Chemical Industry and Engineering Progress ›› 2025, Vol. 44 ›› Issue (9): 5363-5376.DOI: 10.16085/j.issn.1000-6613.2024-1219
• Resources and environmental engineering • Previous Articles
WANG Xiaoguang1(
), DONG Qing1, LANG Wenli1, HONG Xiangxin1, HUANG Zhenxiang2, TAN Fengyu2,3(
), LEI Yizhu3, YU Ziyi2
Received:2024-07-26
Revised:2024-08-29
Online:2025-09-30
Published:2025-09-25
Contact:
TAN Fengyu
王晓光1(
), 董青1, 郎文丽1, 洪翔鑫1, 黄振祥2, 谭凤玉2,3(
), 雷以柱3, 余子夷2
通讯作者:
谭凤玉
作者简介:王晓光(1983—),男,研究方向为瓦斯发电。E-mail:985827396@qq.com。
基金资助:CLC Number:
WANG Xiaoguang, DONG Qing, LANG Wenli, HONG Xiangxin, HUANG Zhenxiang, TAN Fengyu, LEI Yizhu, YU Ziyi. Progress on emission reduction and resource utilization of ultra-low concentration methane[J]. Chemical Industry and Engineering Progress, 2025, 44(9): 5363-5376.
王晓光, 董青, 郎文丽, 洪翔鑫, 黄振祥, 谭凤玉, 雷以柱, 余子夷. 超低浓度甲烷减排与资源化利用研究进展[J]. 化工进展, 2025, 44(9): 5363-5376.
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| 政策文件名称 | 主要内容 | 时间 |
|---|---|---|
| 《碳排放权交易管理暂行条例》 | 重点排放单位可以按照国家有关规定,购买经核证的温室气体减排量用于清缴其碳排放配额 | 2024年 |
| 《全国温室气体自愿减排交易(CCER)》 | 构建强制碳配额+自愿碳减排两个相互关联的碳市场体系,对碳市场期现联动的打通及碳金融产品开发创新的推动 | 2024年 |
| 《甲烷排放控制行动方案》 | 甲烷排放控制顶层设计文件;强调加强甲烷排放监测、核算、报告和核查体系建设;推进能源、农业、垃圾和污水处理领域甲烷排放和利用 | 2023年 |
| 《“全球甲烷承诺”部长级会议》 | 到2030年将人为甲烷排放量从2020年水平减少至少30% | 2023年 |
| 欧盟《甲烷减排法规》 | 通过立法强制要求对能源生产活动产生的甲烷排放进行监测、报告和核查 | 2023年 |
| 《“十四五”现代能源体系规划》 | 指出要加大能源行业甲烷采收利用力度,推进甲烷减排 | 2022年 |
| 《通胀削减法案甲烷排放收费政策简介》 | 首次提出2024年正式对石油和天然气行业的甲烷排放收费;对甲烷排放收费的范围和适用性、费率和潜在收费豁免作出了详细规定 | 2022年 |
| 《工业领域碳达峰实施方案》 | 提出加快推进工业绿色低碳转型,切实做好油气、煤炭、固废利用等工业领域“碳达峰”工作 | 2022年 |
| 《美国甲烷减排行动计划》 | 针对油气领域甲烷减排制定了新的规则;针对废弃煤炭、石油、天然气设施以及改进工业制造设备等 | 2021年 |
| 政策文件名称 | 主要内容 | 时间 |
|---|---|---|
| 《碳排放权交易管理暂行条例》 | 重点排放单位可以按照国家有关规定,购买经核证的温室气体减排量用于清缴其碳排放配额 | 2024年 |
| 《全国温室气体自愿减排交易(CCER)》 | 构建强制碳配额+自愿碳减排两个相互关联的碳市场体系,对碳市场期现联动的打通及碳金融产品开发创新的推动 | 2024年 |
| 《甲烷排放控制行动方案》 | 甲烷排放控制顶层设计文件;强调加强甲烷排放监测、核算、报告和核查体系建设;推进能源、农业、垃圾和污水处理领域甲烷排放和利用 | 2023年 |
| 《“全球甲烷承诺”部长级会议》 | 到2030年将人为甲烷排放量从2020年水平减少至少30% | 2023年 |
| 欧盟《甲烷减排法规》 | 通过立法强制要求对能源生产活动产生的甲烷排放进行监测、报告和核查 | 2023年 |
| 《“十四五”现代能源体系规划》 | 指出要加大能源行业甲烷采收利用力度,推进甲烷减排 | 2022年 |
| 《通胀削减法案甲烷排放收费政策简介》 | 首次提出2024年正式对石油和天然气行业的甲烷排放收费;对甲烷排放收费的范围和适用性、费率和潜在收费豁免作出了详细规定 | 2022年 |
| 《工业领域碳达峰实施方案》 | 提出加快推进工业绿色低碳转型,切实做好油气、煤炭、固废利用等工业领域“碳达峰”工作 | 2022年 |
| 《美国甲烷减排行动计划》 | 针对油气领域甲烷减排制定了新的规则;针对废弃煤炭、石油、天然气设施以及改进工业制造设备等 | 2021年 |
| 检测方法 | 工作原理 |
|---|---|
