ORIGINAL_ARTICLE
Progress on Membrane Distillation and Related Technologies
https://www.msrjournal.com/article_21945_729ad23d52146d8c323bc087f0c5d6f3.pdf
2016-10-01
161
162
10.22079/jmsr.2016.21945
Membrane Distillation (MD)
Mohamed
Khayet
khayetm@fis.ucm.es
1
Department of Applied Physics I, Faculty of Physics, University Complutense of Madrid, Avda. Complutense s/n 28040 Madrid, Spain
LEAD_AUTHOR
Carmen
García Payo
mcgpayo@fis.ucm.es
2
Department of Applied Physics I, Faculty of Physics, University Complutense of Madrid, Avda. Complutense s/n 28040 Madrid, Spain
AUTHOR
ORIGINAL_ARTICLE
Performance of Chemically Modified TiO2-poly (vinylidene fluoride) DCMD for Nutrient Isolation and Its Antifouling Properties
The surface properties of TiO2-PVDF nanocomposite membranes were investigated by incorporating different chemically modified TiO2 nanoparticles into the poly (vinylidene fluoride) (PVDF) matrix. The nanocomposite membranes were prepared via dual coagulation bath diffusion and the induced phase inversion method. The membrane surface morphologies were investigated by using SEM and AFM and related to the membrane surface energy via contact angle goniometry. The results showed that the average membrane surface pore sizes were increased with the addition of TiO2 nanoparticles. Nonetheless, the contact angle measurements demonstrated that the hydrophobicity of nanocomposite membranes can be maintained even with the addition of hydrophilic TiO2. This observation could be rationalized as surface roughness enhancement. The experimental results demonstrated that the initial flux of acid treated TiO2 has both higher initial flux and high COD removal due to their induced surface roughness. The TiO2-PVDF membranes were found to possess the significant bactericidal effect on B. Subtilis compared to the neat membrane even without the presence of UV light.
https://www.msrjournal.com/article_21946_55dc75a2db906bd2c20154362ff64263.pdf
2016-10-01
163
168
10.22079/jmsr.2016.21946
Membrane Distillation (MD)
DCMD
Nanocomposite
Chemical modification
Biofouling
N.S.
Mohd Yatim
1
School of Chemical Engineering, Engineering campus, Universiti Sains Malaysia, Seri Ampangan, 14300 Nibong Tebal, Penang, Malaysia
AUTHOR
K.
Abd. Karim
2
School of Chemical Engineering, Engineering campus, Universiti Sains Malaysia, Seri Ampangan, 14300 Nibong Tebal, Penang, Malaysia
AUTHOR
O.
Boon Seng
chobs@usm.my
3
School of Chemical Engineering, Engineering campus, Universiti Sains Malaysia, Seri Ampangan, 14300 Nibong Tebal, Penang, Malaysia
LEAD_AUTHOR
ORIGINAL_ARTICLE
Application of Salt Additives and Response Surface Methodology for Optimization of PVDF Hollow Fiber Membrane in DCMD and AGMD Processes
In this study, the influence of the salts as an additive on the performance of the membrane was investigated and an extensive work was performed to optimize PVDF hollow fiber membranes through a response surface methodology (RSM). The prepared membranes were characterized by SEM, contact angle and LEP measurement. Then, the RSM was used for the optimization of surface pore size, porosity and hydrophobicity of the synthesized hollow fiber at different conditions (polymer concentration, salt concentrations, and air gap). Under MD conditions (feed concentration, 100 mg/l; feed temperature 80 °C, and cooling temperature 15 °C), the optimum membrane was compared with the virgin one in the same condition. In addition, the influence of distillate flux at different feed concentrations and temperatures was evaluated. The results show that the optimum hollow fiber membrane was fabricated in the polymer concentration of 22 %w/w, BaCl2 concentration of 2.9 %w/w and an air gap of 34.5 cm. Consequently, the optimum fiber was examined for the desalination of water with 35, 50 and 70 g/l salt concentration by DC and AG membrane distillation. Our findings show that the distillate flux with the salt rejection of 99.9% was increased to 46% and 31% for DCMD and AGMD, respectively.
