TY - JOUR
T1 - Novel cylindrical cross-flow hollow fiber membrane module for direct contact membrane distillation-based desalination
AU - Singh, Dhananjay
AU - Li, Lin
AU - Obusckovic, Gordana
AU - Chau, John
AU - Sirkar, Kamalesh K.
N1 - Publisher Copyright:
© 2017 Elsevier B.V.
PY - 2018
Y1 - 2018
N2 - Direct contact membrane distillation-based desalination is attractive especially for high salt concentrations. We recently developed successfully a hollow-fiber membrane (HFM) based rectangular module with hot brine in cross-flow over the HFMs and obtained high and stable water flux under demanding scaling conditions. This module design with a low surface area/device volume is inadequate for larger-scale plants. A novel cylindrical cross-flow module containing high-flux composite hydrophobic HFMs is described for membrane surface areas, 0.15 and 0.6 m2, using porous fluorosiloxane-coated porous polypropylene hollow fibers. This simple and easily-scalable module design packs four times membrane surface area/unit equipment volume compared to earlier design. Distilled water production rates from 1 wt% saline feed was studied over brine temperatures of 60–91 °C. A model developed to describe the observed water production rates in dead-end feed introduction configuration appears to describe observed water production rates well. Model predictions were explored for a range of HFM lengths and larger HFM ID to compare with those from rectangular modules with shorter HFMs.
AB - Direct contact membrane distillation-based desalination is attractive especially for high salt concentrations. We recently developed successfully a hollow-fiber membrane (HFM) based rectangular module with hot brine in cross-flow over the HFMs and obtained high and stable water flux under demanding scaling conditions. This module design with a low surface area/device volume is inadequate for larger-scale plants. A novel cylindrical cross-flow module containing high-flux composite hydrophobic HFMs is described for membrane surface areas, 0.15 and 0.6 m2, using porous fluorosiloxane-coated porous polypropylene hollow fibers. This simple and easily-scalable module design packs four times membrane surface area/unit equipment volume compared to earlier design. Distilled water production rates from 1 wt% saline feed was studied over brine temperatures of 60–91 °C. A model developed to describe the observed water production rates in dead-end feed introduction configuration appears to describe observed water production rates well. Model predictions were explored for a range of HFM lengths and larger HFM ID to compare with those from rectangular modules with shorter HFMs.
UR - http://www.scopus.com/inward/record.url?scp=85030862240&partnerID=8YFLogxK
UR - http://www.scopus.com/inward/citedby.url?scp=85030862240&partnerID=8YFLogxK
U2 - 10.1016/j.memsci.2017.09.007
DO - 10.1016/j.memsci.2017.09.007
M3 - Article
AN - SCOPUS:85030862240
SN - 0376-7388
VL - 545
SP - 312
EP - 322
JO - Journal of Membrane Science
JF - Journal of Membrane Science
ER -