Introduction of a novel amino-agarose (AAG) derivative as a fixed facilitated transport carrier to prepare newly asymmetric PES/AAG membranes for CO2 removal

Greenhouse Gases: Science and Technology

Volumn 5, Issue 6, 2015, Pages 701-713

  Seidi, Farzad ^a   Salarabadi, Mahsa Babaei ^b   Saedi, Shahab ^a   Modadi, Loghman ^b   Shamsabadi, Ahmad Arabi ^c   Nikravesh, Bahar ^a  

^a ISLAMIC AZAD UNIVERSITY   (Iran)

^b UNIVERSITY OF KURDISTAN   (Iran)

^c Marun Petrochemical Company   (Iran)

Author keywords

amino agarose; carbon dioxide; fixed facilitated transport; membrane; methane; polyethersulfone

Indexed keywords

ADDITIVES; BLENDING; CARBON DIOXIDE; FOURIER TRANSFORM INFRARED SPECTROSCOPY; GRAVIMETRIC ANALYSIS; MEMBRANES; METHANE; NUCLEAR MAGNETIC RESONANCE; NUCLEAR MAGNETIC RESONANCE SPECTROSCOPY; SCANNING ELECTRON MICROSCOPY; THERMODYNAMIC STABILITY; THERMOGRAVIMETRIC ANALYSIS;

AGAROSE; FACILITATED TRANSPORT; FEED PRESSURE; MEMBRANES MORPHOLOGY; PES MEMBRANES; POLYETHERSULFONES; POLYMERIC ADDITIVES; THERMAL GRAVIMETRIC ANALYSIS;

GAS PERMEABLE MEMBRANES;

EID: 84930904438     PISSN: None     EISSN: 21523878     Source Type: Journal    
DOI: 10.1002/ghg.1514     Document Type: Article

References (49)

