Seawater Desalination for Production of Highly Pure Water Using a Hydrophobic PTFE Membrane and Direct Contact Membrane Distillation (DCMD)

Qatar’s primary source of fresh water is through
seawater desalination. Amongst the major processes that are
commercially available on the market, the most common large scale
techniques are Multi-Stage Flash distillation (MSF), Multi Effect
distillation (MED), and Reverse Osmosis (RO). Although commonly
used, these three processes are highly expensive down to high energy
input requirements and high operating costs allied with maintenance
and stress induced on the systems in harsh alkaline media. Beside that
cost, environmental footprint of these desalination techniques are
significant; from damaging marine eco-system, to huge land use, to
discharge of tons of GHG and huge carbon footprint.
Other less energy consuming techniques based on membrane
separation are being sought to reduce both the carbon footprint and
operating costs is membrane distillation (MD).
Emerged in 1960s, MD is an alternative technology for water
desalination attracting more attention since 1980s. MD process
involves the evaporation of a hot feed, typically below boiling point
of brine at standard conditions, by creating a water vapor pressure
difference across the porous, hydrophobic membrane. Main
advantages of MD compared to other commercially available
technologies (MSF and MED) and specially RO are reduction of
membrane and module stress due to absence of trans-membrane
pressure, less impact of contaminant fouling on distillate due to
transfer of only water vapor, utilization of low grade or waste heat
from oil and gas industries to heat up the feed up to required
temperature difference across the membrane, superior water quality,
and relatively lower capital and operating cost.
To achieve the objective of this study, state of the art flat-sheet
cross-flow DCMD bench scale unit was designed, commissioned, and
tested. The objective of this study is to analyze the characteristics and
morphology of the membrane suitable for DCMD through SEM
imaging and contact angle measurement and to study the water
quality of distillate produced by DCMD bench scale unit.
Comparison with available literature data is undertaken where
appropriate and laboratory data is used to compare a DCMD distillate
quality with that of other desalination techniques and standards.
Membrane SEM analysis showed that the PTFE membrane used
for the study has contact angle of 127º with highly porous surface
supported with less porous and bigger pore size PP membrane. Study
on the effect of feed solution (salinity) and temperature on water
quality of distillate produced from ICP and IC analysis showed that
with any salinity and different feed temperature (up to 70ºC) the
electric conductivity of distillate is less than 5 μS/cm with 99.99%
salt rejection and proved to be feasible and effective process capable
of consistently producing high quality distillate from very high feed
salinity solution (i.e. 100000 mg/L TDS) even with substantial
quality difference compared to other desalination methods such as
RO and MSF.





References:
[1] "Power in the GCC." Kippreport 8 Feb. 2010: 28.
[2] Alhajri, K, and L Almisned. "Water Resources In The GCC Countries: A
Strategic Option." Renewable Energy 5.1-4 (1994): 524-528.
[3] Al. Ansari, Mohammed Saleh . "Concentrating Solar Power to Be Used
in Seawater Desalination within the Gulf Cooperation Council." Energy
and Environment Research 3 (2013): 1-23.
[4] Dawoud, Mohamed A., and Mohamed M. Al Mulla. "Environmental
Impacts of Seawater Desalination: Arabian Gulf Case Study."
International Journal of Environment and Sustainability 1.3 (2012): 22-
37.
[5] Corrado, Sommariva. "Basic Design of Thermal Desalination Process."
Workshop. Global Water Sustainability Center. Qatar Science and
Technology Park, Doha. 6 Dec. 2011. Class lecture.
[6] Al-Darwish, AbdulMonem. "Qatar's Strategy in the Sustainable
Development of Water Resources." COP 18. KAHRAMA. QNCC, Doha.
28 Nov. 2012. Speech.
[7] Adham, Samer, Altaf Hussain, Joel MinierMatar, Raul Dores, and Arnold
Janson. "Application of Membrane Distillation for desalting brines from
thermal desalination plants." Desalination 314 (2013): 101-108.
[8] Lattemann, Sabine, and Thomas Hopner. "Environmental Impact and
impact assessment of seawater desalination." Desalination 220 (2008): 1-
15.
