TY - JOUR
T1 - Separation of sulfoether compounds in garlic oil by integrated membrane technologies
AU - Xiao, Huan
AU - Zhong, Zhaoxiang
AU - Low, Ze-Xian
AU - Huang, Yao
AU - Sun, Yun
AU - Yao, Zhong
PY - 2016/12
Y1 - 2016/12
N2 - This study investigated an integrated process to separate sulfoether compounds from garlic oil. The garlic oil was pretreated by vapor distillation and the oil–water mixture was treated with the combination of ceramic membrane microfiltration (MF) and poly(dimethylsiloxane)/poly(vinylidene fluoride) composite membrane pervaporation (PV). The optimum operating conditions with respect to sulfoether compounds' recovery were determined to be 1.8% feed concentration, 30C and 0.10 MPa for ceramic membrane MF; and 40C, 5 h, 0.24 MPa and 0.32 L/min for PV. It was found that the emulsified oil was effectively separated by ceramic MF membranes, and the rejection rates of diallyl sulfide (DAS), diallyl disulfide (DADS) and diallyl trisulfide (DATS) were 91.11, 99.8 and 100%, respectively. In the subsequent process, PV membrane was used to recover the dissolved oil. PV membrane had a good enrichment effect on DAS and DADS in the penetrant permeate fluid, with separation factors of 6.31 and 5.45, respectively. Compared with oil–water mixture by vapor distillation, the yield of garlic oil is 99.6%. This study showed that MF and PV processes were attractive technologies for the recovery of garlic sulfoether compounds as they yield good separation and operate under mild conditions.
AB - This study investigated an integrated process to separate sulfoether compounds from garlic oil. The garlic oil was pretreated by vapor distillation and the oil–water mixture was treated with the combination of ceramic membrane microfiltration (MF) and poly(dimethylsiloxane)/poly(vinylidene fluoride) composite membrane pervaporation (PV). The optimum operating conditions with respect to sulfoether compounds' recovery were determined to be 1.8% feed concentration, 30C and 0.10 MPa for ceramic membrane MF; and 40C, 5 h, 0.24 MPa and 0.32 L/min for PV. It was found that the emulsified oil was effectively separated by ceramic MF membranes, and the rejection rates of diallyl sulfide (DAS), diallyl disulfide (DADS) and diallyl trisulfide (DATS) were 91.11, 99.8 and 100%, respectively. In the subsequent process, PV membrane was used to recover the dissolved oil. PV membrane had a good enrichment effect on DAS and DADS in the penetrant permeate fluid, with separation factors of 6.31 and 5.45, respectively. Compared with oil–water mixture by vapor distillation, the yield of garlic oil is 99.6%. This study showed that MF and PV processes were attractive technologies for the recovery of garlic sulfoether compounds as they yield good separation and operate under mild conditions.
UR - http://dx.doi.org/10.1111/jfpe.12252
U2 - 10.1111/jfpe.12252
DO - 10.1111/jfpe.12252
M3 - Article
SN - 0145-8876
VL - 39
SP - 591
EP - 600
JO - Journal of Food Process Engineering
JF - Journal of Food Process Engineering
IS - 6
ER -