Alternative design to dual stage NF seawater desalination using high rejection brackish water membranes

Ali AlTaee, Adel O. Sharif

Research output: Contribution to journalArticle

31 Citations (Scopus)

Abstract

Dual stage NF membrane desalination process was proposed as an alternative approach to RO seawater desalination. Despite of being cheaper than RO desalination, dual stage NF process is not commercially applied yet due to the low overall recovery rate. In an attempt to increase the process recovery rate and to reduce the operation complicity, brackish water RO membrane was used instead of NF in the second stage. ROSA software was used in this study to verify the applicability and cost-effectiveness of the NF-BW dual stage desalination process. Similarly to dual stage NF desalination process, an NF membrane was used in the first stage and BW membrane in the second stage. Permeate from NF membrane was used as a feed into the BW membranes. The effect of membrane type and seawater salinity on the process performance was investigated. For any given recovery rate and seawater salinity, the simulation results showed that the overall cost of NF-NF was slightly lower than the NF-BW process but that was on the cost of higher permeate TDS. For instance, at 43,000mg/l feed salinity the difference in the specific power consumption between NF-NF and NF-BW process was 0.38kWh/m3. The permeate TDS was 125mg/l for NF-BW and 1030mg/l for NF-NF process. The difference in the permeate TDS between NF-NF and NF-BW process increased with increasing the feed salinity. In dual stage NF process, a low permeate was achieved at low recovery rate. For example, at 43,000mg/l feed salinity the permeate TDS from dual stage NF process was 359mg/l when the overall recovery rate was 22%. It was also found that the effect of BW membrane type on the process efficiency was insignificant. Finally, the energy requirements of NF-NF and NF-BW were compared to a single stage RO desalination process. The specific power consumption at 43,000mg/l feed salinity was 4.58kWh/m3, 4.2kWh/m3 and 3.86kWh/m3 for RO, NF-BW and NF-NF process respectively.

Original languageEnglish
Pages (from-to)391-397
Number of pages7
JournalDesalination
Volume273
Issue number2-3
DOIs
Publication statusPublished - 15 Jun 2011
Externally publishedYes

Fingerprint

Desalination
brackish water
Seawater
desalination
membrane
seawater
Membranes
salinity
Water
Recovery
Electric power utilization
cost
Saline Waters
Cost effectiveness
Costs
rate
software
tyramine-deoxysorbitol
simulation
energy

Keywords

  • Brackish water
  • Desalination
  • Dual stage NF
  • Nanofiltration
  • Reverse osmosis
  • Seawater

ASJC Scopus subject areas

  • Chemical Engineering(all)
  • Mechanical Engineering
  • Chemistry(all)
  • Materials Science(all)
  • Water Science and Technology

Cite this

Alternative design to dual stage NF seawater desalination using high rejection brackish water membranes. / AlTaee, Ali; Sharif, Adel O.

In: Desalination, Vol. 273, No. 2-3, 15.06.2011, p. 391-397.

Research output: Contribution to journalArticle

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abstract = "Dual stage NF membrane desalination process was proposed as an alternative approach to RO seawater desalination. Despite of being cheaper than RO desalination, dual stage NF process is not commercially applied yet due to the low overall recovery rate. In an attempt to increase the process recovery rate and to reduce the operation complicity, brackish water RO membrane was used instead of NF in the second stage. ROSA software was used in this study to verify the applicability and cost-effectiveness of the NF-BW dual stage desalination process. Similarly to dual stage NF desalination process, an NF membrane was used in the first stage and BW membrane in the second stage. Permeate from NF membrane was used as a feed into the BW membranes. The effect of membrane type and seawater salinity on the process performance was investigated. For any given recovery rate and seawater salinity, the simulation results showed that the overall cost of NF-NF was slightly lower than the NF-BW process but that was on the cost of higher permeate TDS. For instance, at 43,000mg/l feed salinity the difference in the specific power consumption between NF-NF and NF-BW process was 0.38kWh/m3. The permeate TDS was 125mg/l for NF-BW and 1030mg/l for NF-NF process. The difference in the permeate TDS between NF-NF and NF-BW process increased with increasing the feed salinity. In dual stage NF process, a low permeate was achieved at low recovery rate. For example, at 43,000mg/l feed salinity the permeate TDS from dual stage NF process was 359mg/l when the overall recovery rate was 22{\%}. It was also found that the effect of BW membrane type on the process efficiency was insignificant. Finally, the energy requirements of NF-NF and NF-BW were compared to a single stage RO desalination process. The specific power consumption at 43,000mg/l feed salinity was 4.58kWh/m3, 4.2kWh/m3 and 3.86kWh/m3 for RO, NF-BW and NF-NF process respectively.",
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