1. 2 removal from natural gas-A review. Prog Polym Sci 34 (6): 561-580 (2009).
2. 2 from gas mixtures. J Mol Struct 739 (1-3): 57-74 (2005).
3. 2 sorption and transport behavior of ODPA-based polyetherimide polymer films. Polymer 51 (17): 3907-3917 (2010).
4. 2-selective adsorptive silica nanoparticles. Chin J Chem Eng 19 (5): 821-832 (2011).
5. Wang D, Li K, and, Teo W, Highly permeable polyethersulfone hollow fiber gas separation membranes prepared using water as non-solvent additive. J Membr Sci 176 (2): 147-158 (2000).
6. Hamad FA, Chowdhury G, and, Matsuura T, Sulfonated polyphenylene oxide-polyethersulfone thin-film composite membranes: effect of counterions on the gas transport properties. J Membr Sci 191 (1): 71-83 (2001).
7. Hamad F, Khulbe KC, and, Matsuura T, Comparison of gas separation performance and morphology of homogeneous and composite PPO membranes. J Membr Sci 256 (1-2): 29-37 (2005).
8. 2-facilitated transport through poly (N-vinyl-g-sodium aminobutyrate-co-sodium acrylate)/polysulfone composite membranes. J Appl Polym Sci 100 (1): 275-282 (2006).
9. Sridhar S, Veerapur R, Patil M, Gudasi K, and, Aminabhavi T, Matrimid polyimide membranes for the separation of carbon dioxide from methane. J Appl Polym Sci 106 (3): 1585-1594 (2007).
10. Sadrzadeh M, Amirilargani M, Shahidi K, and, Mohammadi T, Gas permeation through a synthesized composite PDMS/PES membrane. J Membr Sci 342 (1-2): 236-250 (2009).
11. Han J, Lee W, Choi JM, Patel R, and, Min BR, Characterization of polyethersulfone/polyimide blend membranes prepared by a dry/wet phase inversion: Precipitation kinetics, morphology and gas separation. J Membr Sci 351 (1-2): 141-148 (2010).
12. Ismail AF, Norida R, Rahman W, Matsuura T, and, Hashemifard S, Preparation and characterization of hyperthin-skinned and high performances asymmetric polyethersulfone membrane for gas separation. Desalination 273 (1): 93-104 (2011).
13. Saedi S, Madaeni SS, Arabi Shamsabadi A, and, Mottaghi F, The effect of surfactants on the structure and performance of PES membrane for separation of carbon dioxide from methane. Sep Purif Technol 99: 104-119 (2012).
14. El-Azzami LA, and, Grulke EA, Carbon dioxide separation from hydrogen and nitrogen by fixed facilitated transport in swollen chitosan membranes. J Membr Sci 323 (2): 225-234 (2008).
15. 2 facilitated transport. C R Chim 13 (3): 372-379 (2010).
16. Blinova NV, and, Svec F, Functionalized polyaniline-based composite membranes with vastly improved performance for separation of carbon dioxide from methane. J Membr Sci 423-424: 514-521 (2012).
17. 2 separation performance of novel fixed carrier composite membranes prepared by interfacial polymerization. J Membr Sci 283 (1-2): 346-356 (2006).
18. Shen J, Qiu J, Wu L, and, Gao C, Facilitated transport of carbon dioxide through poly(2-N,N-dimethyl aminoethyl methacrylate-co-acrylic acid sodium) membrane. Sep Purif Technol 51 (3): 345-351 (2006).
19. 2 in novel PVAm/PVA blend membrane. J Membr Sci 340 (1-2): 154-163 (2009).
20. Cai Y, Wang Z, Yi C, Bai Y, Wang J, and, Wang S, Gas transport property of polyallylamine-poly(vinyl alcohol)/polysulfone composite membranes. J Membr Sci 310 (1-2): 184-196 (2008).
21. 2 through polyvinylamine/polyethlene glycol blend membranes. Desalination 193 (1-3): 90-96 (2006).
22. 2 selectively permeating membranes containing PETEDA dendrimer. J Membr Sci 290 (1-2): 250-258 (2007).
23. 4 mixtures. Desalination 223 (1-3): 425-437 (2008).
24. 2 through polyethylenimine/poly(vinyl alcohol) blend membrane. J Membr Sci 163 (2): 221-227 (1999).
25. Wu J, and, YuanQ, Gas permeability of a novel cellulose membrane. J Membr Sci 204 (1): 185-194 (2002).
26. 2 through chitosan membrane swollen by water vapor in feed gas. Angew Makromol Chem 248 (1): 85-94 (1997).
27. 2 gas sorption and permeation behavior of chitosan membrane. Korean J Chem Eng 15 (2): 223-226 (1998).
28. Spagna G, Barbagallo RN, Pifferi PG, Blanco RM, and, Guisan JM, Stabilization of a b-glucosidase from Aspergillus niger by binding to an amine agarose gel. J Mol Catal B: Enzym 11 (2): 63-69 (2000).
29. 2 through integrally-skinned asymmetric polyethersulfone membrane using a novel synthesized Poly (acrylonitrile-co-N, N-Dimethylaminopropyl acrylamide). Chem Eng J 236: 263-273 (2014).
30. Saedi S, Madaeni SS, Seidi F, Shamsabadi AA, and, Laki S, Synthesis and application of a novel Amino-Starch derivative as a new polymeric additive for fixed facilitated transport of carbon dioxide through an asymmetric polyethersulfone (PES) membrane. Int J Greenh Gas Con 19: 126-137 (2013).
31. Li Y, Cao C, Chung TS, and, Pramoda KP, Fabrication of dual-layer polyethersulfone (PES) hollow fiber membranes with an ultrathin dense-selective layer for gas separation. J Membr Sci 245 (1): 53-60 (2004).
32. Jansen J, Macchione M, and, Drioli E, High flux asymmetric gas separation membranes of modified poly (ether ether ketone) prepared by the dry phase inversion technique. J Membr Sci 255 (1): 167-180 (2005).
33. Freeman B, Yampolskii Y, and, Pinnau I, Materials Science of Membranes for Gas and Vapor Separation, John Wiley & Sons, West Sussex, England (2006).
34. Khulbe K, Feng C, and, Matsuura T, Synthetic Membranes for Membrane Processes, Springer, Berlin Heidelberg, pp. 5-18 (2008).
35. 2 removal from flue gas. Sep Purif Technol 63 (3): 524-530 (2008).
36. 2 separations. J Membr Sci 320 (1-2): 65-72 (2008).
37. Ismail AF, Rahim N, Mustafa A, Matsuura T, Ng B, Abdullah S, and, Hashemifard S, Gas separation performance of polyethersulfone/multi-walled carbon nanotubes mixed matrix membranes. Sep Purif Technol 80 (1): 20-31 (2011).
38. Saljoughi E, Amirilargani M, and, Mohammadi T, Effect of PEG additive and coagulation bath temperature on the morphology, permeability and thermal/chemical stability of asymmetric CA membranes. Desalination 262 (1-3): 72-78 (2010).
39. 4) as an additive in the casting solution. Desalination 258 (1): 79-86 (2010).
40. Ma Y, Shi F, Ma J, Wu M, Zhang J, and, Gao C, Effect of PEG additive on the morphology and performance of polysulfone ultrafiltration membranes. Desalination 272 (1): 51-58 (2011).
41. Saedi S, Madaeni SS, Hassanzadeh K, Shamsabadi AA, and, Laki S, The effect of polyurethane on the structure and performance of PES membrane for separation of carbon dioxide from methane. J Ind Eng Chem 20 (4): 1916-1929 (2014).
42. Jayalakshmi A, Rajesh S, and, Mohan D, Fouling propensity and separation efficiency of epoxidated polyethersulfone incorporated cellulose acetate ultrafiltration membrane in the retention of proteins. App Surf Science 258 (24): 9770-9781 (2012).
43. Aitken C, Koros W, and, Paul D, Effect of structural symmetry on gas transport properties of polysulfones. Macromolecules. 25 (13): 3424-3434 (1992).
44. Visser T, Koops GH, and, Wessling M, On the subtle balance between competitive sorption and plasticization effects in asymmetric hollow fiber gas separation membranes. J Membr Sci 252 (1-2): 265-277 (2005).
45. 2 through ethylenediamine-fixed cation-exchange polysaccharide membranes. J Membr Sci 245 (1-2): 79-86 (2004).
46. 2 through new facilitated transport membranes. Desalination 145 (1-3): 385-388 (2002).
47. 2 separation: Performance with mixed gases. Sep Purif Technol 62 (1): 110-117 (2008).
48. 2 separation with sulfonated PEEK membranes. J Membr Sci 372 (1-2): 87-96 (2011).
49. 2 by using novel facilitated transport membrane at elevated temperatures and pressures. J Membr Sci 291 (1-2) 157v164 (2007).