Chemical Industry and Engineering Progress ›› 2024, Vol. 43 ›› Issue (8): 4307-4319.DOI: 10.16085/j.issn.1000-6613.2023-1016
• Energy processes and technology • Previous Articles
GAO Xinyue1(), FAN Gaofeng1,2, LIU Aiping3, WANG Chang'an1(), HOU Yujie1, ZHANG Jinming1, XU Jie2, CHE Defu1
Received:
2023-06-20
Revised:
2023-08-01
Online:
2024-09-02
Published:
2024-08-15
Contact:
WANG Chang'an
高昕玥1(), 范高峰1,2, 刘爱平3, 王长安1(), 侯育杰1, 张津铭1, 徐杰2, 车得福1
通讯作者:
王长安
作者简介:
高昕玥(1997—),女,博士研究生,研究方向为固体燃料燃烧特性及余热利用。E-mail:colorful5777@stu.xjtu.edu.cn。
CLC Number:
GAO Xinyue, FAN Gaofeng, LIU Aiping, WANG Chang'an, HOU Yujie, ZHANG Jinming, XU Jie, CHE Defu. Research progress on waste heat recovery technology for flue gas and slurry after wet desulphurization[J]. Chemical Industry and Engineering Progress, 2024, 43(8): 4307-4319.
高昕玥, 范高峰, 刘爱平, 王长安, 侯育杰, 张津铭, 徐杰, 车得福. 湿法脱硫后烟气和浆液余热回收技术研究进展[J]. 化工进展, 2024, 43(8): 4307-4319.
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脱硫技术 | 脱硫剂/脱硫产物 | 固形物或结晶物 总质量分数/% | 循环浆液pH | 进口烟气温度/℃ | 出口烟气(浆液)温度/℃ |
---|---|---|---|---|---|
石灰石-石膏法 | 石灰石或石灰等/石膏 | 5~20 | 5.5~6.5 | 100~160 | 50~60 |
镁法 | 镁基试剂,如氢氧化镁/硫酸镁 | 1~5 | 8~10 | 120~160 | 50~60 |
双碱液法 | 钠基脱硫剂,如氢氧化钠/硫酸钠 | 1~5 | 10~11 | 120~160 | 50~60 |
海水法 | 海水/硫酸(常被石灰或石灰石中和,形成石膏) | — | 6.5~8 | 120~150 | 50~60 |
氨法 | 液氨或氨水/硫酸铵 | — | 5.5~6.5 | 120~200 | 50~80 |
脱硫技术 | 脱硫剂/脱硫产物 | 固形物或结晶物 总质量分数/% | 循环浆液pH | 进口烟气温度/℃ | 出口烟气(浆液)温度/℃ |
---|---|---|---|---|---|
石灰石-石膏法 | 石灰石或石灰等/石膏 | 5~20 | 5.5~6.5 | 100~160 | 50~60 |
镁法 | 镁基试剂,如氢氧化镁/硫酸镁 | 1~5 | 8~10 | 120~160 | 50~60 |
双碱液法 | 钠基脱硫剂,如氢氧化钠/硫酸钠 | 1~5 | 10~11 | 120~160 | 50~60 |
海水法 | 海水/硫酸(常被石灰或石灰石中和,形成石膏) | — | 6.5~8 | 120~150 | 50~60 |
氨法 | 液氨或氨水/硫酸铵 | — | 5.5~6.5 | 120~200 | 50~80 |
回收技术 | 回收原理 | 主要技术优势 | 主要技术不足 | 发展趋势 |
---|---|---|---|---|
烟气冷凝 | ||||
间接接触式 | 对流换热 | 系统简单,水热协同回收,应用广泛 | 回收效率低,维护成本高 | 提高换热效率,降低磨损腐蚀危害 |
