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Effect of Different Additives on Separation Performance of Flat Sheet PVDF Membrane Contactor | ||
Journal of Chemical and Petroleum Engineering | ||
مقاله 5، دوره 52، شماره 2، اسفند 2018، صفحه 157-167 اصل مقاله (2.17 M) | ||
نوع مقاله: Research Paper | ||
شناسه دیجیتال (DOI): 10.22059/jchpe.2018.258530.1233 | ||
نویسندگان | ||
Mohammad Khosravi1؛ Ali Ghadimi2؛ Zahra Mansourpour* 1؛ Azadeh Ghaee3؛ Behrouz Sadatnia4 | ||
1School of Chemical Engineering, College of Engineering, University of Tehran, Tehran, Iran | ||
2Department of Petrochemicals Synthesis, Iran Polymer and Petrochemical Institute, Tehran, Iran | ||
3Department of life science engineering, Faculty of new sciences and technologies, University of Tehran, Tehran, Iran | ||
4Department of Biomaterials, Iran Polymer and Petrochemical Institute, Tehran, Iran | ||
چکیده | ||
This paper investigates effects of different additives on morphology and subsequently, separation performance of asymmetric flat sheet Polyvinylidene fluoride (PVDF) membranes to separate CO2 using membrane contractor. Five different additives from different chemical families including Lithium chloride (salt), Polyethylene glycol 400 (polymer), glycerol (weak anti-solvents), methanol (alcohols) and acetic acid (weak secondary solvents) were used for controlling the morphology of the fabricated membranes. The fabricated PVDF membranes were applied to separate CO2 from a gas mixture of (20/80 wt/wt) CO2/N2 by contacting with (20/80 wt/wt) Monoethanolamine/H2O as absorbent. The investigations revealed that among the all considered additives, glycerol has the most promising effect on the performance of CO2 separation from the feed gas mixture. Effects of operational parameters such as flow rate and temperature of absorbents on the separation performance were also studied. Investigations showed that the lowest level of temperature (30 ºC) and the highest level of the flow rate of absorbent (500 ) provide better separation performance. Additionally, the presence of glycerol increased absorption performance (η) from 0.63 to 0.78 (at the lowest level of flow rate) and from 0.79 to 0.91 (at the highest level of flow rate) compared to the bare PVDF membranes. | ||
کلیدواژهها | ||
Absorption Performance؛ Membrane Contactor؛ Morphology؛ Operating Parameters | ||
مراجع | ||
[1] Atchariyawut, S., Jiraratananon, R. and Wang, R. (2007). “Separation of CO2 from CH4 by using gas-liquid membrane contacting process.” Journal of Membrane Science, Vol. 304, No. 1-2, pp. 163-172.
[2] Ismail, A.F. and Mansourizadeh, A.A. (2010). “comparative study on the structure and performance of porous polyvinylidene fluoride and polysulfone hollow fiber membranes for CO2 absorption.” Journal of Membrane Science, Vol. 365, No. 1–2, pp. 319-328.
[3] Bakeri, G., Matsuura, T. and Ismail, A. F. (2011). “The effect of phase inversion promoters on the structure and performance of polyetherimide hollow fiber membrane using in gas-liquid contacting process.” Journal of Membrane Science, Vol. 383, No. 1–2, pp. 159-169.
[4] Qi, Z., and Cussler, E. L. (1985). “Microporous hollow fibers for gas absorption: I. Mass transfer in the liquid.” Journal of Membrane Science, Vol. 23, No. 3, pp. 321-332.
[5] Qi, Z. and Cussler, E. L. (1985). “Microporous hollow fibers for gas absorption: II. Mass transfer across the membrane.” Journal of Membrane Science, Vol. 23, No. 3, pp. 333-345.
[6] Tan, X., Tan, S. P., Teo, W. K. and Li, K. (2006). “Polyvinylidene fluoride (PVDF) hollow fibre membranes for ammonia removal from water.” Journal of Membrane Science, Vol. 271, No. 1–2, pp. 59-68.
[7] Bhaumik, D., Majumdar, S., Fan, Q. and Sirkar, K.K., (2004). “Hollow fiber membrane degassing in ultrapure water and microbiocontamination.” Journal of Membrane Science, Vol. 235, No. 1–2, pp. 31-41.
[8] Faiz, R., Li, K. and Al-Marzouqi, M. (2014). “H2S absorption at high pressure using hollow fibre membrane contactors.” Chemical Engineering and Processing: Process Intensification, Vol. 83, pp. 33-42.
[9] Agrahari, G. K., Rawat, A., Verma, N., Bhattacharya, P. K., (2013). “Removal of dissolved H2S from wastewater using hollow fiber membrane contactor: Experimental and mathematical analysis.” Desalination, Vol. 314, pp. 34-42.
[10] Norouzbahari, S., Shahhosseini, S. and Ghaemi, A. (2016). “Chemical absorption of CO2 into an aqueous piperazine (PZ) solution: development and validation of a rigorous dynamic rate-based model.” RSC Advances, Vol. 6, No. 46, pp. 40017-40032.
[11] Norouzbahari, S., Shahhosseini, S. and Ghaemi, A. (2015). “CO2 chemical absorption into aqueous solutions of piperazine: modeling of kinetics and mass transfer rate.” Journal of Natural Gas Science and Engineering, Vol. 26, pp. 1059-1067.
[12] Rabiee, H., Ghadimi, A., Abbasi, S. and Mohammadi, T. (2015). “CO2 separation performance of poly(ether-b-amide6)/PTMEG blended membranes: Permeation and sorption properties.” Chemical Engineering Research and Design, Vol. 98, pp. 96-106.
