16700吨年PVC悬浮聚合工艺设计讲解

洛阳理工学院课程设计

16700吨/年PVC悬浮聚合工艺设计

摘 要

【本设计是悬浮法生产聚氯乙烯(年产16700万吨)的工艺初步设计。该设计包括设计说明书和设计图纸两部分。设计说明书主要包括聚氯乙烯概述、制聚氯乙烯工艺方案的选择论证、悬浮法制聚氯乙烯的流程说明、工艺流程中助剂的选择及相关设备的选型等内容,对悬浮法的工艺流程有一个较为详细的描述。设计图纸则包括工艺流程图。】

关键词: 悬浮法; 聚氯乙烯; 工艺流程说明

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洛阳理工学院课程设计

Design of 16700 tons PVC suspension polymerization process

ABSTRACT

【The design for the 16700 tons of PVC polymerization process design throughout the design file is composed by two parts of the design specification and design drawings. In the design manual, a brief introduction of PVC production status, development trends, performance, and the main purposes highlighted by suspension polymerization as the polymerization process production methods. In the design process, according to the requirements of the design task book to conduct a more detailed material balance and heat balance and the the polymerizer calculation process calculation and selection of equipment, a simple techno-economic evaluation of the entire device . Drawing of the design drawings, design drawings including process flow diagram of the polymerization reactor assembly drawing】

KEYWORDS:PVC ,suspension polymerization process, production process

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洛阳理工学院课程设计

目 录

前 言 ................................................................................................ 4 第1章 概述 ...................................................................................... 5

1.1 PVC概述、发展状况及前景 ............................................. 5 1.2 聚合工艺实施方法 ............................................................... 6 第2章 聚氯乙烯生产工艺流程设计 .............................................. 11

2.1 聚氯乙烯生产工艺流程设计 .............................................. 11

2.1.1 聚氯乙烯生产工艺流程简述 .................................... 11 2.1.2 聚氯乙烯生产工艺流程图 ........................................ 12

图2.1.2-1 聚氯乙烯生产工艺流程 .................................................. 12 图2.1.2-2工艺流程方框图.............................................................. 13 第3章 物料衡算 ............................................................................. 14

3.1主要工艺参数 ...................................................................... 14

3.1.2 车间物料衡算 ........................................................... 16 3.2 釜数及投料系数的确定 ..................................................... 16 第4章 热量衡算 ............................................................................. 18

4.1 热量衡算 ............................................................................. 18 4.2循环冷却水用量 .................................................................. 19 第5章设备工艺设计 ....................................................................... 20 5.1 机器设备选型的原则 ...................................................... 20 5.2 反应釜 ............................................................................. 20 5.3 汽提塔 ............................................................................. 21 5.4 混料槽 ............................................................................... 21 5.5 离心机 ............................................................................... 22 结 论 .............................................................................................. 23 谢 辞 ................................................................................................ 24 参考文献 .......................................................................................... 25

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