Literature DB >> 20659753

Vacuum membrane distillation of seawater reverse osmosis brines.

Jean-Pierre Mericq1, Stéphanie Laborie, Corinne Cabassud.   

Abstract

Seawater desalination by Reverse Osmosis (RO) is an interesting solution for drinking water production. However, because of limitation by the osmotic pressure, a high recovery factor is not attainable. Consequently, large volumes of brines are discharged into the sea and the flow rate produced (permeate) is limited. In this paper, Vacuum Membrane Distillation (VMD) is considered as a complementary process to RO to further concentrate RO brines and increase the global recovery of the process. VMD is an evaporative technology that uses a membrane to support the liquid-vapour interface and enhance the contact area between liquid and vapour in comparison with conventional distillation. This study focuses on VMD for the treatment of RO brines. Simulations were performed to optimise the operating conditions and were completed by bench-scale experiments using actual RO brines and synthetic solutions up to a salt concentration of 300 g L(-1). Operating conditions such as a highly permeable membrane, high feed temperature, low permeate pressure and a turbulent fluid regime allowed high permeate fluxes to be obtained even for a very high salt concentration (300 g L(-1)). For the membrane studied, temperature and concentration polarisation were shown to have little effect on permeate flux. After 6 to 8 h, no organic fouling or biofouling was observed for RO brines. At high salt concentrations, scaling occurred (mainly due to calcium precipitation) but had only a limited impact on the permeate flux (24% decrease for a permeate specific volume of 43L m(-2) for the highest concentration of salt). Calcium carbonate and calcium sulphate precipitated first due to their low solubility and formed mixed crystal deposits on the membrane surface. These phenomena only occurred on the membrane surface and did not totally cover the pores. The crystals were easily removed simply by washing the membrane with water. A global recovery factor of 89% can be obtained by coupling RO and VMD.
Copyright © 2010 Elsevier Ltd. All rights reserved.

Entities:  

Mesh:

Substances:

Year:  2010        PMID: 20659753     DOI: 10.1016/j.watres.2010.06.052

Source DB:  PubMed          Journal:  Water Res        ISSN: 0043-1354            Impact factor:   11.236


  5 in total

1.  POSS-Functionalized Graphene Oxide/PVDF Electrospun Membranes for Complete Arsenic Removal Using Membrane Distillation.

Authors:  Sebastian Leaper; Edgardo Oscar Avendaño Cáceres; Jose Miguel Luque-Alled; Sarah H Cartmell; Patricia Gorgojo
Journal:  ACS Appl Polym Mater       Date:  2021-03-05

2.  Cane sugar crystallization using submerged vacuum membrane distillation crystallization (SVMDC).

Authors:  Helen Julian; Hafizh Rizqullah; Michael Armando Siahaan; I Gede Wenten
Journal:  J Food Sci Technol       Date:  2020-09-01       Impact factor: 3.117

3.  Evaluation of the Specific Energy Consumption of Sea Water Reverse Osmosis Integrated with Membrane Distillation and Pressure-Retarded Osmosis Processes with Theoretical Models.

Authors:  Shao-Chi Tsai; Wei-Zhi Huang; Geng-Sheng Lin; Zhen Wang; Kuo-Lun Tung; Ching-Jung Chuang
Journal:  Membranes (Basel)       Date:  2022-04-16

4.  A Novel Hybrid Reactor of Pressure-Retarded Osmosis Coupling with Activated Sludge Process for Simultaneously Treating Concentrated Seawater Brine and Wastewater and Recovering Energy.

Authors:  Jiaxin Ding; Qian Zhou; Zixun Zhou; Wenyu Chu; Yao Jiang; Wei Lai; Pin Zhao; Xinhua Wang
Journal:  Membranes (Basel)       Date:  2022-03-31

5.  Enhancement of brackish water desalination using hybrid membrane distillation and reverse osmosis systems.

Authors:  Emad Ali; Jamel Orfi; Abdullah Najib; Jehad Saleh
Journal:  PLoS One       Date:  2018-10-09       Impact factor: 3.240

  5 in total

北京卡尤迪生物科技股份有限公司 © 2022-2023.