TY - JOUR
T1 - Economic analysis of desalination technologies in the context of carbon pricing, and opportunities for membrane distillation
AU - Kesieme, Uchenna K.
AU - Milne, Nicholas
AU - Aral, Hal
AU - Cheng, Chu Yong
AU - Duke, Mikel
PY - 2013/8/15
Y1 - 2013/8/15
N2 - The economics of membrane distillation (MD) and common seawater desalination methods including multi effect distillation (MED), multistage flash (MSF) and reverse osmosis (RO) are compared. MD also has the opportunity to enhance RO recovery, demonstrated experimentally on RO concentrate from groundwater. MD concentrated RO brine to 361,000mg/L total dissolved solids, an order of magnitude more saline than typical seawater, validating this potential. On a reference 30,000m3/day plant, MD has similar economics with other thermal desalination techniques, but RO is more cost effective. With the inclusion of a carbon tax of $23 per tonne carbon in Australia, RO remained the economically favourable process. However, when heat comes at a cost equivalent of 10% of the value of the steam needed for MD and MED, under a carbon tax regime, the cost of MD reduces to $0.66/m3 which is cheaper than RO and MED. The favour to MD was due to lower material cost. On low thermally, high electrically efficient installations MD can desalinate water from low temperature (<50°C) heat sources at a cost of $0.57/m3. Our assessment has found that generally, MD opportunities occur when heat is available at low cost, while extended recovery of RO brine is also viable.
AB - The economics of membrane distillation (MD) and common seawater desalination methods including multi effect distillation (MED), multistage flash (MSF) and reverse osmosis (RO) are compared. MD also has the opportunity to enhance RO recovery, demonstrated experimentally on RO concentrate from groundwater. MD concentrated RO brine to 361,000mg/L total dissolved solids, an order of magnitude more saline than typical seawater, validating this potential. On a reference 30,000m3/day plant, MD has similar economics with other thermal desalination techniques, but RO is more cost effective. With the inclusion of a carbon tax of $23 per tonne carbon in Australia, RO remained the economically favourable process. However, when heat comes at a cost equivalent of 10% of the value of the steam needed for MD and MED, under a carbon tax regime, the cost of MD reduces to $0.66/m3 which is cheaper than RO and MED. The favour to MD was due to lower material cost. On low thermally, high electrically efficient installations MD can desalinate water from low temperature (<50°C) heat sources at a cost of $0.57/m3. Our assessment has found that generally, MD opportunities occur when heat is available at low cost, while extended recovery of RO brine is also viable.
KW - Carbon tax
KW - Desalination
KW - Economics and waste heat
KW - Membrane distillation
KW - Price
UR - http://www.scopus.com/inward/record.url?scp=84880326591&partnerID=8YFLogxK
U2 - 10.1016/j.desal.2013.03.033
DO - 10.1016/j.desal.2013.03.033
M3 - Article
AN - SCOPUS:84880326591
SN - 0011-9164
VL - 323
SP - 66
EP - 74
JO - Desalination
JF - Desalination
ER -