Abstract:
:The membrane fouling mechanism was studied in treating succinic acid fermentation broth during dead-end ultrafiltration. Different membranes were used and two models were applied to analyze the fouling mechanism. Resistance-in-series model was applied to determine the main factor that caused the operation resistance. Results indicated that most membranes tended to be fouled by cake layer or concentration polarization. Hermia's model, which is composed of four individual sub-models, was used to analyze the predominant fouling mechanism. Results showed that the fouling of RC 10 kDa and PES 30 kDa was controlled by the complete blocking mechanism, while PES 100 kDa was controlled by the intermediate blocking and PES 10 kDa was controlled by cake layer. This conclusion was also proved by SEM photos. Membrane characteristics were monitored before and after ultrafiltration by AFM and goniometer. Both contact angle and roughness of most membranes increased after ultrafiltration.
journal_name
Bioresour Technoljournal_title
Bioresource technologyauthors
Wang C,Li Q,Tang H,Yan D,Zhou W,Xing J,Wan Ydoi
10.1016/j.biortech.2012.03.099subject
Has Abstractpub_date
2012-07-01 00:00:00pages
366-71eissn
0960-8524issn
1873-2976pii
S0960-8524(12)00563-9journal_volume
116pub_type
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