[9] Charcosset, Catherine. "A Review of Membrane Processes and
Renewable Energies for Desalination." Desalination 245.1-3 (2009): 214-
231.
[10] Lawson, K. "Membrane Distillation. I. Module Design and Performance
Evaluation Using Vacuum Membrane Distillation." Journal of Membrane
Science 120 (1996): 111-121.
[11] Martinez, L, and F Floridodiaz. "Theoretical and Experimental Studies on
Desalination Using Membrane Distillation1." Desalination 139.1-3
(2001): 373-379.
[12] J. Phattaranawik and R. Jiraratananon, "Direct contact membrane
distillation: effect of mass transfer on heat transfer”, J. Membrane Sci.
188 (2001), 137-146.
[13] Lawson, K, and D Lloyd. "Membrane Distillation." Journal of Membrane
Science 124 (1997): 1-25.
[14] Elbourawi, M, Z Ding, R Ma, and M Khayet. "A Framework for Better
Understanding Membrane Distillation Separation Process." Journal of
Membrane Science 285.1-2 (2006): 4-29.
[15] Martinez-Diez, F. J. Florido-Diaz, Theoretical and experimental studies
on desalination using membrane distillation, Desalination. 139 (2001)
373-379.
[16] L. Martinez-Diez, F. J. Florido-Diaz, M. I. Vazquez-Gonzalez, Study of
evaporation efficiency in membrane distillation, Desalination. 126 (1999)
193-198.
[17] P.K. Weyl, (1967), "Recovery demineralized water from saline waters”.
United States Patent 3,340,186.
[18] Zeaman, Leos J., Zydney, Andrew L., Microfiltration and Ultrafiltration,
Principles and Applications., New York: Marcel Dekker, Inc, 1996.
[19] Cath, T. "Experimental Study Of Desalination Using Direct Contact
Membrane Distillation: A New Approach To Flux Enhancement."
Journal of Membrane Science 228.1 (2004): 5-16.
[20] Baek, Youngbin ,Junil Kang, Patrick Theato, and Jeyong Yoon.
"Measuring hydrophilicity of RO membranes by contact angles via
sessile drop and captive bubble method: A comparative study."
Desalination 303 (2012): 23–28.
[21] Camacho, Lucy Mar ,LudovicDumée, Jianhua Zhang Zhang, Jun-de Li,
Mikel Duke, Juan Gomez, and Stephen Gray. "Advances in Membrane
Distillation for Water Desalination and Purification Applications." Water
5 (2013): 94-196.
[22] Zhang, Jianhua, Noel Dow, Mikel Duke, Eddy Ostarcevic, Jun-De Li,
and Stephen Gray. "Identification of Material And Physical Features Of
Membrane Distillation Membranes For High Performance Desalination."
Journal of Membrane Science 349.1-2 (2010): 295-303.
[23] J. Zhang, N. Dow, M. Duke, E. Ostarcevic, J.-D. Li, S. Gray,
Identification ofmaterial and physical features of membrane distillation
membranes for high performance desalination, Journal of Membrane
Science. 349(2010): 295-303.
[24] Hwang, Ho Jung, Ke He, Stephen Gray, Jianhua Zhang, and IlShik
Moon. "Direct Contact Membrane Distillation (DCMD): Experimental
Study on The Commercial PTFE Membrane And Modeling." Journal of
Membrane Science 371.1-2 (2011): 90-98.
[25] Zhu, Hailin ,Hongjie Wang, Feng Wang, YuhaiGuo, and Huapeng
Zhang. "Preparation and properties of PTFE hollow fiber membranes for
desalination through vacuum membrane distillation." Journal of
Membrane Science 446 (2013): 145-153
[26] Wenzel, Robert N.. "Resistance of Solid Surfaces To Wetting By Water."
Industrial & Engineering Chemistry 28.8 (1936): 988-994.
[27] Adnan, Sharmiza ,Manh Hoang, and Huanting Wang. "Commercial
PTFE membranes for membrane distillation application: Effect of
microstructure and support material." Desalination 284 (2012): 297–308.