Comparison of Pressure-Retarded Osmosis Performance between Pilot-Scale Cellulose Triacetate Hollow-fiber and Polyamide Spiral-Wound Membrane Modules.

Yuriko Kakihana,Masafumi Shibuya,Mitsuru Higa,Yuki Ikebe,Nora Jullok

doi:10.3390/membranes11030177

Yuriko Kakihana, Masafumi Shibuya + Show 3 more

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https://doi.org/10.3390/membranes11030177

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Journal: Membranes	Publication Date: Feb 28, 2021
Citations: 7	License type: CC BY 4.0

Affiliation: Yamaguchi University, Universiti Malaysia Perlis

Abstract

Pressure-retarded osmosis (PRO) has recently received attention because of its ability to generate power via an osmotic pressure gradient between two solutions with different salinities: high- and low-salinity water sources. In this study, PRO performance, using the two pilot-scale PRO membrane modules with different configurations—five-inch cellulose triacetate hollow-fiber membrane module (CTA-HF) and eight-inch polyamide spiral-wound membrane modules (PA-SW)—was evaluated by changing the draw solution (DS) concentration, applied hydrostatic pressure difference, and the flow rates of DS and feed solution (FS), to obtain the optimum operating conditions in PRO configuration. The maximum power density per unit membrane area of PA-SW at 0.6 M NaCl was 1.40 W/m2 and 2.03-fold higher than that of CTA-HF, due to the higher water permeability coefficient of PA-SW. In contrast, the maximum power density per unit volume of CTA-SW at 0.6 M NaCl was 4.67 kW/m3 and 6.87-fold higher than that of PA-SW. The value of CTA-HF increased to 13.61 kW/m3 at 1.2 M NaCl and was 12.0-fold higher than that of PA-SW because of the higher packing density of CTA-HF.

Highlights

Energy demand is increasing globally, in tandem with economic development and population growth
The concentrated brine coming from desalination plants sometimes causes environmental problems [4], owing to its high salinity, it can be used as a valuable energy resource referred to as salinity gradient energy (SGE) [5,6,7,8]
The water permeability (A value) was obtained from the slope of the solid line calculated by fitting the data to Equation (1) and gives 0.65 × 10−12 and 4.6 × 10−12 [m s−1 Pa−1 ] for cellulose triacetate hollow-fiber membrane module (CTA-HF)

Summary

Introduction

Energy demand is increasing globally, in tandem with economic development and population growth. Because the majority of primary energy sources comes from fossil fuels [1], the world is facing crucial challenges in meeting energy-source demands, owing to the decrease in the accessibility of cheap fossil fuels [2]. Water shortages are among society’s most challenging problems, for which seawater reverse-osmosis desalination (SWRO) is a promising solution. The concentrated brine coming from desalination plants sometimes causes environmental problems [4], owing to its high salinity, it can be used as a valuable energy resource referred to as salinity gradient energy (SGE) [5,6,7,8]. SGE is a renewable energy source that is obtained by mixing two salt solutions with different salinities [9,10]. There are two main membranebased technologies that convert SGE into electricity: reverse electrodialysis (RED) [9,11,12]

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