Effects of membrane properties on water production cost in small scale membrane distillation systems

Desalination ◽  
2012 ◽  
Vol 306 ◽  
pp. 60-71 ◽  
Author(s):  
Mohamed I. Ali ◽  
Edward K. Summers ◽  
Hassan A. Arafat ◽  
John H. Lienhard V
Author(s):  
Danielle Park ◽  
Elnaz Norouzi ◽  
Chanwoo Park

A small-scale Direct Contact Membrane Distillation (DCMD) system was built to investigate its water distillation performance for varying inlet temperatures and flow rates of feed and permeate streams, and salinity. A counterflow configuration between the feed and permeate streams was used to achieve an efficient heat exchange. A two-dimensional Computational Fluid Dynamics (CFD) model was developed and validated using the experimental results. The numerical results were compared with the experiments and found to be in good agreement. From this study, the most desirable conditions for distilled water production were found to be a higher feed water temperature, lower permeate temperature, higher flow rate and less salinity. The feed water temperature had a greater impact on the water production than the permeate water temperature. The numerical simulation showed that the water mass flux was maximum at the inlet of the feed stream where the feed temperature was the highest and rapidly decreased as the feed temperature decreased.


Desalination ◽  
2014 ◽  
Vol 354 ◽  
pp. 53-61 ◽  
Author(s):  
Gayathri Naidu ◽  
Sanghyun Jeong ◽  
Yongjun Choi ◽  
Eunkyung Jang ◽  
Tae-Mun Hwang ◽  
...  

Membranes ◽  
2021 ◽  
Vol 11 (4) ◽  
pp. 252
Author(s):  
Yuki Suga ◽  
Ryousuke Takagi ◽  
Hideto Matsuyama

Membrane distillation (MD) is a technology that can treat feed solutions with higher osmotic pressure, as well as produce high-purity water. However, the water production cost of the MD process is expensive. In this study, to decrease the water production cost, we attempted to evaluate the effect of membrane characteristics on the long-term stability of a vacuum MD (VMD) system. We fabricated four different types of polyvinylidene difluoride hollow fiber membranes, and operated a VMD system with 3.5 wt% NaCl aqueous solution at 65 °C as a feed under 11 kPa of air gap pressure. Consequently, in the proposed VMD system, it is found that the liquid entry pressure (LEP) is the most important factor. When LEP was higher than 0.37 MPa, the pilot-scale module was very stable for long-term operations, and the vapor flux was approximately 19.3 kg/m2·h with a total salt retention factor of over 99.9% during the 300-h operation.


Membranes ◽  
2021 ◽  
Vol 11 (5) ◽  
pp. 304
Author(s):  
Qingxiu Miao ◽  
Yaoling Zhang ◽  
Shuo Cong ◽  
Fei Guo

Membrane distillation (MD) processes need a relatively mild temperature gradient as the driving force for desalination. In the field, it is reasonable to utilize solar energy as the heat source for the feed, and seawater as the infinite cold source for condensation. Solar-driven MD provides a route for the practical application of seawater desalination at a small scale. In this work, we focus on floating MD modules with a solar heating bag as the power source, and perform proof-of-principle experiments on the MD performance under various conditioning parameters, including feed flow rate, feed temperature, salinity, air gap, and sea waves. The results indicate that floating solar-driven MD modules are feasible in terms of permeate flux and salt rejection ratio, and the upward evaporation MD configuration leads to a better performance in terms of permeate flux. The simulation and experiments also show that the natural sea waves disturb the heating bag and the MD module floating on the surface of seawater, and effectively enhance the feed circulation and transport in the system.


Small Methods ◽  
2021 ◽  
pp. 2001200
Author(s):  
Minmin Gao ◽  
Connor Kangnuo Peh ◽  
Fan Lu Meng ◽  
Ghim Wei Ho

2012 ◽  
Vol 217-219 ◽  
pp. 907-913
Author(s):  
Shi Chun Yang ◽  
Xiao Long Lv

The optimal decoloring conditions for glutamate supernatant in orthogonal experiment are: 15g/l bentonite concentration, 2h decoloring time, and 40°C decoloring temperature. VMD technology can concentrate glutamate supernatant filtrate from 2.01% to 5.35%, and bring down flux from 6.71 L/m2h to 1.94L/m2h, at a concentration rate of 1.72 times. The glutamic acid concentration in supernatant fluid is enriched from 2.03% to 5.16%, and flux attenuated from 5.47 L/m2h to 1.91 L/m2h. As glutamic acid concentration in supernatant increases, membrane flux gradually decreases. Analysis of water production in glutamate supernatant membrane distillation and the meteorological chromatograms of glutamic acid filtrate prove that the difference between water-yielding peak time of supernatant fluid and that of the filtrate is less than 0.1 min. The volatile substances during water production are from glutamic acid filtrate and are of the same matter. Therefore, the product water in supernatant fluid membrane distillation can be reused to improve water production efficiency.


2020 ◽  
Vol 3 (1) ◽  
Author(s):  
Katarzyna Janowska ◽  
Vittorio Boffa ◽  
Mads Koustrup Jørgensen ◽  
Cejna Anna Quist-Jensen ◽  
Fabien Hubac ◽  
...  

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