年产15万吨氯苯精制工艺设计

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1、本科毕业设计年产15万吨氯苯精制工艺设计TheDesignof150000t/aChlorobenzeneRefiningProcess学院名称：化学与环境工程学院专业班级：化学工程与工艺2班学生姓名：石晓雨学号：201005010070指导教师姓名：路有昌指导教师职称：副教授2014年5月毕业设计原创性声明和使用授权说明原创性声明本人郑重承诺：所呈交的毕业设计（论文），是我个人在指导教师的指导下进行的研究工作及取得的成果。尽我所知，除文中特别加以标注和致谢的地方外，不包含其他人或组织已经发表或公布过的研究成果，也不包含我为获得安阳工学院及其它教育机构的学位或学历而使用过的材料。对本研究

2、提供过帮助和做出过贡献的个人或集体，均已在文中作了明确的说明并表示了谢意。作者签名：　　　　　日　期：　　　　指导教师签名：　　　　　日　　期：　　　　使用授权说明本人完全了解安阳工学院关于收集、保存、使用毕业设计（论文）的规定，即：按照学校要求提交毕业设计（论文）的印刷本和电子版本；学校有权保存毕业设计（论文）的印刷本和电子版，并提供目录检索与阅览服务；学校可以采用影印、缩印、数字化或其它复制手段保存论文；在不以赢利为目的前提下，学校可以公布论文的部分或全部内容。作者签名：　　　　　日　期：　　　　目录摘要········································

3、······················IAbstract··························································II引言······························································1第一章绪论······················································21.1产品性质····················································21.2主要原、辅材料的规格及来源·····

4、·····························21.3产品的市场发展概况··········································3第二章生产流程和方案的确定····································42.1生产方法简述和方案论证·····································42.1.1一般方法简介··············································42.1.2生产工艺改进·········································

5、·····42.2生产工艺流程确定············································52.2.1生产工艺流程的确定········································52.2.2工艺流程简图··············································62.2.3精制阶段设计方案简介······································7第三章生产流程简述··············································83.1原料预处理部分··

6、············································83.2氯化反应部分················································93.3氯化液预处理部分···········································103.4氯苯精制部分···············································11第四章整个过程物料衡算·······································134.1计算框图·····················

7、······························134.2始算基准的确定·············································134.3精馏过程物料衡算···········································144.4初馏过程物料衡算···········································154.5氯化工段物料衡算······