汽车安全与节能学报 ›› 2025, Vol. 16 ›› Issue (3): 345-366.DOI: 10.3969/j.issn.1674-8484.2025.03.001
• 综述与展望 • 下一篇
收稿日期:2025-06-02
修回日期:2025-06-09
出版日期:2025-06-30
发布日期:2025-07-01
作者简介:李理光(1962—),男(白族),教授。E-mail :liguang@tongji.edu.cn。
基金资助:
LI Liguang(
), SHANG Quanbo, TANG Yongjian, DENG Jun
Received:2025-06-02
Revised:2025-06-09
Online:2025-06-30
Published:2025-07-01
摘要:
在全球化石能源消耗与气候变化引发的碳减排需求和能源低碳化与零碳化转型的背景下,氨氢融合燃料内燃机(ICEs)因其零碳排放潜力成为交通运输领域的关注热点和重要研究方向之一。氨燃料具有高携氢能量密度、易储运和高抗爆性等优势,但其燃烧速度低,燃料含氮特性使其污染物排放具有高氮氧化物(NOx)、未燃氨(NH3)和氧化亚氮(N2O)的特点,在内燃机领域的氨氢融合燃料燃烧优化与近零排放控制是一项全新研究,面临艰巨的挑战。本文综述了氨氢融合燃料内燃机的排放特性及近零排放控制技术的最新研究进展。首先,在排放机理方面,氨燃料燃烧过程中NOx的生成路径复杂,受当量比、压力和温度等因素影响,早期的机理研究主要聚焦在低压和中高温范围,但与内燃机高压高温差距较大,是当前研究的重点。其次,缸内污染物生成与控制是降低排放的重要措施,通过优化燃料喷射策略、点火时刻和进气条件,能够有效平衡污染物排放与热效率关系。研究表明,氨氢融合,即氢气助燃可提升燃烧效率,减少未燃氨和N2O排放,但会增加NOx生成。最后,缸外后处理技术是实现近零排放的关键。由于氨氢燃料燃烧排放的特殊性,需要开发全新的专用后处理系统,包括选择性催化还原(SCR)技术处理NOx,氨泄漏氧化催化器(ASC)和针对高温室效应的N2O抑制生成与还原的新型催化剂。此外,氢气选择性催化还原(H2-SCR)技术为处理氨氢发动机中的氢气排放提供了新思路。未来研究需进一步优化缸内燃烧与后处理系统的协同控制,开发低温高效催化剂,并探索组合式后处理方案,以满足日益严格的排放法规和近零排放。氨氢融合燃料内燃机在实现碳中和目标中具有广阔应用前景,但其广泛应用仍需解决包括排放控制等技术瓶颈问题。
中图分类号:
李理光, 商权波, 唐泳健, 邓俊. 氨氢融合燃料内燃机排放特性与近零排放控制[J]. 汽车安全与节能学报, 2025, 16(3): 345-366.
LI Liguang, SHANG Quanbo, TANG Yongjian, DENG Jun. Review on the emission characteristics and near-zero emission control for ammonia-hydrogen internal combustion engines[J]. Journal of Automotive Safety and Energy, 2025, 16(3): 345-366.
