Chemical Industry and Engineering Progress ›› 2023, Vol. 42 ›› Issue (7): 3770-3779.DOI: 10.16085/j.issn.1000-6613.2022-1614
• Resources and environmental engineering • Previous Articles Next Articles
LI Jia(), FAN Xing(), CHEN Li, LI Jian
Received:
2022-09-01
Revised:
2023-03-03
Online:
2023-08-14
Published:
2023-07-15
Contact:
FAN Xing
通讯作者:
樊星
作者简介:
李佳(1998—),女,硕士研究生,研究方向为大气污染控制。E-mail:591240968@qq.com。
基金资助:
CLC Number:
LI Jia, FAN Xing, CHEN Li, LI Jian. Research progress of simultaneous removal of NO x and N2O from the tail gas of nitric acid production[J]. Chemical Industry and Engineering Progress, 2023, 42(7): 3770-3779.
李佳, 樊星, 陈莉, 李坚. 硝酸生产尾气中NO x 和N2O联合脱除技术研究进展[J]. 化工进展, 2023, 42(7): 3770-3779.
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尾气组成 | 体积分数/% |
---|---|
NO x | 0.01~0.35 |
N2O | 0.03~0.35 |
O2 | 1~4 |
H2O | 0.3~2 |
尾气组成 | 体积分数/% |
---|---|
NO x | 0.01~0.35 |
N2O | 0.03~0.35 |
O2 | 1~4 |
H2O | 0.3~2 |
催化剂体系 | 特点 |
---|---|
锰氧化物基 | 低温(<250℃)催化剂,改性后可进一步提高催化剂活性,耐硫性差,高温下N2选择性明显下降 |
钒氧化物基 | 中低温(300~400℃)催化剂,耐硫耐水性能优异,操作温度窗口窄,高温下催化剂稳定性和选择性差,主要用于工业尾气脱硝 |
铜分子筛 | 中低温(<400℃)催化剂,低温活性和N2选择性优异,高温水热稳定性较差,适用于低硫环境下的SCR脱硝,如汽车尾气脱硝 |
铁分子筛 | 高温(>400℃)催化剂,高温活性和N2选择性优异,操作温度窗口宽,水热稳定性好,适用于低硫环境下的SCR脱硝,如电厂尾气脱硝 |
催化剂体系 | 特点 |
---|---|
锰氧化物基 | 低温(<250℃)催化剂,改性后可进一步提高催化剂活性,耐硫性差,高温下N2选择性明显下降 |
钒氧化物基 | 中低温(300~400℃)催化剂,耐硫耐水性能优异,操作温度窗口窄,高温下催化剂稳定性和选择性差,主要用于工业尾气脱硝 |
铜分子筛 | 中低温(<400℃)催化剂,低温活性和N2选择性优异,高温水热稳定性较差,适用于低硫环境下的SCR脱硝,如汽车尾气脱硝 |
铁分子筛 | 高温(>400℃)催化剂,高温活性和N2选择性优异,操作温度窗口宽,水热稳定性好,适用于低硫环境下的SCR脱硝,如电厂尾气脱硝 |
项目 | 联合脱除工艺 | ||||
---|---|---|---|---|---|
SCR催化剂同时催化 NO x 和N2O还原 | 复合式催化剂同时催化 NO x 还原和N2O分解 | 先催化N2O分解, 后催化NO x 还原 | 先催化NO x 还原, 后催化N2O还原 | 先催化NO x 还原, 后催化N2O分解 | |
工艺类型 | 一段式 | 一段式 | 两段式 | 两段式 | 两段式 |
布设位置 | 尾气膨胀机之前 | 尾气膨胀机之前 | 尾气膨胀机之前 | 尾气膨胀机之前 | 尾气膨胀机之后 |
工艺特点 | 可同步脱除NO x 和N2O,工艺布置紧凑 | 可同步脱除NO x 和N2O,工艺布置紧凑 | 可利用NO x 对N2O分解的促进作用 | 适用范围广,脱除效率高 | 对硝酸生产工艺无影响,净化装置安装限制小 |