https://www.msrjournal.com/article_21947_5852a20c10441e839dc680d8349f8c10.pdf
2016-10-01
169
178
10.22079/jmsr.2016.21947
Desalination
Membrane Distillation (MD)
Hollow Fiber
Salt additive
Box-Behnken Design
Tohid
Vazirnejad
tohid_vaziri@yahoo.com
1
Department of Chemical Engineering, University of Tehran, Tehran, Iran
AUTHOR
Javad
Karimi-Sabet
j_karimi@alum.sharif.edu
2
NFCRS, Nuclear Science and Technology Research Institute, Tehran, Iran
LEAD_AUTHOR
Abolfazl
Dastbaz
a.dastbaz@ut.ac.ir
3
Department of Chemical Engineering, University of Tehran, Tehran, Iran
AUTHOR
Mohammad Ali
Moosavian
moosavian@ut.ac.ir
4
Department of Chemical Engineering, University of Tehran, Tehran, Iran
AUTHOR
Sohrab Ali
Ghorbanian
ghorban@ut.ac.ir
5
Department of Chemical Engineering, University of Tehran, Tehran, Iran
AUTHOR
ORIGINAL_ARTICLE
On Designing of Membrane Thickness and Thermal Conductivity for Large Scale Membrane Distillation Modules
Membrane distillation has the potential to concentrate solutions to their saturation level, thus offering the possibility to recover valuable salts from the solutions. The process performance and stability, however, is strongly dependent upon the features of membranes applied. In addition, several other parameters, membrane thickness and thermal conductivity significantly affect the process performance. These parameters are of fundamental importance in the selection of optimum module length due to their influence on temperature and flux profiles along the fiber. In the current study, the experimental data from a lab-scale membrane distillation plant has been modeled to analyze the interrelated effect of membrane thickness, thermal conductivity and module length on process performance. It has been observed that flux initially improves by decreasing the membrane thickness followed by a decrease and ultimately negative value. For any given fiber length and thickness, the flux can be greatly improved by decreasing the membrane-conductivity. The length that corresponds to the highest flux and the maximum fiber length ensuring a positive flux have been identified as a function of membrane thickness and thermal conductivity.
https://www.msrjournal.com/article_21948_b3c2e3e3e2cc53619e09466e5f0f5f5f.pdf
2016-10-01
179
185
10.22079/jmsr.2016.21948
Membrane Distillation (MD)
Crystallization
Thickness
Thermal conductivity
Length
Aamer
Ali
a.aamer@itm.cnr.it
1
Institute on Membrane Technology (ITM-CNR), National Research Council, c/o University of Calabria, Cubo 17C, Via Pietro Bucci, 87036 Rende CS, Italy
LEAD_AUTHOR
C.A.
Quist-Jensen
2
University of Calabria - Department of Environmental and Chemical Engineering, Rende, Italy
AUTHOR
F.
Macedonio
3
Institute on Membrane Technology (ITM-CNR), National Research Council, c/o University of Calabria, Cubo 17C, Via Pietro Bucci, 87036 Rende CS, Italy
AUTHOR
Enrico
Drioli
e.drioli@itm.cnr.it
4
Hanyang University, WCU Energy Engineering Department, Seoul 133-791, S. Korea
AUTHOR
ORIGINAL_ARTICLE
Nanoparticle Separation Using Direct Contact Membrane Distillation and Its Fouling Study
Direct contact membrane distillation (DCMD) which emerges as an alternative separation technology can effectively perform a colloidal separation process under thermal driven force. DCMD is capable of extracting pure water from aqueous solutions containing non-volatile nanoparticles through the hydrophobic microporous membrane when a vapour pressure difference was established across the membrane. This work aims to study the efficiency of the MD process in separating TiO2 nanoparticles. It was interesting to find out that below 1.0 g/L TiO2 concentration, no sign of flux reduction was noticed. It is indicated that the pore blocking phenomenon was not significant. However, as concentration exceeding 1.0 g/L, the flux started to decline due to the resistance of the gelation layer which impeded water from flowing through the membrane. The blocking law analysis showed that the cake layer was developed within 3 hours of operation. At higher feed velocity, the flux declination problem could be solved due to the surface scouring effect.
