Experimental study and numerical optimization for removal of methyl orange using polytetrafluoroethylene membranes in vacuum membrane distillation process

被引:38
作者
Yadav, Anshul [1 ,4 ]
Patel, Raj Vardhan [1 ]
Singh, Chandra Prakash [2 ]
Labhasetwar, Pawan Kumar [3 ,4 ]
Shahi, Vinod Kumar [1 ,4 ]
机构
[1] CSIR Cent Salt & Marine Chem Res Inst, Membrane Sci & Separat Technol Div, Bhavnagar 364002, Gujarat, India
[2] Indian Inst Technol Kanpur, Dept Mech Engn, Kanpur 208016, Uttar Pradesh, India
[3] CSIR, Water Technol & Management Div, Natl Environm Engn Res Inst, Nagpur 440020, Maharashtra, India
[4] Acad Sci & Innovat Res AcSIR, Ghaziabad 201002, India
关键词
Vacuum membrane distillation; Response surface methodology; Optimization; PTFE membrane; Computational fluid dynamics; RESPONSE-SURFACE METHODOLOGY; BLUE BLACK DYE; MASS-TRANSFER; DESALINATION; PERFORMANCE; HEAT; OPPORTUNITIES; SIMULATION; SEPARATION;
D O I
10.1016/j.colsurfa.2021.128070
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
One of the most water-intensive and environment polluting anthropogenic industries is the textile industry. Amongst textile dyes, methyl orange (MO) is an extensively used anionic azo dye that is toxic to the environment. In this study, the effect of various process parameters was studied for different operating conditions (mass flow rate, vacuum pressure, inlet feed temperature, dye concentration) to remove MO from synthetic wastewater in the vacuum membrane distillation (VMD) process. We determined the optimum conditions for operating variables using response surface methodology (RSM) and developed a regression model to describe permeate flux, dye rejection and specific energy consumption. The optimum operating parameters from the RSM study were bulk feed temperature: 70 degrees C, mass flowrate: 40 kg h-1, dye concentration: 60 mg l- 1 and vacuum pressure: 720 mm Hg. For the optimized input process parameters, the experimentally observed values were permeate flux: 19.60 +/- 1.03 l m-2 h-1, dye rejection: 99.80 +/- 0.07%, and SEC: 2.04 +/- 0.11 kW h m-3. Furthermore, for these optimized conditions, a 3D CFD model was developed to gain insight into the membrane module's thermal, velocity, and concentration field. The evaporation of feed at the membrane surface on the feed side and condensation of vapours at the membrane surface on the permeate side was captured in this model. The permeate flux profile and dye rejection for various cycles of VMD operation with intermittent washing were also performed to study the fouling behaviour of the membrane. The membrane's surface fouling was analyzed using SEM and FT-IR analysis. The SEM analysis of the fouled membrane indicated that the dye deposition was not severe due to high hydrophobicity, high liquid entry pressure, and high pore wetting resistance of the PTFE membrane. The FT-IR analysis showed that the fouled PTFE membrane sufficiently retained its initial structure and property.
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页数:14
相关论文
共 64 条
[31]   Synergic effects of hydrophilic and hydrophobic nanoparticles on performance of nanocomposite distillation membranes: An experimental and numerical study [J].
Li, Zhelun ;
Rana, Dipak ;
Wang, Zhaohui ;
Matsuura, Takeshi ;
Lan, Christopher Q. .
SEPARATION AND PURIFICATION TECHNOLOGY, 2018, 202 :45-58
[32]   Environmental and Health Impacts of Air Pollution: A Review [J].
Manisalidis, Ioannis ;
Stavropoulou, Elisavet ;
Stavropoulos, Agathangelos ;
Bezirtzoglou, Eugenia .
FRONTIERS IN PUBLIC HEALTH, 2020, 8
[33]   New model for frost growth rate [J].
Na, BC ;
Webb, RL .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2004, 47 (05) :925-936
[34]   Separation of ethylene glycol solution by vacuum membrane distillation (VMD) [J].
Mohammadi, T ;
Akbarabadi, M .
DESALINATION, 2005, 181 (1-3) :35-41
[35]   Optimization of nanocomposite membrane for vacuum membrane distillation (VMD) using static and continuous flow cells: Effect of nanoparticles and film thickness [J].
Murugesan, Viyash ;
Rana, Dipak ;
Matsuura, Takeshi ;
Lan, Christopher Q. .
SEPARATION AND PURIFICATION TECHNOLOGY, 2020, 241
[36]   Effective separation of methylene blue dye from aqueous solutions by integration of micellar enhanced ultrafiltration with vacuum membrane distillation [J].
Parakala, Sowmya ;
Moulik, Siddhartha ;
Sridhar, S. .
CHEMICAL ENGINEERING JOURNAL, 2019, 375
[37]   Heat transport and membrane distillation coefficients in direct contact membrane distillation [J].
Phattaranawik, J ;
Jiraratananon, R ;
Fane, AG .
JOURNAL OF MEMBRANE SCIENCE, 2003, 212 (1-2) :177-193
[38]   A Numerical Simulation of Membrane Distillation Treatment of Mine Drainage by Computational Fluid Dynamics [J].
Qi, Ji ;
Lv, Jiafeng ;
Li, Zhen ;
Bian, Wei ;
Li, Jingfeng ;
Liu, Shuqin .
WATER, 2020, 12 (12)
[39]   Experimental determination of liquid entry pressure (LEP) in vacuum membrane distillation for oily wastewaters [J].
Racz, Gabor ;
Kerker, Steffen ;
Schmitz, Oliver ;
Schnabel, Benjamin ;
Kovacs, Zoltan ;
Vatai, Gyula ;
Ebrahimi, Mehrdad ;
Czermak, Peter .
MEMBRANE AND WATER TREATMENT, 2015, 6 (03) :237-249
[40]  
Rita Kant Rita Kant, 2012, Natural Science, V4, P22