Influence of Air-Gap Length on CO2 Stripping from Diethanolamine Solution and Water Performance of Surface Modified PVDF Hollow Fiber Membrane Contactor

Document Type : Research Article

Authors

1 Department of Chemical Engineering, Gachsaran Branch, Islamic Azad University, Gachsaran, I.R. IRAN

2 Advanced Membrane Technology Research Center (AMTEC), Universiti Teknologi Malaysia (UTM), 81310 Skudai, Johor, MALAYSIA

3 Australian Institute for Bioengineering and Nanotechnology (AIBN), University of Queensland, Brisbane 4072, QLD, AUSTRALIA

Abstract

Surface Modifying Macromolecule (SMM) blended PVDF hollow fibers (HFs) were spun at different air-gaps (o to 20 cm) and used for CO2 stripping from aqueous DEA solution and water. The manufactured fibers were first subjected to various characterization tests such as contact angle and critical water entry pressure measurement to evaluate the HF hydrophobicity and wetting resistance, respectively. The pure helium permeation experiments were also conducted to obtain membrane pore size and effective porosity. Morphology of the HFs was investigated by Scanning Electron Microscopy (SEM) and Atomic Force Microscopy (AFM). The SEM images showed that both outer and inner diameters of HFs decreased significantly by increasing air-gap length which mainly because of elongation of HF caused by gravity while traveling through the air–gap. Also, the gradual decrease in roughness on the external surface of the produced HFs was observed from the AFM images.  It was found that the increase of liquid velocity enhances the CO2 stripping flux. It was found that 10 cm air-gap gave maximum stripping flux of 3.34×10-2 and 1.34×10-3 (mol/m2 s) for DEA solution and water, respectively. The increase in gas velocity, on the other hand, did not affect the stripping flux significantly. It was observed that the increase of temperature from 25 to 80 oC led to marked enhancement of stripping flux from 6.30×10-3 to 3.34×10-2 (mol/m2 s) and 6.5×10-5 to 1.34×10-3 (mol/m2 s), for DEA solution and water, respectively. Furthermore, the increase in DEA concentration from 0.25 to 1 mol/L, led to enhancement of the stripping flux from 6.84×10-3 to 3.34×10-2 (mol/m2 s) at a liquid velocity of 0.7 m/s. It was concluded that the HF spun at 10 cm air-gap exhibited the best stripping performance among all fabricated HFs.