[13] Ghadimi, A., Mohammadi, T. and Kasiri, N. (2016). “Mathematical modeling of the gas transport through PEBAX/(nonporous silica) nanocomposite membranes: Development based on Van Amerongen and Van Krevelen relations.” Separation and Purification Technology, Vol. 170, pp. 280-293.
[14] Karoor, S. and Sirkar, K. K. (1993) “Gas absorption studies in microporous hollow fiber membrane modules.” Industrial & Engineering Chemistry Research, Vol. 32, No. 4, pp. 674-684.
[15] Kim, Y. S. and Yang, S. M. (2000). “Absorption of carbon dioxide through hollow fiber membranes using various aqueous absorbents.” Separation and Purification Technology, Vol. 21, No. 1–2, pp. 101-109.
[16] Mansourizadeh, A., Ismail, A. F., Abdullah, M.S. and Ng, B.C. (2010) “Preparation of polyvinylidene fluoride hollow fiber membranes for CO2 absorption using phase-inversion promoter additives.” Journal of Membrane Science, Vol. 355, No. 1–2, pp. 200-207.
[17] Shi, L., Wang, R., Cao, Y., Liang, D. T. and Tay, J.H. (2008). “Effect of additives on the fabrication of poly(vinylidene fluoride-co-hexafluropropylene) (PVDF-HFP) asymmetric microporous hollow fiber membranes.” Journal of Membrane Science, Vol. 315, No. 1–2, pp. 195-204.
[18] Naim, R., Ismail, A. F. and Mansourizadeh, A. (2012). “Preparation of microporous PVDF hollow fiber membrane contactors for CO2 stripping from diethanolamine solution.” Journal of Membrane Science, Vol. 392–393, pp. 29-37.
[19] Bottino, A., Capannelli, G., Munari, S. and Turturro, A. (1988). “High performance ultrafiltration membranes cast from LiCl doped solutions.” Desalination, Vol. 68, No. 2–3, pp. 167-177.
[20] Kong, J. and Li, K. (2001) “Preparation of PVDF hollow-fiber membranes via immersion precipitation.” Journal of Applied Polymer Science, Vol. 81, No. 7, pp. 1643-1653.
[21] Khayet, M. and Matsuura, T. “Preparation and Characterization of Polyvinylidene Fluoride Membranes for Membrane Distillation.” Industrial & Engineering Chemistry Research, Vol. 40, No. 24, pp. 5710-5718.
[22] Wang, W. P., Lin, H. T. and Ho, C. D. (2006) “An analytical study of laminar co-current flow gas absorption through a parallel-plate gas-liquid membrane contactor.” Journal of Membrane Science, Vol. 278, No. 1–2, pp. 181-189.
[23] Paul, S., Ghoshal, A. K. and Mandal, B. (2008). “Theoretical studies on separation of CO2 by single and blended aqueous alkanolamine solvents in flat sheet membrane contactor (FSMC).” Chemical Engineering Journal, Vol. 144, No. 3, pp. 352-360.
[24] Bakeri, G., Ismail, A. F., Rana, D. and Matsuura, T. (2012) “Development of high performance surface modified polyetherimide hollow fiber membrane for gas-liquid contacting processes.” Chemical Engineering Journal, Vol. 198–199, pp. 327-337.
[25] Burggraaf, A. J. and Cot, L. (1996). Fundamentals of Inorganic Membrane Science and Technology. Elsevier Science. Amsterdam.
[26] Li, K. (2007). Ceramic Membranes for Separation and Reaction. John Wiley & Sons.
[27] Mansourizadeh, A. and Ismail, A.F. (2010) “Effect of additives on the structure and performance of polysulfone hollow fiber membranes for CO2 absorption.” Journal of Membrane Science, Vol. 348, No. 1–2, pp. 260-267.
[28] Zhang, Y. and Wang, R. (2013). “Fabrication of novel polyetherimide-fluorinated silica organic-inorganic composite hollow fiber membranes intended for membrane contactor application.” Journal of Membrane Science, Vol. 443, pp. 170-180.
[29] Wang, R., Li, D.F., Zhou, C., Liu, M. and Liang, D.T. (2004). “Impact of DEA solutions with and without CO2 loading on porous polypropylene membranes intended for use as contactors.” Journal of Membrane Science, Vol. 229, No. 1–2, pp.147-157.
[30] Feng, C., Wang, R., Shi, B., Li, G. and Wu, Y. (2006) “Factors affecting pore structure and performance of poly(vinylidene fluoride-co-hexafluoro propylene) asymmetric porous membrane.” Journal of Membrane Science, Vol. 277, No. 1–2, pp. 55-64.
[31] Naim, R., Ismail, A. F. and Mansourizadeh, A. (2012). “Effect of non-solvent additives on the structure and performance of PVDF hollow fiber membrane contactor for CO2 stripping.” Journal of Membrane Science, Vol. 423-424, pp. 503-513.
[32] Mansourizadeh, A. and Ismail, A. F. (2011). “Preparation and characterization of porous PVDF hollow fiber membranes for CO2 absorption: Effect of different non-solvent additives in the polymer dope.” International Journal of Greenhouse Gas Control, Vol. 5, No. 4, pp. 640-648.
[33] Xu, Z. K., Shen, L. Q., Yang, Q., Liu, F., Wang, S. Y. and Xu, Y. Y. (2003). “Ultrafiltration hollow fiber membranes from poly(ether imide): preparation, morphologies and properties.” Journal of Membrane Science, Vol. 223, No. 1–2, pp. 105-118. | ||
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