年产15万吨烧碱车间工艺设计论文

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1、毕业设计年产15万吨烧碱车间工艺设计本科生毕业设计（论文）目录摘要·················································1第一章氯碱工业的发展··································31.1氯碱工业的历史······································31.2烧碱的性质、用途及其质量标准························31.3溶液电解方法的发展··································51.4氯碱工业的特点及发展趋势········

2、····················51.5离子膜··············································71.6离子膜电解技术······································101.7我国离子膜法电解槽的现状····························11第二章工艺流程的选择与说明····························112.1原料的选择50本科生毕业设计（论文）··········································112.2盐水精制的选择··

3、····································122.3电解工艺············································122.4碱液蒸发与浓缩······································132.5固碱工艺············································132.6液氯工段工艺流程简述································132.7氯气干燥的目的与机理································132

4、.8氢气处理············································132.9盐酸工段工序流程简述································14第三章工艺计算········································143.1电解槽的工艺计算·····································143.2洗涤塔内氢气的工艺计算·······························1750本科生毕业设计（论文）3.3钛冷却器内氯气工艺衡算·················

5、··············193.4硫干燥塔内氯气物料衡算·······························21第四章设备设计········································224.1离子膜电解槽的设计···································224.2钛冷却器的设计·······································244.3蒸发塔的设计·········································264.4蒸发设备的计算···············

6、························36第五章厂房布置·········································425.1厂房布置的重要意义···································425.2厂房布置的原则及方法·································42第六章环境保护50本科生毕业设计（论文）·········································44摘要作为一种基本的和重要的化工原料，烧碱在工业生产的各个领域都有着广泛的应用。50本科生毕业设计（论文）随

7、着氯碱工业的迅速发展，离子膜电解生产烧碱越来越被广泛运用，膜电解生产的其氧化钠浓度可达30%-50%（质量）。此外，离子膜电解制碱还有投资省，能耗低，氢氧化钠质量好，无污染，生产成本低等优点。因此无论是国外还是国内在新建，改造和扩建生产装置时都会首先考虑这一技术。本设计依据技术先进，经济合理，工艺可靠，系统最优的原则完成。烧碱的生产方法是离子膜电解法，通过以下一系列工序：盐水精制，电解精盐水，蒸发电解液来得到最终产品——固碱。本设计说明书包括：烧碱生产方法的论证，物料衡算和能量衡算，主体设备及辅助设备的设计。设计中对烧碱离子膜