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[1] Naim R., Ismail A.F., Cheer N.B., Abdullah M.S., Polyvinylidene Fluoride and Polyetherimide Hollow Fiber Membranes for CO2 Stripping in Membrane Contactor, Chemical Engineering Research and Design. 92(7):  1391-1398 (2014).
[2] Koonaphapdeelert S., Wu Z., Li K., Carbon Dioxide Stripping in Ceramic Hollow Fibre Membrane Contactors, Chemical Engineering Science, 64(1): 1-8 (2009).
[3] Khaisri S., deMontigny D., Tontiwachwuthikul P., Jiraratananon R., CO2 Stripping from Monoethanolamine Using a Membrane Contactor, Journal of Membrane Science, 376(1–2): 110-118 (2011).
[4] Rahbari-Sisakht M., Ismail A.F., Rana D., Matsuura T., Effect of Novel Surface Modifying Macromolecules on Morphology and Performance of Polysulfone Hollow fiber Membrane Contactor for CO2 Absorption, Separation and Purification Technology, 99: 61-68 (2012).
[5] Rahbari-Sisakht M., Ismail A.F., Rana D., Matsuura T., Emadzadeh D., Effect of SMM Concentration on Morphology and Performance of Surface Modified PVDF Hollow Fiber Membrane Contactor for CO2 Absorption, Separation and Purification Technology, 116: 67-72 (2013).
[6] Rahbari-Sisakht M., Ismail A.F., Rana D., Matsuura T., Emadzadeh D., Carbon Dioxide Stripping from Water Through Porous Polysulfone Hollow Fiber Membrane Contactor, Separation and Purification Technology, 108: 119-123 (2013).
[8] Ghasem N., Al-Marzouqi M., Duidar A., Effect of PVDF Concentration on the Morphology and Performance of Hollow Fiber Membrane Employed as Gas–Liquid Membrane Contactor for CO2 Absorption, Separation and Purification Technology, 98: 174-185 (2012).
[9] Ghasem N., Al-Marzouqi M., Abdul Rahim N., Modeling of CO2 Absorption in a Membrane Contactor Considering Solvent Evaporation, Separation and Purification Technology, 110: 1-10 (2013).
[10] Korminouri F., Rahbari-Sisakht M., Rana D., Matsuura T., Ismail A.F., Study on the Effect of Air–Gap Length on Properties and Performance of Surface Modified PVDF Hollow Fiber Membrane Contactor for Carbon Dioxide Absorption, Separation and Purification Technology, 132: 601-609 (2014).
[11] Korminouri F., Rahbari-Sisakht M., Matsuura T., Ismail A.F., Surface Modification of Polysulfone Hollow Fiber Membrane Spun under Different air-Gap Lengths for Carbon Dioxide Absorption in Membrane Contactor System, Chemical Engineering Journal, 264: 453-461 (2015).
[12] Simioni M., Kentish S.E., Stevens G.W., Membrane Stripping: Desorption of Carbon Dioxide from Alkali Solvents, Journal of Membrane Science, 378(1–2): 18-27 (2011).
[13] Rahbari-Sisakht M., Korminouri F., Emadzadeh D., Matsuura T., Ismail A.F., Effect of Air-Gap Length on Carbon Dioxide Stripping Performance of a Surface Modified Polysulfone Hollow Fiber Membrane Contactor, RSC Advances, 4(103). 59519-59527 (2014).
[15] Suk D.E., Matsuura T., Park H.B., Lee Y.M., Synthesis of a New Type of Surface Modifying Macromolecules (nSMM) and Characterization and Testing of nSMM Blended Membranes for Membrane Distillation, Journal of Membrane Science, 277(1–2): 177-185 (2006).
[16] Tsai H.A., Huang D.H., Fan S.C., Wang Y.C., Li C.L., Lee K.R., Lai J.Y., Investigation of Surfactant Addition Effect on the Vapor Permeation of Aqueous Ethanol Mixtures Through Polysulfone Hollow Fiber Membranes, Journal of Membrane Science, 198(2): 245-258 (2002).
[17] Zhang X., Wen Y., Yang Y., Liu L., Effect of Air-Gap Distance on the Formation and Characterization of Hollow Polyacrylonitrile (PAN) Nascent Fibers. Journal of Macromolecular Science, Part B., 47(6): 1039-1049 (2008).
[18] Liu R.X., Qiao X.Y., Chung T.-S., Dual-Layer P84/Polyethersulfone Hollow Fibers for Pervaporation Dehydration of Isopropanol, Journal of Membrane Science, 294(1–2): 103-114 (2007).
