EFFECT OF OPERATING PARAMETERS ON THE SEPARATION OF SUGARS BY NANOFILTRATION

Citation
N. Aydogan et al., EFFECT OF OPERATING PARAMETERS ON THE SEPARATION OF SUGARS BY NANOFILTRATION, Separation science and technology, 33(12), 1998, pp. 1767-1785
Citations number
15
Categorie Soggetti
Engineering, Chemical",Chemistry
ISSN journal
01496395
Volume
33
Issue
12
Year of publication
1998
Pages
1767 - 1785
Database
ISI
SICI code
0149-6395(1998)33:12<1767:EOOPOT>2.0.ZU;2-9
Abstract
Due to the complexity of fermentation mixtures, separation of solutes and secondary substrates has a special importance. Membrane processes such as nanofiltration may offer good alternatives for the separation of fermentation products or recovery of substrates. For an efficient s eparation, the membrane type and operating parameters such as feed flo w rate, operating pressure, and feed should be optimized. In this stud y the separation and recovery of sugars were targeted. It was found th at with an increase of the feed flow rate, permeate flux increased sin ce the effect of concentration polarization was minimized. As a result , experiments were carried out at the highest possible flow rate. The effect of pressure was studied at five pressures (10-50 bar). It was f ound that there is a linear relationship between the pressure and perm eate flux up to 30 bars. Beyond 30 bars the effect of pressure became less significant. Thus, 30 bars was chosen as the operating pressure. To investigate the effect of concentration, 1 to 10 weight percentage sucrose and glucose solutions were utilized. It was observed that with an increase in concentration, permeate flux decreased and rejections increased, finally reaching a limiting value. Binary solutions of sucr ose and glucose were also studied. It was seen that the separation fac tor slightly decreased, probably due to a glucose-sucrose interaction. Experimental data were used with a mathematical model to predict the permeate flux and rejection. Good agreement of the predicted results w as obtained with the experimental data for a 500 MWCO membrane.