| 燃料 种类 | 燃烧影响 | 排放影响 |
|---|---|---|
| 氢气 | 提高循环热效率以及功率 | 无碳排放,NOx排放与化石燃料相近 |
| 天然气 | 减小峰值压力 | 增大NOx、NH3排放,减小CO2排放 |
| 汽油 | 提升功率,减小峰值压力 | 增大NOx、NH3排放,减小CO2排放 |
| 柴油 | 显著提升扭矩 | 减小HC、CO2,减小NOx(氨的掺混比例小于70%) |
| DME | 扩大发动机载荷限制 | 增大HC、CO、NOx排放 |
| 燃料 种类 | 燃烧影响 | 排放影响 |
|---|---|---|
| 氢气 | 提高循环热效率以及功率 | 无碳排放,NOx排放与化石燃料相近 |
| 天然气 | 减小峰值压力 | 增大NOx、NH3排放,减小CO2排放 |
| 汽油 | 提升功率,减小峰值压力 | 增大NOx、NH3排放,减小CO2排放 |
| 柴油 | 显著提升扭矩 | 减小HC、CO2,减小NOx(氨的掺混比例小于70%) |
| DME | 扩大发动机载荷限制 | 增大HC、CO、NOx排放 |
| 作者 | 催化剂 | 测试条件 | NO转化效率 |
|---|---|---|---|
| WANG Fei等[ | Pt-Fe/ZSM-5 | 500×10-6 NO,500×10-6 NH3,10% O2,5% H2O,SV = 140 000 h-1 | > 90% (190~300 ℃) |
| WANG Yuhang等[ | Ce/Fe/WUiO-66-derived | 500×10-6 NH3,500×10-6 NO,200×10-6 SO2, 30 000 h-1 | > 80% (250~450 ℃) |
| QIN Guozhen等[ | MIL-101(Fe)-derived | 500×10-6 NH3,500×10-6 NO,30 000 h-1 | 80% @210 ℃ |
| SONG Kunli等[ | Mn-Fe-BTC | 500×10-6 NH3,500×10-6 NO,36 000 h-1 | 60~270 ℃,> 80% |
| SONG Kunli等[ | TEOS&Mn-BTC | 500×10-6 NH3,500×10-6 NO,72 000 h-1 | 60~330 ℃,> 80%,提升N2的选择敏感性 |
| SONG Kunli等[ | IPA-Mn-BTC | 500×10-6 NH3,500×10-6 NO,36 000 h-1,6% H2O | 60~230 ℃,> 80 %,提升了水热老化性能 |
| JIA Yang等[ | Cu-BTC-derived | 500×10-6 NH3,500×10-6 NO,40 000 h-1 | 270~390 ℃,> 80% |
| S. Katarzyna等[ | Mn-HKUST-1 | 1 000×10-6 NH3,1 000×10-6 NO,13 360 h-1 | 185 ℃,60% |
| 作者 | 催化剂 | 测试条件 | NO转化效率 |
|---|---|---|---|
| WANG Fei等[ | Pt-Fe/ZSM-5 | 500×10-6 NO,500×10-6 NH3,10% O2,5% H2O,SV = 140 000 h-1 | > 90% (190~300 ℃) |
| WANG Yuhang等[ | Ce/Fe/WUiO-66-derived | 500×10-6 NH3,500×10-6 NO,200×10-6 SO2, 30 000 h-1 | > 80% (250~450 ℃) |
| QIN Guozhen等[ | MIL-101(Fe)-derived | 500×10-6 NH3,500×10-6 NO,30 000 h-1 | 80% @210 ℃ |
| SONG Kunli等[ | Mn-Fe-BTC | 500×10-6 NH3,500×10-6 NO,36 000 h-1 | 60~270 ℃,> 80% |
| SONG Kunli等[ | TEOS&Mn-BTC | 500×10-6 NH3,500×10-6 NO,72 000 h-1 | 60~330 ℃,> 80%,提升N2的选择敏感性 |
| SONG Kunli等[ | IPA-Mn-BTC | 500×10-6 NH3,500×10-6 NO,36 000 h-1,6% H2O | 60~230 ℃,> 80 %,提升了水热老化性能 |
| JIA Yang等[ | Cu-BTC-derived | 500×10-6 NH3,500×10-6 NO,40 000 h-1 | 270~390 ℃,> 80% |
| S. Katarzyna等[ | Mn-HKUST-1 | 1 000×10-6 NH3,1 000×10-6 NO,13 360 h-1 | 185 ℃,60% |
| 作者 | 催化剂 | T90 / ℃ | N2选择性/ % | 反应条件 |
|---|---|---|---|---|
| WANG Zhong等[ | Ag / ZSM-5 | 110 | 75 | 1000×10-6 NH3,10 vol% O2,35 000 h-1空速 |