https://www.msrjournal.com/article_21949_9ed5c5d065e4c3744430e0807016c2e3.pdf
2016-10-01
186
192
10.22079/jmsr.2016.21949
Direct contact membrane distillation
DCMD
Nanoparticles separation
flux
Rejection
H.Y.
Wong
1
School of Chemical Engineering, Engineering Campus, Universiti Sains Malaysia, Seri Ampangan, 14300 Seberang Prai Selatan, Pulau Pinang, Malaysia
AUTHOR
K.K.
Lau
2
Department of Chemical Engineering, Faculty of Engineering, Universiti Teknologi Petronas, Bandar Seri Iskandar, 31750, Tronoh, Perak Darul Ridzuan, Malayisa
AUTHOR
Enrico
Drioli
e.drioli@itm.cnr.it
3
National Research Council, Institute on Membrane Technology (ITM-CNR) c/o University of Calabria - Cubo 17C, 87036 Rende CS, Italy
AUTHOR
O.B.
Seng
chobs@usm.my
4
School of Chemical Engineering, Engineering Campus, Universiti Sains Malaysia, Seri Ampangan, 14300 Seberang Prai Selatan, Pulau Pinang, Malaysia
LEAD_AUTHOR
ORIGINAL_ARTICLE
The Application of Membrane Distillation for Broth Separation in Membrane Bioreactors
The possibility of applying membrane distillation to support the fermentation process was investigated. The capillary polypropylene membranes were assembled in the membrane modules. The studies were carried out using the standard solutions containing the compounds frequently occurring in the broths such as ethanol, citric, acetic and lactic acids, glycerol and 1,3-propanediol. The performance of membrane bioreactor, in which glycerol was fermented by the use of Citrobacter freundii bacteria was also examined. The separation of particular components of broths was investigated in a long-term application of membrane distillation and a good resistance to wetting of the used polypropylene membrane was demonstrated during the two year period.
https://www.msrjournal.com/article_21950_730038658eb33cd720d8fcc99dba626f.pdf
2016-10-01
193
200
10.22079/jmsr.2016.21950
Membrane Distillation (MD)
Bioreactor
Fermentation
Glycerol
Biofouling
Marek
Gryta
marek.gryta@zut.edu.pl
1
West Pomeranian University of Technology, Szczecin Faculty of Chemical Technology and Engineering ul. Pułaskiego 10, 70-322 Szczecin, Poland
LEAD_AUTHOR
ORIGINAL_ARTICLE
Concentration of Colourful Wild Berry Fruit Juices by Membrane Osmotic Distillation via Cascade Model Systems
Fresh juices of colourful wild berries: cornelian cherry, blackthorn, white beam and elderberry are considered as valuable, highly nutritive beverages and characterized by the high level of vitamins and antioxidant capacity. The concentration process of these juices by membrane osmotic distillation was studied, where only water vapour is eliminated, while the heat sensitive, valuable compounds can be preserved. To shorten the length of the concentration period, cascade model systems with 2, 3 and 4 stages were examined, using model sucrose solutions and real fruit juices. 60 °Brix of juice concentration was possible to reach, with a flux of 0.3-2.4 L m-2 h-1. Furthermore, as a result of cascade system experiments, the length of the separation could be shortened, significantly.
https://www.msrjournal.com/article_21951_fc28cdff5899e8bc2213c6a479f5e2ff.pdf
2016-10-01
201
206
10.22079/jmsr.2016.21951
Membrane osmotic distillation (MOD)
Cascade system
Hollow fibre membrane
Cornelian cherry
Blackthorn
White beam
A.
