精对苯二甲酸(PTA)生产技术及工艺流程毕业论文

精对苯二甲酸(PTA)生产技术及工艺流

程毕业论文

目录

摘要······································································I 前言·································································- 1 -第一章精对苯二甲酸的工业概貌········································- 2 -

1.1 世界精对苯二甲酸工业概貌····································- 2 -

1.2 我国精对苯二甲酸工业概貌····································- 3 -第二章精对苯二甲酸的上下游产业链·································- 5 -

2.1 精对苯二甲酸的上游产业······································- 5 -

2.2 精对苯二甲酸的下游产业······································- 5 -第三章精对苯二甲酸的性质及其主要用途····························- 6 -

3.1 精对苯二甲酸的性质··········································- 6 -

3.1 精对苯二甲酸的主要用途······································- 6 -第四章精对苯二甲酸的主要原料·····································- 7 -第五章产品方案及规格··············································- 8 -

5.1 产品方案······················································- 8 -

5.2 主要产品规格·················································- 8 -

第六章精对苯二甲酸的生产工艺技术·································- 9 -

6.1 国外工艺技术现状·············································- 9 -

6.2 国的工艺技术选择············································- 10 -第七章精对苯二甲酸的工艺流程及操作条件·························- 11 -

7.1 反应历程简介················································- 11 -

7.1.1 对二甲苯氧化··········································- 11 -

7.1.2对苯二甲酸精制········································- 12 -

7.2 工艺流程简述················································- 12 -

7.2.1 空气压缩机············································- 12 -

7.2.2 100 单元---母液储存罐································- 12 -

7.2.3 200 单元--氧化反应、结晶、高压吸收及常压吸收。····- 13 -

7.2.4 300 单元－－分离、干燥·······························- 14 -

7.2.5 400 单元－－溶剂及催化剂回收、残渣蒸发、溶剂脱水、萃取、

常压汽提系统。··············································- 14 -

7.2.6 500 单元—进料配制、反应进料预热、加氢反应、结晶·- 16 -

7.2.7 600 单元—过滤、干燥·································- 19 -

7.2.8 PTA 产品之储存装袋及出料····························- 20 -第八章精对苯二甲酸生产的关键设备及其特点·······················- 22 -

8.1 精对苯二甲酸氧化单元的关键设备——氧化反应器············- 22 -

8.2 精对苯二甲酸精制单元的关键设备····························- 22 -第九章结论·························································- 24 -参考文献·····························································- 25 -致谢························································- 26 -

前言

本项目由精对苯二甲酸（PTA）主生产装置、辅助生产装置和公用工程装置等组成。精对苯二甲酸（PTA）主生产装置：主要包括氧化单元、精制单元和公用设施等，其中：

氧化单元：主要包括空气压缩、进料准备、氧化反应、CTA结晶、CTA过滤、CTA干燥、溶剂回收、催化剂回收残渣处理（CRU）、MA水解、尾气焚烧处、CTA 母液储存系统理等。

精制单元：主要包括浆料制备、加氢反应、PTA结晶、PTA压力过滤、PTA 干燥和产品输送、工艺水和母液固体回收、碱系统等。

辅助生产装置：原料及化工料罐区、精对苯二甲酸（PTA）输送、包装及贮存码头输送系统等。

本次主要论述的是精对苯二甲酸装置中氧化单元和精制单元生产技术、工艺流程及一些氧化溶剂的回收、脱水、萃取、尾气干燥、处理等。本装置设计能力为每年产120万吨PTA工程项目是市近年来投资最大的资项目之一，主要生产化纤原料——PTA，是一家实现PTA技术自主开发研究并建造的公司。以对二甲苯为原料，液相氧化生成粗对苯二甲酸，再经加氢精制，结晶，分离，干燥，得到精对苯二甲酸。

第一章精对苯二甲酸的工业概貌

1.1 世界精对苯二甲酸工业概貌

目前，亚洲是全球精对苯二甲酸（PTA）最主要的生产地和需求地，而北美和西欧地区的生产能力远远低于亚洲。世界PTA主要贸易量集中在亚洲地区，2009年进出口量分别占世界总量的71.1％及65.9％；西欧地区则分别占14.6％及20.1%；北美地区分别占5.9％及11.3％。北美及西欧地区是世界PTA主要净出口地区，而亚洲、中南美洲和中东欧是主要净进口地区。从近几年世界PTA 的贸易趋势来看，亚洲地区贸易量占世界总贸易量的比例逐年上升，西欧地区略有下滑，而北美地区呈下降的趋势。

目前，世界PTA主要用于生产聚酯，占PTA总消费量的98％以上，而PTT （聚对苯二甲酸丙二醇酯）与PBT（聚对苯二甲酸丁二醇酯）在工业化生产规模较小，目前对PTA的需求量仅约200万吨。

未来几年世界PTA工业仍将快速发展，据预测，2010年世界PTA的需求量将达到4500万吨，其中亚洲3000万吨，占世界的67％；2010年世界PTA产能超过4952万吨/年，新增产能主要来自亚洲的中国、印度、泰国等国家。中东、北美及西欧等地的PTA产能增速相对较缓，新建计划不多。而未来世界PTA消费结构变化不明显，用于生产聚酯的比例仍将超过90％。

1.1.1数据引自：表1摘自专家论坛精细化工原料及中间体2011年第1期来自中国知网。

1.2 我国精对苯二甲酸工业概貌

我国PTA生产主要集中在江浙一带。我国2008年PTA产能分布为占30%、占17%、占17%、占11%、占11%、占7%、天津占3%、占2%、占1%和新疆占1%。2010年省PTA产能将占全国总产能的50%，成为我国最大的PTA生产基地。的逸盛石化、的华联三鑫石化、大榭开发区的三菱化学公司的第2期和第3期PTA 工程也将按计划进行，预计到2010年，PTA总产能将达到260万吨/年。

1.1.2数据引自：表2摘自专家论坛精细化工原料及中间体2011年第1期来自中国知网