Petroleum Reservoir Evaluation and Development ›› 2024, Vol. 14 ›› Issue (1): 1-9.doi: 10.13809/j.cnki.cn32-1825/te.2024.01.001
• Specialist Forum • Previous Articles Next Articles
YE Xiaodong(),CHEN Jun,CHEN Xi,WANG Haimei,WANG Huijun
Received:
2023-12-26
Online:
2024-02-26
Published:
2024-03-05
CLC Number:
YE Xiaodong,CHEN Jun,CHEN Xi,WANG Haimei,WANG Huijun. China's CCUS technology challenges and countermeasures under “double carbon” target[J].Petroleum Reservoir Evaluation and Development, 2024, 14(1): 1-9.
Table 1
Project information on membrane separation method for capturing CO2 in flue gas[34]"
膜材料 | 试验机构 | 国家 | 试验规模/(Nm3/d) | 烟道气来源 | 建成时间 |
---|---|---|---|---|---|
Polaris? | MTR | 美国 | 86 000.00 | 燃气火力发电厂 | 2014年 |
PolyActive? | Helmholtz-Zentrum Geesthacht | 德国 | 1 200.00 | 燃煤火力发电厂 | 2015年 |
PVAm类材料 | NTNU | 挪威 | 0.96 | 水泥厂 | 2016年 |
Ultrason? | NCCC | 美国 | 1.50 | 燃煤火力发电厂 | 2017年 |
Polaris? | 华润海丰 | 中国 | 86 000.00 | 燃煤火力发电厂 | 2019年 |
PVAm类材料 | 天津大学 | 中国 | 50 000.00 | 燃煤火力发电厂 | 2021年 |
Table 2
Situation of CO2 capture projects after international chemical adsorption combustion[34]"
项目概况 | 气体来源 | 吸附材料 | 捕集规模/MW | CO2捕集率/% | 主要实施机构 |
---|---|---|---|---|---|
2009年CaOling双循环流化床 | 燃煤烟气 | CaO | 1.70 | >90 | 西班牙国家煤碳研究所 |
2010年美国气流床+回转窑 | 燃煤烟气 | CaO | 0.12 | >90 | 俄亥俄州立大学 |
2012年韩国输运床+鼓泡床 | 燃煤烟气 | K2CO3 | 10.00 | >80 | 韩国能源研究所 |
2012年德国双循环流化床 | 合成烟气 | CaO | 1.00 | 90~92 | 达姆施塔特工业大学 |
2019年美国双流化床 | 燃煤烟气 | 固体胺 | 1.00 | 90 | ADA公司 |
Table 3
Carbon capture technology evaluation[34]"
捕集技术 | 工业成本 | ||||||||
---|---|---|---|---|---|---|---|---|---|
现状 | 2030年 | ||||||||
热耗量/ (GJ/t) | 电耗量/ [(kW·h)/t] | 设备投资/ (元/t) | 总成本/ (元/t) | 热耗量/ (GJ/t) | 电耗量/ [(kW·h)/t] | 设备投资/ (元/t) | 总成本/ (元/t) | ||
燃烧后化学吸收 | 2.8 | 75 | 40 | 270 | 2.2 | 65 | 40 | 220 | |
燃烧后化学吸附 | 2.0 | 60 | 240 | 400 | 1.8 | 50 | 120 | 270 | |
燃烧后物理吸附 | 2.1 | 80 | 150 | 330 | 1.9 | 70 | 120 | 280 | |
燃烧后膜分离 | 0 | 450 | 150 | 310 | 0 | 250 | 120 | 210 | |
富氧燃烧 | 0 | 380 | 240 | 380 | 0 | 270 | 120 | 220 | |
化学链燃烧 | 80 | 80 |
Table 4
Carbon utilization technology evaluation[34]"
技术名称 | 2030年碳减排 潜力/104 t | |
---|---|---|
CO2化学转化制备化学品 | CO2与甲烷重整制备合成气技术 | 2 000~3 000 |
CO2裂解经一氧化碳制备液体燃料技术 | 30~100 | |
CO2加氢合成甲醇技术 | 4 800~7 200 | |
CO2加氢制烯烃技术 | 250~370 | |
CO2光电催化转化技术 | 15~35 | |
CO2合成有机碳酸酯技术 | 350~500 | |
CO2合成可降解聚合物材料技术 | 30~60 | |
CO2合成异氰酸酯/聚氨酯技术 | 350~400 | |
CO2制备PC技术 | 25~35 | |
CO2矿化利用 | 钢渣矿化利用CO2 | 100~150 |
磷石膏矿化利用CO2技术 | 100~150 | |
钾长石加工联合CO2矿化技术 | 20~30 | |
CO2矿化养护混凝土技术 | 4 000~4 500 |
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