| 催化燃烧型传感器 | 利用甲烷在催化剂表面氧化产生的热量变化,通过热敏元件转化为电信号,热敏电阻感应到温度升高,其阻值相应变化,从而形成与甲烷浓度成正比的电信号输出 |
| 电化学型传感器 | 利用甲烷与电解质发生化学反应,产生电流;电流大小与甲烷浓度直接相关,通过测量电流强度即可确定甲烷浓度 |
| 红外吸收型传感器 | 利用甲烷分子对特定红外波段具有选择性吸收,吸收程度与甲烷浓度成正比;通过比较入射光与出射光强度,即可计算出甲烷浓度 |
| 半导体型传感器 | 利用甲烷吸附导致半导体材料电阻变化的特性,当甲烷气体吸附到半导体表面时,改变了其电阻率;通过测量电阻变化,间接反映出甲烷浓度 |
| 光纤型传感器 | 利用光的传播特性,通过检测甲烷对光信号的调制(如吸收、散射、相位变化等)来判断甲烷浓度 |
| 气相色谱法 | 将气体样本引入色谱柱,利用不同成分的分离特性来检测甲烷的存在 |
| 化学分析法 | 使用化学反应法,如甲烷的特定化学试剂反应,可以检测到低浓度的甲烷 |
| 光谱分析法 | 利用甲烷特定的光谱特性来检测其浓度,比如傅里叶变换红外光谱(FTIR)技术 |
| 检测方法 | 工作原理 |
|---|---|
| 催化燃烧型传感器 | 利用甲烷在催化剂表面氧化产生的热量变化,通过热敏元件转化为电信号,热敏电阻感应到温度升高,其阻值相应变化,从而形成与甲烷浓度成正比的电信号输出 |
| 电化学型传感器 | 利用甲烷与电解质发生化学反应,产生电流;电流大小与甲烷浓度直接相关,通过测量电流强度即可确定甲烷浓度 |
| 红外吸收型传感器 | 利用甲烷分子对特定红外波段具有选择性吸收,吸收程度与甲烷浓度成正比;通过比较入射光与出射光强度,即可计算出甲烷浓度 |
| 半导体型传感器 | 利用甲烷吸附导致半导体材料电阻变化的特性,当甲烷气体吸附到半导体表面时,改变了其电阻率;通过测量电阻变化,间接反映出甲烷浓度 |
| 光纤型传感器 | 利用光的传播特性,通过检测甲烷对光信号的调制(如吸收、散射、相位变化等)来判断甲烷浓度 |
| 气相色谱法 | 将气体样本引入色谱柱,利用不同成分的分离特性来检测甲烷的存在 |
| 化学分析法 | 使用化学反应法,如甲烷的特定化学试剂反应,可以检测到低浓度的甲烷 |
| 光谱分析法 | 利用甲烷特定的光谱特性来检测其浓度,比如傅里叶变换红外光谱(FTIR)技术 |
| 反应设备 | 工作原理 | 催化剂 | 气体 流向 | 起燃温度 | 最低甲烷体积分数 | 经济性分析 |
|---|---|---|---|---|---|---|
| TFRR | 甲烷与热交换介质直接在反应区进行热交换,受热达到燃烧所需要的温度发生氧化反应 | 无 | 逆流 | 1000℃ | 0.2% | 需要复杂的流动和高效的热管理系统,经济成本高 |
| CFRR | 甲烷与热交换介质在催化剂床层之间接触,受热达到燃烧所需要的温度发生催化氧化反应 | 有 | 逆流 | 350~800℃ | 0.1% | 设备设计和催化剂更换等过程难度大,经济成本高 |
| CMR | 甲烷与热交换介质在涂有催化剂的平行气流通道整体式反应器内接触,受热达到燃烧所需要的温度发生催化氧化反应 | 有 | 平行 | 500℃ | 0.4% | 设备设计、催化剂更换和整体催化剂的制造成本略低,经济成本较适中 |
| 反应设备 | 工作原理 | 催化剂 | 气体 流向 | 起燃温度 | 最低甲烷体积分数 | 经济性分析 |
|---|---|---|---|---|---|---|
| TFRR | 甲烷与热交换介质直接在反应区进行热交换,受热达到燃烧所需要的温度发生氧化反应 | 无 | 逆流 | 1000℃ | 0.2% | 需要复杂的流动和高效的热管理系统,经济成本高 |
| CFRR | 甲烷与热交换介质在催化剂床层之间接触,受热达到燃烧所需要的温度发生催化氧化反应 | 有 | 逆流 | 350~800℃ | 0.1% | 设备设计和催化剂更换等过程难度大,经济成本高 |
| CMR | 甲烷与热交换介质在涂有催化剂的平行气流通道整体式反应器内接触,受热达到燃烧所需要的温度发生催化氧化反应 | 有 | 平行 | 500℃ | 0.4% | 设备设计、催化剂更换和整体催化剂的制造成本略低,经济成本较适中 |
| 燃气轮机类型 | 工作原理 | 燃烧温度 | 甲烷最低体积分数 | NO x 排放量 | CO排放量 |
|---|---|---|---|---|---|
| EDL回热式燃气轮机 | 整体式蜂窝状反应器 | 700~1000℃ | 1.6% | 较高 | 低 |
| CSIRO稀燃催化燃气轮机 | 整体式反应堆 | — | 0.8% | 低 | 低 |
| IR微型燃气轮机 | 整体式反应堆 | 500℃ | 1.0% | 低 | 低 |
| 川崎催化燃烧燃气轮机 | 整体式反应堆 | 300~1000℃ | 2.0% | 低 | 低 |
| 燃气轮机类型 | 工作原理 | 燃烧温度 | 甲烷最低体积分数 | NO x 排放量 | CO排放量 |
|---|---|---|---|---|---|
| EDL回热式燃气轮机 | 整体式蜂窝状反应器 | 700~1000℃ | 1.6% | 较高 | 低 |
| CSIRO稀燃催化燃气轮机 | 整体式反应堆 | — | 0.8% | 低 | 低 |
| IR微型燃气轮机 | 整体式反应堆 | 500℃ | 1.0% | 低 | 低 |
| 川崎催化燃烧燃气轮机 | 整体式反应堆 | 300~1000℃ | 2.0% | 低 | 低 |
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