Innovative swirling flow-type microbubble generator for multi-stage DCMD desalination system: Focus on the two-phase flow pattern, bubble size distribution, and its effect on MD performance

被引:42
作者
Kim, Yu-Bin [1 ]
Lee, Ho-Saeng [2 ]
Francis, Lijo [3 ]
Kim, Young-Deuk [4 ]
机构
[1] Hanyang Univ, Dept Mech Design Engn, 222 Wangsimni Ro, Seoul 04763, South Korea
[2] Korea Res Inst Ships & Ocean Engn, SUPRC, 124-32 Simcheungsu Gil, Goseong Gun 219822, Gangwon Do, South Korea
[3] HBKU, QEERI, POB 34110, Doha, Qatar
[4] Hanyang Univ, Dept Mech Engn, 55 Hanyangdaehak Ro, Ansan 15588, Gyeonggi Do, South Korea
关键词
Membrane distillation; Microbubble generator; Permeation flux enhancement; Two-phase flow; Seawater desalination; DIRECT-CONTACT MEMBRANE; HEAT-TRANSFER; MASS-TRANSFER; TEMPERATURE POLARIZATION; SEAWATER DESALINATION; AQUEOUS-SOLUTIONS; MODULE DESIGN; AIR-GAP; DISTILLATION; SPACER;
D O I
10.1016/j.memsci.2019.117197
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this study, we proposed a novel air-assisted swirling flow-type microbubble generator (MBG) to improve the downstream transmembrane flux of a multistage direct contact membrane distillation (MDCMD) based seawater desalination system, and experimentally demonstrated its performance under various operating conditions. To simulate the downstream operating conditions of the MDCMD system, low temperature and high concentration conditions were implemented on the feed side in the experiments. It was observed that the formation of a gas-liquid two-phase flow in the feed stream demonstrated a positive influence on the performance of the direct contact membrane distillation (DCMD) process; particularly, microbubbles less than 100 mu m performed an important role in improving the heat and mass transfer. The DCMD performance using MBG was demonstrated to be more pronounced at lower feed temperatures and higher feed flow rates, where the enhancement in permeation flux was as high as 37%. The optimal air flow rate to achieve maximum DCMD performance was determined to be 50 cc/min at a given feed flow rate, while a further increase in air flow rate incurred a slug flow in the feed channel, which resulted in a decrease in the number of microbubbles and hence a decrease in the DCMD performance. In addition, the process performance was evaluated using highly concentrated brine as the feed solution, and the results demonstrated the feasibility of applying MBG to practical desalination processes.
引用
收藏
页数:15
相关论文
共 75 条
[1]   Potential of membrane distillation in seawater desalination: Thermal efficiency, sensitivity study and cost estimation [J].
Al-Obaidani, Sulaiman ;
Curcio, Efrem ;
Macedonio, Francesca ;
Di Profio, Gianluca ;
Ai-Hinai, Hilal ;
Drioli, Enrico .
JOURNAL OF MEMBRANE SCIENCE, 2008, 323 (01) :85-98
[2]   Modelling flow and heat transfer in spacer-filled membrane distillation channels using open source CFD code [J].
Al-Sharif, Sharaf ;
Albeirutty, Mohammed ;
Cipollina, Andrea ;
Micale, Giorgio .
DESALINATION, 2013, 311 :103-112
[3]   Membrane distillation: A comprehensive review [J].
Alkhudhiri, Abdullah ;
Darwish, Naif ;
Hilal, Nidal .
DESALINATION, 2012, 287 :2-18
[4]   Experimental and theoretical analyses of temperature polarization effect in vacuum membrane distillation [J].
Alsaadi, Ahmad S. ;
Francis, Lijo ;
Amy, Gary L. ;
Ghaffour, Noreddine .
JOURNAL OF MEMBRANE SCIENCE, 2014, 471 :138-148
[5]   A flow pattern independent drift flux model based void fraction correlation for a wide range of gas-liquid two phase flow [J].
Bhagwat, Swanand M. ;
Ghajar, Afshin J. .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2014, 59 :186-205
[6]   A comparative study of gas hold-up, bubble size, interfacial area and mass transfer coefficients in stirred gas-liquid reactors and bubble columns [J].
Bouaifi, M ;
Hebrard, G ;
Bastoul, D ;
Roustan, M .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2001, 40 (02) :97-111
[7]   Heat transfer intensification and scaling mitigation in bubbling-enhanced membrane distillation for brine concentration [J].
Chen, Guizi ;
Yang, Xing ;
Lu, Yinghong ;
Wang, Rong ;
Fane, Anthony G. .
JOURNAL OF MEMBRANE SCIENCE, 2014, 470 :60-69
[8]   Performance enhancement and scaling control with gas bubbling in direct contact membrane distillation [J].
Chen, Guizi ;
Yang, Xing ;
Wang, Rong ;
Fane, Anthony G. .
DESALINATION, 2013, 308 :47-55
[9]   Theoretical modeling and experimental analysis of direct contact membrane distillation [J].
Chen, Tsung-Ching ;
Ho, Chii-Dong ;
Yeh, Ho-Ming .
JOURNAL OF MEMBRANE SCIENCE, 2009, 330 (1-2) :279-287
[10]   EXPERIMENTAL INVESTIGATION OF SWIRLING VORTEX MOTION IN JETS [J].
CHIGIER, NA ;
CHERVINS.A .
JOURNAL OF APPLIED MECHANICS, 1967, 34 (02) :443-&