Direct osmosis process for power generation using salinity gradient: FO/PRO pilot plant investigation using hollow fiber modules
被引:5
作者:
Mermier, N. R. J-D.
论文数: 0引用数: 0
h-index: 0
机构:
Fed Univ Rio de Janeiro UFRJ, Chem Engn Program COPPE, POB 68502, BR-21941972 Rio De Janeiro, BrazilFed Univ Rio de Janeiro UFRJ, Chem Engn Program COPPE, POB 68502, BR-21941972 Rio De Janeiro, Brazil
Mermier, N. R. J-D.
[1
]
Borges, C. P.
论文数: 0引用数: 0
h-index: 0
机构:
Fed Univ Rio de Janeiro UFRJ, Chem Engn Program COPPE, POB 68502, BR-21941972 Rio De Janeiro, BrazilFed Univ Rio de Janeiro UFRJ, Chem Engn Program COPPE, POB 68502, BR-21941972 Rio De Janeiro, Brazil
Borges, C. P.
[1
]
机构:
[1] Fed Univ Rio de Janeiro UFRJ, Chem Engn Program COPPE, POB 68502, BR-21941972 Rio De Janeiro, Brazil
Hollow fiber membranes;
Osmotic water flux;
Power density;
Permeation modules;
Pressure retarded osmosis;
Renewable energy source;
PRESSURE-RETARDED OSMOSIS;
INTERNAL CONCENTRATION POLARIZATION;
OSMOTIC POWER;
MEMBRANES;
COMPOSITE;
PERFORMANCE;
FABRICATION;
ENERGY;
D O I:
10.1016/j.cep.2015.10.014
中图分类号:
TE [石油、天然气工业];
TK [能源与动力工程];
学科分类号:
0807 ;
0820 ;
摘要:
The phenomenon of osmosis is known for more than 150 years and involves the contact of a semipermeable membrane with solutions of different salinity. The osmotic flux that permeates through the membrane can be used for electric power generation as a renewable source of energy. This process can be accomplished by means of the pressure retarded osmosis (PRO). This work consisted of the construction of a demonstrative FO/PRO power pilot plant. Assymetric polymeric cellulose acetate hollow fiber membranes were produced and conditioned in permeation modules. The pilot plant consists of three countercurrent flow hollow fiber modules connected in parallel. According to the modules and fibers dimensions, the membrane area per module can reach 1.5 m(2) that means a packing density of 1500 m(2) m(-3). The pilot scale enables the activation of a hydroturbine/generator device coupled to a 9-LEDs panel which can establish the technological and scientific bases for further industrial upscaling. A forward osmosis (FO) test using a MgSO4 solution (0.8 M, pi: 22 bar) and an intermittent PRO test using a NaCl solution (0.8 M, pi: 37 bar) were performed, where the maximum osmotic flux values were 33 and 8 L m(-2) h(-1), corresponding to an energy performance of 5 and 2 W m(-2), respectively. These values are comparable with most of the latest bench-scale FO membrane investigations. (C) 2015 Elsevier B.V. All rights reserved.