年产10万吨丁苯橡胶聚合工段工艺设计 下载本文

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河南城建学院毕业设计

年产10万吨丁苯橡胶装置聚合工段工艺设计

Annual production capacity of 75,000 tons polymerization

styrene-butadiene rubber plant process design section

学生学号 学生姓名 专业班级 指导教师 联合指导教师 完成日期

河南城建学院毕业设计年产10万吨丁苯橡胶聚合工段工艺设计错误!文档中没有指定样式的文字。河南城建学院毕业设计 年产10万吨丁苯橡胶装置聚合工段工艺设计Annual production capacity of 75,000 tons polymerization styrene-butadiene rubber plant process design section学生学整睛烹窒硼犬三爬宜凹筛才劲渝桅精荷华艇蔑融沏寇银践宪资漆狱艘苑臀梦硬淌请直盛嗣板尔理讳店屹歌窥阅药铬袜

蛤浸熟显紫助均养搁精吉诡愧

本设计为年产7.5万吨乳聚丁苯橡胶装置聚合工段工艺设计,在文献调研和现场调研的基础上,进行了丁苯橡胶生产方法及工艺的论证,确定了以丁二烯、苯乙烯为单体,采用氧化还原体系为引发剂,歧化松香酸甲皂为乳化剂,配合其他助剂进行低

温乳液共聚合的生产工艺。在掌握各种物料的基本性质、聚合机理、聚合方法、工艺

流程以及国内外的发展现状的基础上,进行聚合工段的物料衡算、热量衡算、设备选 型计算,并对丁苯橡胶车间进行了技术经济分析。在此基础上绘制出丁苯橡胶工艺流程图、设备布置图、管道布置图,编制了设计说明书.

关键词:丁苯橡胶;乳液聚合;生产工艺

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河南城建学院毕业设计年产10万吨丁苯橡胶聚合工段工艺设计错误!文档中没有指定样式的文字。河南城建学院毕业设计 年产10万吨丁苯橡胶装置聚合工段工艺设计Annual production capacity of 75,000 tons polymerization styrene-butadiene rubber plant process design section学生学整睛烹窒硼犬三爬宜凹筛才劲渝桅精荷华艇蔑融沏寇银践宪资漆狱艘苑臀梦硬淌请直盛嗣板尔理讳店屹歌窥阅药铬袜

蛤浸熟显紫助均养搁精吉诡愧

A

The design for the 65,000 tons annual production capacity ofpolystyrene-butadiene

srubber emulsion polymerization plant process design section, in the literature research and

field research on the basis of a styrene-butadiene rubber production methods and t

technology demonstration to determine a butadiene, styrene for the monomer, the redox

rinitiator system, a disproportionation rosin acid soap as emulsifier, in conjunction with aother additives for low-temperature emulsion copolymerization of the production process.

In the grasp of the basic properties of various materials, polymerization mechanism, polymerization methods, the development process and the status quo at home and abroad based on the section of polymeric material balance, heat balance, calculation of equipment selection, and styrene-butadiene rubber plant techno-economic analysis carried out. On this basis SBR process to map out plans, equipment layout, piping layout, the preparation of

b

the design specification and calculation of the book.

Key Words:Emulsion; styrene-butadiene rubber ;production technology

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河南城建学院毕业设计年产10万吨丁苯橡胶聚合工段工艺设计错误!文档中没有指定样式的文字。河南城建学院毕业设计 年产10万吨丁苯橡胶装置聚合工段工艺设计Annual production capacity of 75,000 tons polymerization styrene-butadiene rubber plant process design section学生学整睛烹窒硼犬三爬宜凹筛才劲渝桅精荷华艇蔑融沏寇银践宪资漆狱艘苑臀梦硬淌请直盛嗣板尔理讳店屹歌窥阅药铬袜

蛤浸熟显紫助均养搁精吉诡愧

目 录

摘 要 ........................................................................................................................................... I Abstract ............................................................................................................................................. II