| SUN Mengmeng等[ | Pt Cu / ZSM-5 | 245 | 77 | 180×10-6 NH3,8 vol% O2,100 000 h-1空速 |
| 孙萌萌等[ | FeCu / ZSM-5 | 350 | >90 | 2×10-8 NH3,10% O2,8% CO2,100 000 h-1 |
| G-K. King等[ | Fe-ZSM-5 | 500 | 98 | 0.5 vol% NH3,2.5 vol% O2,40 ml/min总流速,0.1 g催化剂 |
| ZHANG Tao等[ | Cu-SSZ-13 | 200 | 95 | 500×10-6 NH3,5 vol% O2,200 ml/min总流速,160 000 h-1空速 |
| M. Rutkowska等[ | FeCr / Beta | 400 | >90 | 0.5 vol% NH3,2.5vol% O2,40 ml/min 总流速,空速24 L·(h·g)-1 |
| LIN Mingyue等[ | Au / Nb2O5 | 245 | 95 | 50×10-6 NH3,20% O2,总流量100 ml/min |
| S. Sachi等[ | Pt / Al2O3 | 250 | 50 | 0.5% NH3,5% O2,66 000 h-1 |
| 作者 | 催化剂 | T90 / ℃ | N2选择性/ % | 反应条件 |
|---|---|---|---|---|
| WANG Zhong等[ | Ag / ZSM-5 | 110 | 75 | 1000×10-6 NH3,10 vol% O2,35 000 h-1空速 |
| SUN Mengmeng等[ | Pt Cu / ZSM-5 | 245 | 77 | 180×10-6 NH3,8 vol% O2,100 000 h-1空速 |
| 孙萌萌等[ | FeCu / ZSM-5 | 350 | >90 | 2×10-8 NH3,10% O2,8% CO2,100 000 h-1 |
| G-K. King等[ | Fe-ZSM-5 | 500 | 98 | 0.5 vol% NH3,2.5 vol% O2,40 ml/min总流速,0.1 g催化剂 |
| ZHANG Tao等[ | Cu-SSZ-13 | 200 | 95 | 500×10-6 NH3,5 vol% O2,200 ml/min总流速,160 000 h-1空速 |
| M. Rutkowska等[ | FeCr / Beta | 400 | >90 | 0.5 vol% NH3,2.5vol% O2,40 ml/min 总流速,空速24 L·(h·g)-1 |
| LIN Mingyue等[ | Au / Nb2O5 | 245 | 95 | 50×10-6 NH3,20% O2,总流量100 ml/min |
| S. Sachi等[ | Pt / Al2O3 | 250 | 50 | 0.5% NH3,5% O2,66 000 h-1 |
| 编号 | 车辆型号 | 发动机型号 | 车辆/发动机编号 | 后处理 技术 | 测试循环 | N2O排放速率 | N2O在温室气体 排放中比例/ % | |
|---|---|---|---|---|---|---|---|---|
| (mg·mile-1) | [mg·(bhp·h)-1] | |||||||
| 1 | 城市公交 | 2026 Cummins ISL 2800 | 2 | 催化 DPF | 公路模式 | 155 | -2 | |
| 2 | 重型卡车 | 2004 Cummins ISX 450 | 2 | 无 | HD-UDDS | 23 | -0.3 | |
| 3 | 重型卡车 | 2004 Caterpillar C-11 | 1 | 无 | HD-FTP | 5 | 0.26 | |
| 氧化催化 | HD-FTP | 11.4 | 0.41 | |||||
| 4 | 重型卡车 | 2002 Mark AI-300A | 1 | 无 | HD-FTP | 6 | 0.3 | |
| 催化 DPF | HD-FTP | 14~19 | 0.7~0.9 | |||||
| 5 | 长途货运卡车 | 2004 Mercedes MBE4000 | 1 | 无 | HD-UDDS | 11 | 0.2 | |
| 2003 Cummins ISMM400 | 1 | 无 | HD-UDDS | 8 | 0.2 | |||
| 1999 Caterpillar C-12 | 1 | 无 | HD-UDDS | 12 | 0.2 | |||
| 6 | 长途货运卡车 | 1996 Caterpilar 3126E | 1 | 氧化催化 | HD-FTP | 10 | 0.2 | |
| 编号 | 车辆型号 | 发动机型号 | 车辆/发动机编号 | 后处理 技术 | 测试循环 | N2O排放速率 | N2O在温室气体 排放中比例/ % | |
|---|---|---|---|---|---|---|---|---|
