Economic analysis of desalination technologies in the context of carbon pricing, and opportunities for membrane distillation

Uchenna K. Kesieme, Nicholas Milne, Hal Aral, Chu Yong Cheng, Mikel Duke

Research output: Contribution to journalArticlepeer-review

140 Citations (Scopus)

Abstract

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.

Original languageEnglish
Pages (from-to)66-74
Number of pages9
JournalDesalination
Volume323
DOIs
Publication statusPublished - 15 Aug 2013
Externally publishedYes

Keywords

  • Carbon tax
  • Desalination
  • Economics and waste heat
  • Membrane distillation
  • Price

Fingerprint

Dive into the research topics of 'Economic analysis of desalination technologies in the context of carbon pricing, and opportunities for membrane distillation'. Together they form a unique fingerprint.

Cite this