Synthesize and characterization of polysulfone membrane for the separation of hydrogen sulfide from natural gas

被引:4
作者
Shokri, Aref [1 ,2 ]
机构
[1] Payame Noor Univ PNU, Dept Chem, Tehran, Iran
[2] Jundi Shapur Res Inst, Dezful, Iran
关键词
Dimethylformamide (DMF); Dimethylacetamide (DMAC); Hydrogen Sulfide; Natural gas; Polysulfone membrane; MIXED MATRIX MEMBRANES; TRANSPORT-PROPERTIES; PHASE INVERSION; PERMEATION; ZEOLITE; H2S; CO2; PERFORMANCE; MORPHOLOGY; PARTICLES;
D O I
10.1016/j.surfin.2021.101233
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The existence of Hydrogen Sulfide in natural gas (N.G) can lead to corrosion in equipment, global warming and so on. So, the separation of Hydrogen Sulfide from N.G is essential. In this study, the Polysulfone (PS) membrane was synthesized with Dimethylacetamide (DMAC) and Dimethylformamide (DMF) as solvent. The SEM (scanning electronic microscopy) images were used to compare prepared membranes by DMF and DMAC. An experimental setup was established and the effect of solvents, PS concentration, temperature and pressure were explored on the separation of H2S from N.G. The best temperature was achieved at 25 degrees C. The results showed that the DMAC solvent was more appropriate than DMF and the amount of selectivity of this kind of membrane was reduced with an increase in temperature and pressure. In M3 membranes (20% of PS, DMAC solvent), which was the best membrane, the permeated amount was increased from 11800 to 490000 Barrer with an increase in pressure from 2.5 to 20 Barg, still the selectivity ratio of H2S to N.G was increased with increase in pressure from 2.5 to 5 Barg at first and then reduced with enhance in pressure until 20 Barg. The maximum selectivity ratio of H2S to N.G was 1.56 for M3 membranes at 25 degrees C and 5 barg, at this condition, the permeated amount of H2S was 119000 Barrer.
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页数:8
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共 36 条
  • [1] Hydrogen separation and purification with poly (4-methyl-1-pentyne)/MIL 53 mixed matrix membrane based on reverse selectivity
    Abedini, Reza
    Omidkhah, Mohammadreza
    Dorosti, Fatereh
    [J]. INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2014, 39 (15) : 7897 - 7909
  • [2] Development of matrimid/zeolite 4A mixed matrix membranes using low boiling point solvent
    Ahmad, Jamil
    Hagg, May-Britt
    [J]. SEPARATION AND PURIFICATION TECHNOLOGY, 2013, 115 : 190 - 197
  • [3] Investigation of a new co-polyimide, 6FDA-bisP and its ZIF-8 mixed matrix membranes for CO2/CH4 separation
    Ahmad, Mohd Zamidi
    Martin-Gil, Violeta
    Perfilov, Viacheslav
    Sysel, Petr
    Fila, Vlastimil
    [J]. SEPARATION AND PURIFICATION TECHNOLOGY, 2018, 207 : 523 - 534
  • [4] Enhanced CO2 transport properties of membranes by embedding nano-porous zeolite particles into Matrimid®5218 matrix
    Amooghin, Abtin Ebadi
    Omidkhah, Mohammadreza
    Kargari, Ali
    [J]. RSC ADVANCES, 2015, 5 (12) : 8552 - 8565
  • [5] Morphology and permeation properties of polysulfone membranes for gas separation: Effects of non-solvent additives and co-solvent
    Aroon, M. A.
    Ismail, A. F.
    Montazer-Rahmati, M. M.
    Matsuura, T.
    [J]. SEPARATION AND PURIFICATION TECHNOLOGY, 2010, 72 (02) : 194 - 202
  • [6] Fabrication and characterization of highly efficient three component CuBTC/graphene oxide/PSF membrane for gas separation application
    Azizi, Alireza
    Feijani, Elahe Ahmadi
    Ghorbani, Zohreh
    Tavasoli, Ahmad
    [J]. INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2021, 46 (02) : 2244 - 2254
  • [7] Bakhtiari O., 2012, J MEMBR SCI TECHNOL, V1, P1
  • [8] Supersonic separation technology for carbon dioxide and hydrogen sulfide removal from natural gas
    Cao, Xuewen
    Guo, Dan
    Sun, Wenjuan
    Zhang, Pan
    Ding, Gaoya
    Bian, Jiang
    [J]. JOURNAL OF CLEANER PRODUCTION, 2021, 288
  • [9] Mixed matrix membranes of aminosilanes grafted FAU/EMT zeolite and cross-linked polyimide for CO2/CH4 separation
    Chen, Xiao Yuan
    Nik, Omid Ghaffari
    Rodrigue, Denis
    Kaliaguine, Serge
    [J]. POLYMER, 2012, 53 (15) : 3269 - 3280
  • [10] Removal of hydrogen sulfide from methane using commercial polyphenylene oxide and Cardo-type polyimide hollow fiber membranes
    Chenar, Mahdi Pourafshari
    Savoji, Houman
    Soltanieh, Mohammad
    Matsuura, Takeshi
    Tabe, Shahram
    [J]. KOREAN JOURNAL OF CHEMICAL ENGINEERING, 2011, 28 (03) : 902 - 913