开发阶段 | 尚在研究 | 尚在研究 | 已有应用 | 已有应用 | 尚在研究 |
催化剂 | Fe-beta | Bi-Ni/V2O5-WO3/TiO2 | Fe-分子筛 | Fe-分子筛 | V2O5/Al2O3(NO x 还原)、改性Co3O4(N2O分解) |
反应条件 | 367μL/L NO x +1645μL/L N2O+2012μL/L NH3+1.56% O2+N2(平衡)、空速8200h-1、温度354~373℃ | 250μL/L NO+125μL/L N2O+250μL/L NH3+3% O2+N2(平衡)、空速45000h-1、温度390℃ | Borealis AG硝酸厂、1200t/d、温度425~520℃ | Abu Qir Fertilizer硝酸厂、1830t/d、温度330~520℃ | 700~1500μL/L NO x +900~1200μL/L N2O+700~1500μL/L NH3+1.9%~4.5% O2+N2(平衡)、NO x 还原段空速9664h-1、温度220~240℃、N2O分解段空速7667h-1、温度230~260℃ |
脱除效率或排放浓度 | |||||
NO x | >96% | 90% | 出口浓度5~10μL/L | 出口浓度约1μL/L | >98%(模拟结果) |
N2O | >96% | 72% | >98% | >99% | >98%(模拟结果) |
参考文献 | [ | [ | [ | [ | [ |
发展方向 | 改善催化剂低温活性(尤其是催化N2O还原/分解的活性),提高催化剂抗共存气体干扰性 | 拓宽催化剂活性温度窗口 | 降低N2O分解所需温度,提高工艺净化实际尾气的性能 |
项目 | 联合脱除工艺 | ||||
---|---|---|---|---|---|
SCR催化剂同时催化 NO x 和N2O还原 | 复合式催化剂同时催化 NO x 还原和N2O分解 | 先催化N2O分解, 后催化NO x 还原 | 先催化NO x 还原, 后催化N2O还原 | 先催化NO x 还原, 后催化N2O分解 | |
工艺类型 | 一段式 | 一段式 | 两段式 | 两段式 | 两段式 |
布设位置 | 尾气膨胀机之前 | 尾气膨胀机之前 | 尾气膨胀机之前 | 尾气膨胀机之前 | 尾气膨胀机之后 |
工艺特点 | 可同步脱除NO x 和N2O,工艺布置紧凑 | 可同步脱除NO x 和N2O,工艺布置紧凑 | 可利用NO x 对N2O分解的促进作用 | 适用范围广,脱除效率高 | 对硝酸生产工艺无影响,净化装置安装限制小 |
开发阶段 | 尚在研究 | 尚在研究 | 已有应用 | 已有应用 | 尚在研究 |
催化剂 | Fe-beta | Bi-Ni/V2O5-WO3/TiO2 | Fe-分子筛 | Fe-分子筛 | V2O5/Al2O3(NO x 还原)、改性Co3O4(N2O分解) |
反应条件 | 367μL/L NO x +1645μL/L N2O+2012μL/L NH3+1.56% O2+N2(平衡)、空速8200h-1、温度354~373℃ | 250μL/L NO+125μL/L N2O+250μL/L NH3+3% O2+N2(平衡)、空速45000h-1、温度390℃ | Borealis AG硝酸厂、1200t/d、温度425~520℃ | Abu Qir Fertilizer硝酸厂、1830t/d、温度330~520℃ | 700~1500μL/L NO x +900~1200μL/L N2O+700~1500μL/L NH3+1.9%~4.5% O2+N2(平衡)、NO x 还原段空速9664h-1、温度220~240℃、N2O分解段空速7667h-1、温度230~260℃ |
脱除效率或排放浓度 | |||||
NO x | >96% | 90% | 出口浓度5~10μL/L | 出口浓度约1μL/L | >98%(模拟结果) |
N2O | >96% | 72% | >98% | >99% | >98%(模拟结果) |
参考文献 | [ | [ | [ | [ | [ |
发展方向 | 改善催化剂低温活性(尤其是催化N2O还原/分解的活性),提高催化剂抗共存气体干扰性 | 拓宽催化剂活性温度窗口 | 降低N2O分解所需温度,提高工艺净化实际尾气的性能 |
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