| (mg·mile-1) | [mg·(bhp·h)-1] | |||||||
| 1 | 城市公交 | 2026 Cummins ISL 2800 | 2 | 催化 DPF | 公路模式 | 155 | -2 | |
| 2 | 重型卡车 | 2004 Cummins ISX 450 | 2 | 无 | HD-UDDS | 23 | -0.3 | |
| 3 | 重型卡车 | 2004 Caterpillar C-11 | 1 | 无 | HD-FTP | 5 | 0.26 | |
| 氧化催化 | HD-FTP | 11.4 | 0.41 | |||||
| 4 | 重型卡车 | 2002 Mark AI-300A | 1 | 无 | HD-FTP | 6 | 0.3 | |
| 催化 DPF | HD-FTP | 14~19 | 0.7~0.9 | |||||
| 5 | 长途货运卡车 | 2004 Mercedes MBE4000 | 1 | 无 | HD-UDDS | 11 | 0.2 | |
| 2003 Cummins ISMM400 | 1 | 无 | HD-UDDS | 8 | 0.2 | |||
| 1999 Caterpillar C-12 | 1 | 无 | HD-UDDS | 12 | 0.2 | |||
| 6 | 长途货运卡车 | 1996 Caterpilar 3126E | 1 | 氧化催化 | HD-FTP | 10 | 0.2 | |
| 作者 | 催化剂 | 测试气体 | 最大NOx 转化效率/ % | 高活性温度 窗口/ ℃ |
|---|---|---|---|---|
| YU Qing等[ | Pt / Cr / ZSM-35 | 0.1% NO, 0.5% H2, 6.7% O2, 80 000 h-1 | > 95 | 80~150 |
| O. G. George等[ | Pt / MgO-CeO2 | 0.015% NO, 0.2% H2, 2% O2, 33 000 h-1 | ≈ 100 | 120~180 |
| LIU Zhiming等[ | Pt / TiO2-WO3 | 0.025% NO, 0.1% H2, 5% O2, 53 000 h-1 | > 90 | 100~200 |
| LI Jia等[ | Pd-Ir / TiO2 | 0.1% NO, 0.3% H2, 5% O2, 60 000 h-1 | > 80 | 140~200 |
| XU Chaochao等[ | Co-FePd | 0.1% NO, 1% H2, 3% O2, 23 400 h-1 | > 96 | 170~250 |
| C. K. Vasiliki等[ | Pt / Al2O3 | 0.05% NO, 0.1% H2, 5% O2, 80 000 h-1 | > 91 | 95~200 |
| HONG Zhe等[ | Pt / SSZ-13 | 0.1% NO, 0.5% H2, 10% O2, 50 000 h-1 | > 81 | 80~140 |
| DUAN Kaijiao等[ | Pd0.5 / TiO2-Al2O3 | 0.025% NO, 0.1% H2, 5% O2, 50 000 h-1 | > 90 | 100~250 |
| 作者 | 催化剂 | 测试气体 | 最大NOx 转化效率/ % | 高活性温度 窗口/ ℃ |
|---|---|---|---|---|
| YU Qing等[ | Pt / Cr / ZSM-35 | 0.1% NO, 0.5% H2, 6.7% O2, 80 000 h-1 | > 95 | 80~150 |
| O. G. George等[ | Pt / MgO-CeO2 | 0.015% NO, 0.2% H2, 2% O2, 33 000 h-1 | ≈ 100 | 120~180 |
| LIU Zhiming等[ | Pt / TiO2-WO3 | 0.025% NO, 0.1% H2, 5% O2, 53 000 h-1 | > 90 | 100~200 |
| LI Jia等[ | Pd-Ir / TiO2 | 0.1% NO, 0.3% H2, 5% O2, 60 000 h-1 | > 80 | 140~200 |
| XU Chaochao等[ | Co-FePd | 0.1% NO, 1% H2, 3% O2, 23 400 h-1 | > 96 | 170~250 |
| C. K. Vasiliki等[ | Pt / Al2O3 | 0.05% NO, 0.1% H2, 5% O2, 80 000 h-1 | > 91 | 95~200 |
| HONG Zhe等[ | Pt / SSZ-13 | 0.1% NO, 0.5% H2, 10% O2, 50 000 h-1 | > 81 | 80~140 |
| DUAN Kaijiao等[ | Pd0.5 / TiO2-Al2O3 | 0.025% NO, 0.1% H2, 5% O2, 50 000 h-1 | > 90 | 100~250 |
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