[19] Khulbe K.C., Feng C.Y., Hamad F., Matsuura T., Khayet M., Structural and Performance Study of Micro Porous Polyetherimide Hollow Fiber Membranes Prepared at Different Air-Gap, Journal of Membrane Science, 245(1–2): 191-198 (2004).
[20] Wang D., Li K., Teo W.K., Highly Permeable Polyethersulfone Hollow Fiber Gas Separation Membranes Prepared Using Water as Non-Solvent Additive, Journal of Membrane Science, 176(2): 147-158 (2000).
[21] Khayet M., The Effects of Air Gap Length on the Internal and External Morphology of Hollow Fiber Membranes, Chemical Engineering Science, 58(14): 3091-3104 (2003).
[22] Khayet M., García-Payo M.C., Qusay F.A., Zubaidy M.A., Structural and Performance Studies of Poly(vinyl chloride) Hollow Fiber Membranes Prepared at Different Air Gap Lengths, Journal of Membrane Science, 330(1–2): 30-39 (2009).
[23] Naim R., Ismail A.F., Mansourizadeh A., Effect of Non-Solvent Additives on the Structure and Performance of PVDF Hollow Fiber Membrane Contactor for CO2 Stripping, Journal of Membrane Science, 423–424: 503-513 (2012).
[24] Naim R., Khulbe K.C., Ismail A.F., Matsuura T., Characterization of PVDF Hollow Fiber Membrane for CO2 Stripping by Atomic Force Microscopy Analysis, Separation and Purification Technology, 109: 98-106 (2013).
[26] Rahbari-Sisakht M., Ismail A.F., Rana D., Matsuura T., Carbon Dioxide Stripping from Diethanolamine Solution Through Porous Surface Modified PVDF Hollow Fiber Membrane Contactor, Journal of Membrane Science, 427: 270-275
(2013).
[27] Ismail A.F., Dunkin I.R., Gallivan S.L., Shilton S.J., Production of Super Selective Polysulfone Hollow Fiber Membranes for Gas Separation, Polymer, 40(23): 6499-6506 (1999).
[28] Rahbari-Sisakht M., Ismail A.F., Matsuura T., Development of Asymmetric Polysulfone Hollow Fiber Membrane Contactor for CO2 Absorption, Separation and Purification Technology, 86: 215-220 (2012).
[29] Rahbari-sisakht M., Ismail A.F., Matsuura T., Effect of Bore Fluid Composition on Structure and Performance of Asymmetric Polysulfone Hollow Fiber Membrane Contactor for CO2 Absorption, Separation and Purification Technology, 88: 99-106 (2012).
[30] Rahbari-Sisakht M., Ismail A.F., Rana D., Matsuura T., A Novel Surface Modified Polyvinylidene Fluoride Hollow Fiber Membrane contactor for CO2 Absorption, Journal of Membrane Science, 415–416: 221-228 (2012).
[31] Khayet M., Feng C.Y., Khulbe K.C., Matsuura T., Study on the Effect of a Non-Solvent Additive on the Morphology and Performance of Ultrafiltration Hollow-Fiber Membranes, Desalination, 148(1–3): 321-327 (2002).
[32] Li M.-H. Chang B.-C., Solubilities of Carbon Dioxide in Water + Monoethanolamine + 2-Amino-2-methyl-1-propanol. Journal of Chemical & Engineering Data. 39(3): 448-452 (1994).
[33] Rahbari-Sisakht M., Rana D., Matsuura T., Emadzadeh D., Padaki M., Ismail A.F., Study on CO2 Stripping from Water Through Novel Surface Modified PVDF Hollow Fiber Membrane Contactor, Chemical Engineering Journal, 246: 306-310 (2014).
[34] Khulbe K.C., Feng C.Y., Matsuura T., Mosqueada-Jimenaez D.C., Rafat M., Kingston D., Narbaitz R.M., Khayet M., Characterization of Surface-Modified Hollow Fiber Polyethersulfone Membranes Prepared at Different Air Gaps, Journal of Applied Polymer Science,104(2): 710-721 (2007).
[35] Mansourizadeh A. Ismail A.F., CO2 Stripping from Water Through Porous PVDF Hollow Fiber Membrane Cntactor, Desalination, 273(2–3): 386-390 (2011).
[36] Weiland R.H., Rawal M., and Rice R.G., Stripping of Carbon Dioxide from Monoethanolamine Solutions in a Packed Column, AIChE Journal, 28(6): 963-973 (1982).
[37] Mokhatab S., Poe W.A., Speight J.G., "Handbook of Natural Gas Transmission and Processing", Gulf Professional Publishing, Burlington (2006).