255\h1HYPERLINK\l"_Toc325794256"1.3化工设计指导思想PAGEREF_Toc325794256\h1HYPERLINK\l"_Toc325794257"1.4设计原则PAGEREF_Toc325794257\h1HYPERLINK\l"_Toc325794258"第二章厂址选择PAGEREF_Toc325794258\h3HYPERLINK\l"_Toc325794259"2.1选择原则PAGEREF_Toc325794259\h3HYPERLINK\l"_Toc325794260"2.2厂址选定PAGEREF_Toc325794260\h4HYPERLINK\l"_Toc325794261"2.2.1地理位置PAGEREF_Toc325794261\h4HYPERLINK\l"_Toc325794262"2.2.2原料和市场PAGEREF_Toc325794262\h4HYPERLINK\l"_Toc325794263"2.2.3自然条件PAGEREF_Toc325794263\h5HYPERLINK\l"_Toc325794264"2.2.4交通运输PAGEREF_Toc325794264\h5HYPERLINK\l"_Toc325794265"2.2.5电力能源PAGEREF_Toc325794265\h6HYPERLINK\l"_Toc325794266"2.2.6政策环境PAGEREF_Toc325794266\h7HYPERLINK\l"_Toc325794267"2.3厂址附图PAGEREF_Toc325794267\h7HYPERLINK\l"_Toc325794268"2.4产品方案PAGEREF_Toc325794268\h8HYPERLINK\l"_Toc325794269"2.5主要原料规格及消耗PAGEREF_Toc325794269\h8HYPERLINK\l"_Toc325794270"第三章工艺说明PAGEREF_Toc325794270\h9HYPERLINK\l"_Toc325794271"3.1工艺方案的选择PAGEREF_Toc325794271\h9HYPERLINK\l"_Toc325794272"3.1.1DavyMckee顺酐法PAGEREF_Toc325794272\h9HYPERLINK\l"_Toc325794273"3.1.2Reppe法PAGEREF_Toc325794273\h9HYPERLINK\l"_Toc325794274"3.1.3丁二烯法PAGEREF_Toc325794274\h9HYPERLINK\l"_Toc325794275"3.1.4丙烯醇法PAGEREF_Toc325794275\h9HYPERLINK\l"_Toc325794276"3.2工艺流程说明（对应PFD流程图）PAGEREF_Toc325794276\h10HYPERLINK\l"_Toc325794277"3.2.1酯化工段PAGEREF_Toc325794277\h10HYPERLINK\l"_Toc325794278"3.2.2加氢工段PAGEREF_Toc325794278\h11HYPERLINK\l"_Toc325794279"3.2.3精制工段PAGEREF_Toc325794279\h12HYPERLINK\l"_Toc325794280"3.3ChemCAD模拟工艺PAGEREF_Toc325794280\h13HYPERLINK\l"_Toc325794281"3.3.1模拟流程图PAGEREF_Toc325794281\h14HYPERLIN