p. 1−7
2423-7841
Vol.43/No.1
p. 9−17
2423-7841
Vol.43/No.1
p. 19−28
2423-7841
Vol.43/No.1
p. 29−35
2423-7841
Vol.43/No.1
p. 37−45
2423-7841
Vol.43/No.1
89.3% of colorant components. The sodium chloride rejection increased with increase in the pressure, whereas it decreased through an increase in temperature. The average sodium chloride rejection was found to be 9%. According to the obtained result, the average permeate flux increased with increase in temperature and pressure. The results indicated that the membrane fouling was low (13%) with membrane fouling increasing with increase in temperature from 30°C to 40°C, however it was lowered with a further increase up to 50°C. The benefits obtained from using this membrane are the exclusion of membrane fouling by being rinsed with pure water. Furthermore, using the NF process, the volume of effluent was lowered by 90%.]]>
p. 55−64
2423-7841
Vol.43/No.1
p. 55−64
2423-7841
Vol.43/No.1
p. 65−72
2423-7841
Vol.43/No.1
p. 73−83
2423-7841
Vol.43/No.1
p. 85−91
2423-7841
Vol.43/No.1
p. 93−103
2423-7841
Vol.43/No.1