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Simulation of spiral-wound pressure retarded osmosis for harvesting osmotic power: Module-level modeling and implications of feed pre-treatment
被引:2
|作者:
Tagliavini, Matteo
[1
]
Babler, Matthaus U.
[1
]
机构:
[1] KTH Royal Inst Technol, Dept Chem Engn, SE-10044 Stockholm, Sweden
来源:
关键词:
Renewable energy;
Salinity-gradient power;
Pressure retarded osmosis;
Membrane fouling;
Pre-treatment;
THIN-FILM COMPOSITE;
SALINITY-GRADIENT;
CELLULOSE TRIACETATE;
ENERGY-PRODUCTION;
PERFORMANCE;
SEAWATER;
OPTIMIZATION;
GENERATION;
MEMBRANES;
SPACERS;
D O I:
10.1016/j.desal.2023.117184
中图分类号:
TQ [化学工业];
学科分类号:
0817 ;
摘要:
A process-scale model for pressure retarded osmosis (PRO) using a 1-dimensional representation of the spiralwound membrane is presented. Comparing a length-averaged modeling approach with a true counter-current approach reveals that the former holds only for relatively short membrane lengths while it over-predicts the net power output for longer membranes. For a membrane line with eight spiral-wound elements in series, the length-average model over-predicted the PRO performance by 20 %. The model was further used to assess the impact of feed pre-treatment on process performance and optimal process design. Feed pre-treatment was found to be a dominant factor affecting the optimal inlet feed flow rate and the power output. Our model suggests that for a moderate to high feed pre-treatment requirement the inlet feed flow rate is close to minimum feed flow rate of the membrane module. In the absence of feed pre-treatment a power density of 143 and 284 W m- 2 for CTA and TFC membranes, respectively, was found. When feed pre-treatment with 100 Wh m- 3 was employed these numbers dropped to 48 and 94 W m- 2.
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