直接接触式 | 接触换热 | 节能环保,适用条件广泛,回收效率高 | 冷流体被污染后极易损坏后续设备 | 提高换热和环保性能 |
膜分离 | 膜对分子的选择性 | 回收水资源质量高,清洁低耗 | 高成本,难以大规模应用 | 发展低成本、抗腐蚀和耐磨损的膜材料 |
溶液吸收(以吸收式热泵为例) | 烟气与吸收溶液间的水蒸气分压力差 | 高效高质量回收水热资源,降低烟气腐蚀性 | 高成本,工艺复杂,吸收剂可能污染环境 | 寻求新型高效环保吸收液,降低系统能耗,减小设备体积 |
回收技术 | 回收原理 | 主要技术优势 | 主要技术不足 | 发展趋势 |
---|---|---|---|---|
烟气冷凝 | ||||
间接接触式 | 对流换热 | 系统简单,水热协同回收,应用广泛 | 回收效率低,维护成本高 | 提高换热效率,降低磨损腐蚀危害 |
直接接触式 | 接触换热 | 节能环保,适用条件广泛,回收效率高 | 冷流体被污染后极易损坏后续设备 | 提高换热和环保性能 |
膜分离 | 膜对分子的选择性 | 回收水资源质量高,清洁低耗 | 高成本,难以大规模应用 | 发展低成本、抗腐蚀和耐磨损的膜材料 |
溶液吸收(以吸收式热泵为例) | 烟气与吸收溶液间的水蒸气分压力差 | 高效高质量回收水热资源,降低烟气腐蚀性 | 高成本,工艺复杂,吸收剂可能污染环境 | 寻求新型高效环保吸收液,降低系统能耗,减小设备体积 |
回收技术 | 技术原理 | 主要技术优势 | 主要技术不足 | 发展方向 |
---|---|---|---|---|
浆液冷却器 | 冷却浆液 | 节水环保,工艺简单,成本较低 | 缺乏长期工程检验,回收效率较低,设备易腐蚀结垢 | 提高换热效率,降低磨损腐蚀危害 |
闪蒸 | 冷却浆液 | 高效环保,水热协同回收,控制精准 | 可能增加系统能耗,存在汽蚀风险,缺乏工程检验 | 降低应用成本,提高设备防堵塞和耐腐蚀性能 |
热泵 | 溶液吸收 | 利用范围广,回收效率高 | 系统复杂,成本高,吸收溶液可能具有环保隐患 | 发展高效集约环保型多功能热泵 |
回收技术 | 技术原理 | 主要技术优势 | 主要技术不足 | 发展方向 |
---|---|---|---|---|
浆液冷却器 | 冷却浆液 | 节水环保,工艺简单,成本较低 | 缺乏长期工程检验,回收效率较低,设备易腐蚀结垢 | 提高换热效率,降低磨损腐蚀危害 |
闪蒸 | 冷却浆液 | 高效环保,水热协同回收,控制精准 | 可能增加系统能耗,存在汽蚀风险,缺乏工程检验 | 降低应用成本,提高设备防堵塞和耐腐蚀性能 |
热泵 | 溶液吸收 | 利用范围广,回收效率高 | 系统复杂,成本高,吸收溶液可能具有环保隐患 | 发展高效集约环保型多功能热泵 |
利用方式 | 主要利用形式 | 方案主要优势 | 方案可能存在的不足 |
---|---|---|---|
动力生产 | 有机朗肯循环发电 | 安全环保,提高能源利用率 | 高成本,技术复杂,输出功率有限 |
温差发电技术 | 环保可靠,能源利用率高 | 高成本,转换效率受限 | |
热能利用 | 加热凝结水 | 提高系统热效率 | 可能降低系统经济性 |
加热热网水 | 节能环保,提高能源利用率,降低成本 | 非采暖期难以持续利用系统余热 | |
预热空气 | 促进锅炉稳定燃烧,改善低温腐蚀 | 节能效果有限 | |
干燥燃料 | 提高系统经济性、安全性和系统效率 | 干燥效果有限,热量与燃料量匹配困难 |
利用方式 | 主要利用形式 | 方案主要优势 | 方案可能存在的不足 |
---|---|---|---|
动力生产 | 有机朗肯循环发电 | 安全环保,提高能源利用率 | 高成本,技术复杂,输出功率有限 |
温差发电技术 | 环保可靠,能源利用率高 | 高成本,转换效率受限 | |
热能利用 | 加热凝结水 | 提高系统热效率 | 可能降低系统经济性 |
加热热网水 | 节能环保,提高能源利用率,降低成本 | 非采暖期难以持续利用系统余热 | |
预热空气 | 促进锅炉稳定燃烧,改善低温腐蚀 | 节能效果有限 | |
干燥燃料 | 提高系统经济性、安全性和系统效率 | 干燥效果有限,热量与燃料量匹配困难 |
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