160万吨/年延迟焦化装置可行性研究报告TOC\o"1-3"\h\z\uHYPERLINK\l"_Toc309895209"1.概述（请补充项目来源情况）PAGEREF_Toc309895209\h7HYPERLINK\l"_Toc309895210"1.1编制原则PAGEREF_Toc309895210\h7HYPERLINK\l"_Toc309895211"1.2项目范围PAGEREF_Toc309895211\h7HYPERLINK\l"_Toc309895212"1.3研究结果PAGEREF_Toc309895212\h7HYPERLINK\l"_Toc309895213"1.3.7.1环境保护PAGEREF_Toc309895213\h9HYPERLINK\l"_Toc309895214"1.3.7.2安全卫生PAGEREF_Toc309895214\h9HYPERLINK\l"_Toc309895215"2.原材料、产品规格及生产规模PAGEREF_Toc309895215\h9HYPERLINK\l"_Toc309895216"2.1原材料PAGEREF_Toc309895216\h9HYPERLINK\l"_Toc309895217"2.1.1原料来源PAGEREF_Toc309895217\h9HYPERLINK\l"_Toc309895218"2.1.2原料性质PAGEREF_Toc309895218\h9HYPERLINK\l"_Toc309895219"2.2产品PAGEREF_Toc309895219\h11HYPERLINK\l"_Toc309895220"2.2.1产品流向PAGEREF_Toc309895220\h11HYPERLINK\l"_Toc309895221"2.2.2产品性质PAGEREF_Toc309895221\h11HYPERLINK\l"_Toc309895222"2.3生产规模PAGEREF_Toc309895222\h13HYPERLINK\l"_Toc309895223"装置生产规模为160万吨/年。装置操作弹性为65%~105%。年开工时数按8400PAGEREF_Toc309895223\h13HYPERLINK\l"_Toc309895224"小时计算PAGEREF_Toc309895224\h13HYPERLINK\l"_Toc309895225"3.工艺技术方案PAGEREF_Toc309895225\h13HYPERLINK\l"_Toc309895226"3.1国内外技术状况及进展PAGEREF_Toc309895226\h13HYPERLINK\l"_Toc309895227"3.2本装置主要的工艺技术特点PAGEREF_Toc309895227\h16HYPERLINK\l"_Toc309895228"3.3物料平衡PAGEREF_Toc309895228\h18HYPERLINK\l"_Toc309895229"3.4主要操作条件PAGEREF_Toc309895229\h19HYPERLINK\l"_Toc309895230"3.5生产工艺流程PAGEREF_Toc309895230\h20HYPERLINK\l"_Toc309895231"3.6自动控制水平PAGEREF_Toc309895231\h23HYPERLINK\l"_Toc309895232"3.6.2生产过程的自控水平以及控制、检测仪表选型原则PAGEREF_Toc309895232\h23HYPERLINK\l"_Toc309895233"3.6.2.1控制室仪表PAGEREF_Toc309895233\h23HYPERLINK\l"_Toc309895234"a.室内对各工艺过程控制、监测、记录和报警采用DCS系统。PAGEREF_Toc309895234\h24HYPERLINK\l"_Toc309895235"b.对加热炉安全保护采用ESD系统。ESD系统独立于过程控制系统。PAGEREF_Toc309895235\h24HYPERLINK\l"_Toc3098