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Structure design and performance study of tubular air gap membrane distillation module
Authors: JI Zhongguang,LI Wei, WANG Haixia
Units: National Engineering Laboratory of Biohydrometallurgy, GRINM Group Corporation Limited. Beijing 101407, China;GRINM Resources and Environment Tech. Co., Ltd. Beijing 101407, China; General Research Institute for Nonferrous Metals. Beijing 100088, China; GRIMAT Engineering Institute Co., Ltd.Beijing 101407,China
KeyWords: Membrane distillation; flux; Mass transfer;Membrane fouling; Wettability
ClassificationCode:X52
year,volume(issue):pagination: 2021,41(2):88-95

Abstract:
 Low membrane flux and serious membrane fouling are one of the main reasons that restrict membrane distillation technology to large-scale industrial utilization, the air gap membrane distillation is used as a model to study the mass transfer, which the intermediate air gap layer, condensing tube material, condensation surface area, and liquid inlet and outlet pattern are included in. Then, A new type of tubular membrane distillation was proposed and called as membrane contact membrane distillation (M-DCMD). After that, Potassium chloride solution(1 moL·L-1) was concentrated by membrane contact type(M-DCMD), air gap type(AGMD), direct contact type(DCMD) for comparative study theirs concentration process, membrane fouling and membrane wetting. The results show that the membrane flux increased by 59.8% at 65 ℃ by eliminating the air gap layer. stainless steel condenser tube. The membrane flux of stainless steel condenser tube and copper condenser tube increased by 55% and 56% respectively, compared with PVC condenser tube. Therefore, the membrane flux is significantly affected by the material of the condenser tube. When the ratio of condensation surface area to membrane effective working area increased from 1:1.77 to 1:1.24, the flux of membrane distillation increased by 34.3%. When desalting under the same conditions, the comprehensive properties of M-DCMD such as anti-pollution and anti-wetting are significantly better than AGMD and DCMD.

Funds:
北京市自然科学基金(2182085)&国家重点研发计划(2018YFC1900304)

AuthorIntro:
纪仲光(1982—),男,河北遵化人,博士,高级工程师,研究方向:膜及膜分离技术在水处理领域应用, E-mail:jizhongguang@grinm.com

Reference:
 [1] Aamer Ali, Jheng-Han Tsai, Kuo-Lun Tung.etc. Designing and optimization of continuous direct contact membrane distillation process. [J]. Desalination, 2018,426: 97~107.
[2] Wenli Qin, Zongli Xie,Derrick Ng,etc, Comparison of colloidal silica involved fouling behavior in three membrane distillation configurations using PTFE membrane. [J]. Water Res. 2018, 130:343~352.
[3] Haoran Qiu,Yuelian Peng,Lei Ge.etc, Pore channel surface modification for enhancing anti-fouling membrane Distillation. [J]. Appl. Surf. Sci. 2018,443:217~226.
[4] 申龙,高瑞昶,膜蒸馏技术最新研究应用进展. [J]. 化工进展,2013,33(2):289~296.
[5]X. Feng, P. Wu,L.Y. Jiang. Titanium white waste acid concentration by DCMD:Wetting, crystallization and fouling. [J]. Desalination.,2018,312:31~45.
[6]Atia E. Khalifa, Suhaib M. Alawad, Air gap and water gap multistage membrane distillation for water desalination. [J]. Desalination. 2018, 437:175~183.
[7]Navya Thomas, Musthafa O. Mavukkandy,etc. Membrane distillation research & implementation: Lessons from the past five decades. [J]. Sep. Purif. Technol. 2017,189:108~127.
[8]Kunpeng Wang, Deyin Hou, Jun Wang.etc. Hydrophilic surface coating on hydrophobic PTFE membrane for robust anti-oil-fouling membrane distillation. [J]. Appl. Surf. Sci. 2018, 450 :57~65.
[9]Mohammad Rezaei, David M. Warsinger, John H. Lienhard V.etc. Wetting phenomena in membrane distillation: Mechanisms, reversal,and prevention. [J]. Water Res. 2018, 139: 329~352.
[10]Chii-Dong Ho, Luke Chen, Mei-Chih Huang.etc. Distillate flux enhancement in the air gap membrane distillation with inserting carbon-fiber spacers. [J]. Sep. Purif. Technol. 2017, 18:2817~2828.
[11]吕晓龙,武春瑞,高启君,等. 膜蒸馏海水淡化技术探讨. [J]. 水处理技术, 2015, 41(10):26~30
[12] Camacho L, Dumee L. Zhang J, et al. Advances in membrane distillation for water desalination and purification applications. [J]. Water, 2013, 51:94~196.
[13] Gonzalez D,Amigo J, Suarez F. Membrane distillation: perspectives for improved  desalination. [J]. Renew. Sust. Energ. Rev. 2017, 80:238~259.
[14] 田瑞,李嵩,杨晓宏,等.高通量空气隙膜蒸馏系统的实验研究.[J]. 清华大学学报: 自然科学版,2007, 47:2056~2059.

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