Deacidifying rice bran oil by solvent extraction and membrane technology

Citation
V. Kale et al., Deacidifying rice bran oil by solvent extraction and membrane technology, J AM OIL CH, 76(6), 1999, pp. 723-727
Citations number
12
Categorie Soggetti
Agricultural Chemistry
Journal title
JOURNAL OF THE AMERICAN OIL CHEMISTS SOCIETY
ISSN journal
0003021X → ACNP
Volume
76
Issue
6
Year of publication
1999
Pages
723 - 727
Database
ISI
SICI code
0003-021X(199906)76:6<723:DRBOBS>2.0.ZU;2-M
Abstract
Crude rice bran oil containing 16.5% free fatty acids (FFA) was deacidified by extracting with methanol. At the optimal ratio of 1.8:1 methanol/oil by weight, the concentration of FFA in the crude rice bran oil was reduced to 3.7%. A second extraction at 1:1 ratio reduced FFA in the oil to 0.33%. Th e FFA in the methanol extract was recovered by nanofiltration using commerc ial membranes. The DS-5 membrane from Osmonics/Desal and the BW-30 membrane from Dow/FilmTec gave average FFA rejection of 93-96% and an average flux of 41 L/m(2).h (LMH) to concentrate the FFA from 4.69% to 20%. The permeate , containing 0.4-0.7% FFA, can be nanofiltered again to recover more FFA wi th flux of 67-75 LMH. Design estimates indicate a two-stage membrane system can recover 97.8% of the FFA and can result in a final retentate stream wi th 20% FFA or more and a permeate stream with negligible FFA (0.13%) that c an be recycled for FFA extraction. The capital cost of the membrane plant w ould be about $48/kg oil processed/h and annual operating cost would be abo ut $15/ton FFA recovered. The process has several advantages in that it doe s not require alkali for neutralization, no soapstock nor wastewater is pro duced, and effluent discharges are minimized.