1 |
Mirfendereski S M, Niazi Z, Mohammadi T. Selective removal of H2S from gas streams with high CO2 concentration using hollow-fiber membrane contractors [J]. Chemical Engineering & Technology, 2019, 42(1): 196-208.
|
2 |
Afsharpour A, Haghtalab A. Simultaneous measurement absorption of CO2 and H2S mixture into aqueous solutions containing Diisopropanolamine blended with 1-butyl-3-methylimidazolium acetate ionic liquid [J]. International Journal of Greenhouse Gas Control, 2017, 58: 71-80.
|
3 |
吴振中, 李发永, 曹作刚. 含高浓度H2S炼厂酸性气体处理新工艺[J]. 石油化工高等学校学报, 2005, 18(4): 12-15.
|
|
Wu Z Z, Li F Y, Cao Z G. New process for treating high concentrated H2S refinery acidic gas [J]. Journal of Petrochemical Universities, 2005, 18(4): 12-15.
|
4 |
Li Y, Huang W J, Zheng D X, et al. Solubilities of CO2 capture absorbents 2-ethoxyethyl ether, 2-butoxyethyl acetate and 2-(2-ethoxyethoxy)ethyl acetate [J]. Fluid Phase Equilibria, 2014, 370: 1-7.
|
5 |
Madeddu C, Errico M, Baratti R. Solvent recovery system for a CO2-MEA reactive absorption-stripping plant [J]. Chemical Engineering Transactions, 2019, 74: 805-810.
|
6 |
Shiflett M B, Niehaus A M S, Yokozeki A. Separation of CO2 and H2S using room-temperature ionic liquid [bmim][MeSO4] [J]. Journal of Chemical & Engineering Data, 2010, 55(11): 4785-4793.
|
7 |
孟艳芳. 常见煤制气中的酸性气体脱除工艺技术特性对比与选择[J]. 山西能源学院学报, 2017, 30(3): 89-90, 94.
|
|
Meng Y F. Comparison and selection of technical characteristics of acid gas removal in common coal gasification [J]. Journal of Shanxi Institute of Energy, 2017, 30(3): 89-90, 94.
|
8 |
陈昌介, 何金龙, 温崇荣. 高含硫天然气净化技术现状及研究方向[J]. 天然气工业, 2013, 33(1): 112-115.
|
|
Chen C J, He J L, Wen C R. A state of the art of high-sulfur natural gas sweetening technology and its research direction [J]. Natural Gas Industry, 2013, 33(1): 112-115.
|
9 |
Ma C Y, Liu C, Lu X H, et al. Techno-economic analysis and performance comparison of aqueous deep eutectic solvent and other physical absorbents for biogas upgrading [J]. Applied Energy, 2018, 225: 437-447.
|
10 |
Yang S, Qian Y, Yang S Y. Development of a full CO2 capture process based on the rectisol wash technology [J]. Industrial & Engineering Chemistry Research, 2016, 55(21): 6186-6193.
|
11 |
赵鹏飞, 李水弟, 王立志. 低温甲醇洗技术及其在煤化工中的应用[J]. 化工进展, 2012, 31(11): 2442-2448.
|
|
Zhao P F, Li S D, Wang L Z. Rectisol technology and its application in coal chemical industry [J]. Chemical Industry and Engineering Progress, 2012, 31(11): 2442-2448.
|
12 |
李正西. NHD脱硫脱碳技术应用 [J]. 煤化工, 2004, 32(3): 53-57.
|
|
Li Z X. Application of the NHD technology for desulfurization and decarbonization [J]. Coal Chemical Industry, 2004, 32(3): 53-57.
|
13 |
林民鸿. NHD气体净化技术理论与实践(上) [J]. 化肥工业, 2000, 27(4): 17-21.
|
|
Lin M H. NHD gas purification technology: theory and practice (Ⅰ) [J]. Journal of the Chemical Fertilizer Industry, 2000, 27(4): 17-21.
|
14 |
Im D, Roh K, Kim J, et al. Economic assessment and optimization of the Selexol process with novel additives [J]. International Journal of Greenhouse Gas Control, 2015, 42: 109-116.
|
15 |
Ramzan N, Shakeel U, Güngör A, et al. Techno-economic analysis of selexol and sulfinol processes for pre-combustion CO2 capture [C]// 2018 International Conference on Power Generation Systems and Renewable Energy Technologies (PGSRET). Islamabad, Pakistan, 2018: 1-6.
|
16 |
邱朋华, 李丹丹, 徐宝龙, 等. 基于Aspen Plus对Selexol分离CO2流程的分析[J]. 中国电机工程学报, 2014, 34(8): 1231-1237.
|
|
Qiu P H, Li D D, Xu B L, et al. Analysis of CO2 separation by Selexol based on Aspen Plus [J]. Proceedings of the CSEE, 2014, 34(8): 1231-1237.
|
17 |
朱林, 艾珍, 王大军, 等. 使用N-甲酰吗啉和聚乙二醇二甲醚溶剂分离H2S和CO2流程模拟比较[J]. 化工学报, 2017, 68: 218-224.
|
|
Zhu L, Ai Z, Wang D J, et al. Simulation and comparison of H2S and CO2 separation processes using N-formyl morpholine and polyethylene glycol dimethyl ether solvent [J]. CIESC Journal, 2017, 68: 218-224.
|
18 |
Mohammed I Y, Samah M, Sabina G, et al. Comparison of SelexolTM and Rectisol® technologies in an integrated gasification combined cycle (IGCC) plant for clean energy production [J]. International Journal of Engineering Research, 2014, 3(12): 742-744.
|
19 |
Kapetaki Z, Brandani P, Brandani S, et al. Process simulation of a dual-stage Selexol process for 95% carbon capture efficiency at an integrated gasification combined cycle power plant [J]. International Journal of Greenhouse Gas Control, 2015, 39: 17-26.
|
20 |
Bagchi B, Sati S, Shilapuram V. Modelling solubility of CO2 and hydrocarbon gas mixture in ionic liquid ([emim][FAP]) using ASPEN Plus [J]. Journal of Molecular Liquids, 2016, 224: 30-42.
|
21 |
Wang Y L, Liu X B, Kraslawski A, et al. A novel process design for CO2 capture and H2S removal from the syngas using ionic liquid [J]. Journal of Cleaner Production, 2019, 213: 480-490.
|
22 |
霍月洋. 利用Aspen Plus计算气体物质的溶解度[J]. 浙江化工, 2015, 46(4): 48-50.
|
|
Huo Y Y. Simulation and calculation for the solubility of gas by Aspen Plus [J]. Zhejiang Chemical Industry, 2015, 46(4): 48-50.
|
23 |
Xu Y M, Schutte R P, Hepler L G. Solubilities of carbon dioxide, hydrogen sulfide and sulfur dioxide in physical solvents [J]. The Canadian Journal of Chemical Engineering, 1992, 70(3): 569-573.
|
24 |
Ros J A, Brilman D W F, Bernhardsen I M, et al. Describing CO2-Absorbent Properties in AspenPlus® [M]// Computer Aided Chemical Engineering. Amsterdam: Elsevier, 2019: 1087-1092.
|