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设计说明书 封皮及格式最新

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中原工学院 材料与化工学院

化工原理课程设计说明书

设计名称: 班 级: 组 别: 组 员: 指导老师:

日 期:2013 年 12月28日

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设计任务书

一、设计题目

3000吨酒精连续填料精馏塔设计

二、设计任务及操作条件

1、 设计任务:

生产能力(塔顶产品) 3000 吨/年 操作周期 300 天/年

进料组成 35 (质量分数,下同) 塔顶产品组成 ≥94% 塔底产品组成 ≤0.1% 2、 操作条件

操作压力 常压 (塔顶) 进料热状态 35℃ 3、 设备型式 自选 4、 厂 址 郑 州 地 区 三、设计内容:

(1) 精馏塔的物料衡算; (2) 塔板数的确定;

(3) 精馏塔的工艺条件及有关物件数据的计算; (4) 精馏塔的塔体工艺尺寸计算; (5) 塔板主要工艺尺寸的计算; (6) 塔板的流体力学验算; (7) 塔板负荷性能图; (8) 精馏塔接管尺寸计算; (9) 绘制生产工艺流程图; (10) 绘制精馏塔设计条件图;

(11) 对设计过程的评述和有关问题的讨论。

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四、参考资料

1. 陈英南,刘玉兰. 常用化工单元设备的设计. 上海:华东理工大学出版社,2005 2. 黄璐,王保国. 化工设计. 北京:化学工业出版社,2001

3. 贾绍义,柴诚敬. 化工原理课程设计(化工传递与单元操作课程设计). 天津:天津大学

出版社,2002

4. 陈敏恒,丛德兹等. 化工原理(上、下册)(第二版). 北京:化学工业出版社,2000 5. 柴诚敬,刘国维,李阿娜. 化工原理课程设计. 天津:天津科学技术出版社,1995 6. 石油化学工业规划设计院. 塔的工艺计算. 北京:石油化学工业出版社,1997

7. 化工设备技术全书编辑委员会. 化工设备全书—塔设备设计. 上海:上海科学技术出版

社,1988

8. 时钧,汪家鼎等. 化学工程手册,. 北京:化学工业出版社,1986

9. 上海医药设计院. 化工工艺设计手册(上、下). 北京:化学工业出版社,1986

10. 大连理工大学化工原理教研室. 化工原理课程设计. 大连:大连理工大学出版社,1994

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目 录

一、概述 ·············································································································· 6

1. 设计依据 ·································································································· 6 1. 技术来源 ·································································································· 6 1. 设计任务及要求 ······················································································· 6 二、计算过程 ······································································································· 7

1. 塔型选择 ·································································································· 7 2. 操作条件的确定 ······················································································· 7

2.1 操作压力 ························································································· 7 2.2 进料状态 ························································································· 8 2.3 加热方式 ························································································· 8 2.4 热能利用 ························································································· 8 3. 有关的工艺计算 ······················································································· 8

3.1 最小回流比及操作回流比的确定··················································· 9 3.2 塔顶产品产量、釜残液量及加热蒸汽量的计算 ···························· 9 3.3 全凝器冷凝介质的消耗量 ···························································· 10 3.4 热能利用 ······················································································· 10 3.5 理论塔板层数的确定 ···································································· 11 3.6 全塔效率的估算 ··········································································· 11

3.7 实际塔板数NP ············································································ 12 4. 精馏塔主题尺寸的计算 ········································································· 13 4.1 精馏段与提馏段的体积流量 ························································ 13

4.1.1 精馏段 ················································································ 13 4.1.2 提馏段 ················································································ 14 4.2 塔径的计算 ··················································································· 15 4.3 塔高的计算 ··················································································· 17 5. 塔板结构尺寸的确定 ············································································· 18

5.1 塔板尺寸 ······················································································· 18 5.2 弓形降液管 ··················································································· 19

5.2.1 堰高 ···················································································· 19 5.2.2 降液管底隙高度h0 ····························································· 19 5.2.3 进口堰高和受液盘 ····························································· 19 5.3 浮阀数目及排列 ··········································································· 19

5.3.1 浮阀数目 ············································································ 19 5.3.2 排列 ···················································································· 20 5.3.3 校核 ···················································································· 20

6. 流体力学验算························································································· 21

6.1 气体通过浮阀塔板的压力降(单板压降)hp ································· 21

6.1.1 干板阻力hc ······································································· 21

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中原工学院 材料与化工学院 化工原理课程设计说明书 设计名称: 班 级: 组 别: 组 员: 指导老师: 日 期:2013 年 12月28日 1 设计任务书 一、设计题目 3000吨酒精连续填料精馏塔设计 二、设计任务及操作条件 1、 设计任务: 生产能力(塔顶产品) 3000 吨/年 操作周期 300 天/年 进料组成 35 (质量分数,下同) 塔顶产品

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