Boór
boora@almos.uni-pannon.hu
1
Research Institute on Bioengineering, Membrane Technology and Energetics, University of Pannonia, Egyetem str. 10, 8200 Veszprém, HUNGARY
LEAD_AUTHOR
K.
Bélafi-Bakó
2
Research Institute on Bioengineering, Membrane Technology and Energetics, University of Pannonia, Egyetem str. 10, 8200 Veszprém, HUNGARY
AUTHOR
N.
Nemestóthy
3
Research Institute on Bioengineering, Membrane Technology and Energetics, University of Pannonia, Egyetem str. 10, 8200 Veszprém, HUNGARY
AUTHOR
ORIGINAL_ARTICLE
Preliminary Evaluation for Vacuum Membrane Distillation (VMD) Energy Requirement
The energy requirement of vacuum membrane distillation (VMD) with or without recirculation was modelled using both experimental results and theoretical data. The trends are generally consistent between the theoretical and experimental data. Thermal energy contributes the most to the total energy required for the VMD process. To lower the thermal energy cost, waste heat resource and heat recovery of latent heat from the permeate vapour are needed. The electrical energy consumption for VMD is slightly higher than brackish water reverse osmosis (RO) but lower than sea water RO. It is generally more energy efficient to operate the VMD in recirculation mode than single pass mode. Process engineering modelling results indicate that VMD may not be able to compete with RO directly but could be used as a complimentary process to RO, such as for brine concentrate treatment.
https://www.msrjournal.com/article_21952_a4db32548fc4e88cfee63655565ed888.pdf
2016-10-01
207
213
10.22079/jmsr.2016.21952
membrane distillation
VMD
energy
Zongli
Xie
zongli.xie@csiro.au
1
CSIRO Manufacturing, Private bag 33, Clayton South MDC, Victoria 3169, Australia
LEAD_AUTHOR
Derrick
Ng
derrick.ng@csiro.au
2
CSIRO Manufacturing, Private bag 33, Clayton South MDC, Victoria 3169, Australia
AUTHOR
Manh
Hoang
manh.hoang@csiro.au
3
CSIRO Manufacturing, Private bag 33, Clayton South MDC, Victoria 3169, Australia
AUTHOR
Sharmiza
Adnan
sharmiza.adnan@csiro.au
4
CSIRO Manufacturing, Private bag 33, Clayton South MDC, Victoria 3169, Australia
AUTHOR
Jianhua
Zhang
jianhua.zhang@vu.edu.au
5
Institute of Sustainability and Innovation, College of Engineering and Science, Victoria University, PO Box 14428, Melbourne, Victoria 8001, Australia
AUTHOR
Mikel
Duke
mikel.duke@vu.edu.au
6
Institute of Sustainability and Innovation, College of Engineering and Science, Victoria University, PO Box 14428, Melbourne, Victoria 8001, Australia
AUTHOR
Jun-De
Li
jun-de.li@vu.edu.au
7
Institute of Sustainability and Innovation, College of Engineering and Science, Victoria University, PO Box 14428, Melbourne, Victoria 8001, Australia
AUTHOR
Andrew
Groth
andrew.groth@evoqua.com
8
Memcor Products, Evoqua Water Technologies, 15 Blackman Crescent, South Windsor, New South Wales, 2756, Australia
AUTHOR
Chan
Tun
chan.tun@evoqua.com
9
Memcor Products, Evoqua Water Technologies, 15 Blackman Crescent, South Windsor, New South Wales, 2756, Australia
AUTHOR
Stephen
Gray
stephen.gray@vu.edu.au
10
Institute of Sustainability and Innovation, College of Engineering and Science, Victoria University, PO Box 14428, Melbourne, Victoria 8001, Australia
AUTHOR