TY - JOUR
T1 - High temperature direct contact membrane distillation based desalination using PTFE hollow fibers
AU - Singh, Dhananjay
AU - Sirkar, Kamalesh K.
N1 - Funding Information:
We acknowledge funding for this research from MAST (Membrane Science, Engineering & Technology) Center, ConocoPhillips, USA and National Science Foundation, USA (Project No. #9-1). Kay Bjornen and Xiaoyi Gong of ConocoPhillips provided substantial help. We acknowledge Rob German (Markel Corporation) for providing hollow fibers of PTFE.
PY - 2014/9/6
Y1 - 2014/9/6
N2 - Thermally driven direct contact membrane distillation (DCMD)-based desalination process involving a microporous hydrophobic membrane separates a hot brine feed and a cold distillate which condenses the water vapor coming from the hot brine through the gas-filled membrane pores. Conventionally DCMD has been explored for hot brines and other aqueous solutions below 100°C. For feed brines above 100°C, desalination by a conventional membrane technique, such as, reverse osmosis (RO) requires cooling of the feed solution costing additional energy since RO cannot utilize the heat available in the feed solution; DCMD process is ideally suited for such a process. Produced water obtained from steam assisted gravity drainage (SAGD) process is one such example where DCMD can potentially be a very useful process. This process has been explored earlier with flat porous polytetrafluoroethylene (PTFE) membranes. In this paper, desalination by the DCMD technique has been explored in the temperature range of 50-120°C for brine solutions containing 10,000ppm sodium chloride using microporous PTFE hollow fiber membranes. The pressure of the solution went up to 2-3atm. There was no leakage of salt under any conditions. The highest water vapor flux achieved was 115kg/m2h at 118°C, which is close to an order of magnitude higher than that for seawater reverse osmosis (RO) processes. A simulated SAGD produced water was also successfully desalinated.
AB - Thermally driven direct contact membrane distillation (DCMD)-based desalination process involving a microporous hydrophobic membrane separates a hot brine feed and a cold distillate which condenses the water vapor coming from the hot brine through the gas-filled membrane pores. Conventionally DCMD has been explored for hot brines and other aqueous solutions below 100°C. For feed brines above 100°C, desalination by a conventional membrane technique, such as, reverse osmosis (RO) requires cooling of the feed solution costing additional energy since RO cannot utilize the heat available in the feed solution; DCMD process is ideally suited for such a process. Produced water obtained from steam assisted gravity drainage (SAGD) process is one such example where DCMD can potentially be a very useful process. This process has been explored earlier with flat porous polytetrafluoroethylene (PTFE) membranes. In this paper, desalination by the DCMD technique has been explored in the temperature range of 50-120°C for brine solutions containing 10,000ppm sodium chloride using microporous PTFE hollow fiber membranes. The pressure of the solution went up to 2-3atm. There was no leakage of salt under any conditions. The highest water vapor flux achieved was 115kg/m2h at 118°C, which is close to an order of magnitude higher than that for seawater reverse osmosis (RO) processes. A simulated SAGD produced water was also successfully desalinated.
KW - Direct contact membrane distillation
KW - High temperature and pressure
KW - Polytetrafluoroethylene hollow fiber membrane
KW - Produced water
KW - Steam-assisted gravity drainage process
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U2 - 10.1016/j.ces.2014.05.042
DO - 10.1016/j.ces.2014.05.042
M3 - Article
AN - SCOPUS:84903907419
SN - 0009-2509
VL - 116
SP - 824
EP - 833
JO - Chemical Engineering Science
JF - Chemical Engineering Science
ER -