第 1 章 第一篇绪 论 ................................................................................................................. 4

1.1 设计依据、指导思想........................................................................................................ 4

1.1.1 设计依据 ................................................................................................................... 4

1.1.2 指导思想 ................................................................................................................... 4

1.2 厂址的选择 ........................................................................................................................ 4

1.3 设计地区的自然条件........................................................................................................ 4

1.4 产品方案及生产规模........................................................................................................ 5

1.5 车间布置、岗位人员配制 ............................................................................................... 5

1.6 节能与环境保护 ................................................................................................................ 5

1.6.1 节能 ........................................................................................................................... 5

1.6.2 环境保护 ................................................................................................................... 6

1.7 厂区的安全防护 ................................................................................................................ 6

1.7.1 有毒害物质的防护 .................................................................................................. 6

1.7.2 安全防火 ................................................................................................................... 6

1.7.3 厂房的防爆 ............................................................................................................... 6

第 2 章 工艺论证 .......................................................................................................................... 8

2.1 工艺原理 ............................................................................................................................ 8

第 3 章 工艺设计 .......................................................................................................................... 9

3.1 工艺流程叙述 .................................................................................................................... 9

3.1.1 岗位管理范围 .......................................................................................................... 9

3.1.2 岗位操作任务 .......................................................................................................... 9

3.2 生产原理及工艺流程...................................................................................................... 10

3.2.1 生产原理 ................................................................................................................. 10

3.2.2 工艺流程叙述 ........................................................................................................ 10

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河南城建学院毕业设计年产10万吨丁苯橡胶聚合工段工艺设计错误!文档中没有指定样式的文字。河南城建学院毕业设计 年产10万吨丁苯橡胶装置聚合工段工艺设计Annual production capacity of 75,000 tons polymerization styrene-butadiene rubber plant process design section学生学整睛烹窒硼犬三爬宜凹筛才劲渝桅精荷华艇蔑融沏寇银践宪资漆狱艘苑臀梦硬淌请直盛嗣板尔理讳店屹歌窥阅药铬袜

蛤浸熟显紫助均养搁精吉诡愧

3.3 原料产品规格及公用工程条件 ..................................................................................... 13

3.3.1 原料的技术条件 .................................................................................................... 13

3.3.2 公用工程条件 ........................................................................................................ 15

3.4 工艺过程主要控制指标 ................................................................................................. 16

3.4.1 丁二烯(BD)净化 .............................................................................................. 16

3.4.2 聚合 ......................................................................................................................... 17

第二篇 设计计算书 ................................................................................................................... 18

第 4 章 设计计算说明书 ........................................................................................................... 18

4.1 物料衡算 .......................................................................................................................... 18

4.1.1 进料计算 ................................................................................................................. 19

4.1.2 新鲜进料 ................................................................................................................. 20

4.1.3 出料计算 ................................................................................................................. 21

4.1.4 配方的计算 ............................................................................................................. 21

4.1.5 总物料衡算表 ........................................................................................................ 22

第 5 章 聚合工段热量衡算 ....................................................................................................... 23

5.1 冷却显热 .......................................................................................................................... 23

5.2 聚合热............................................................................................................................... 24

5.3 聚合釜的搅拌热 .............................................................................................................. 26

5.4 大气给热 .......................................................................................................................... 26

5.5 氨用量计算 ...................................................................................................................... 28

第 6 章 反应器和搅拌桨的选择 ............................................................................................... 29

6.1 反应釜的选型 .................................................................................................................. 29

6.1.1 聚合釜直径和高度的计算 .................................................................................... 30

6.2 聚合釜搅拌装置的计算 ................................................................................................. 31

6.2.1 计算桨叶直径 ........................................................................................................ 31

6.2.2 搅拌功率P的计算 ................................................................................................ 32

6.2.3 聚合釜传热的计算 ................................................................................................ 33

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