The Fouling Mechanism of Ceramic Membranes Used for Recovering TS-1 Catalysts
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The Fouling Mechanism of Ceramic Membranes Used for Recovering TS-1 Catalysts
Chinese Journal of Chemical EngineeringVol. 17, Issue 1, Pages: 53-57(2009)
Affiliations:
1. State Key Laboratory of Materials-Oriented Chemical Engineering, College of Chemistry and Chemical Engineering, Nanjing University of Technology,Nanjing,China,210009
2. Chemical Engineering Department, Nanjing College of Chemical Technology,Nanjing,China,210048
ZHONG Zhaoxiang, LI Dongyan, LIU Xin, XING Weihong, XU Nanping. The Fouling Mechanism of Ceramic Membranes Used for Recovering TS-1 Catalysts[J]. , 2009, 17(1): 53-57.
DOI:
ZHONG Zhaoxiang, LI Dongyan, LIU Xin, XING Weihong, XU Nanping. The Fouling Mechanism of Ceramic Membranes Used for Recovering TS-1 Catalysts[J]. , 2009, 17(1): 53-57.DOI: 10.1016/S1004-9541(09)60032-X.
The Fouling Mechanism of Ceramic Membranes Used for Recovering TS-1 Catalysts
Ceramic ultrafiltration membranes were used to separate titanium silicalite-1(TS-1) catalysts from the slurry of catalytic ammoximation of cyclohexanone to oxime.Silica was shown to have a great effect on membrane fouling in the alkaline environment of this system.In the ammoximation system
there are three main silica sources
which are residual silica on the catalyst particles surface during preparation
silica dissolved from TS-1 catalyst particles by ammonia solvent
and silica sol added into the reaction slurry to inhibit the dissolution erosion of the TS-1 catalyst.The silica dissolved by ammonia has been proved to influence membrane fouling most among the three silica sources.This was because the amount of silica dissolved by ammonia was the largest
and the polymerization of silica monomers at high concentration caused colloid particles formation
which led to a dense cake layer depositing on the membrane surface.Meanwhile
the size reduction of catalyst particles caused by alkaline dissolution also increased specific resistances of cake layers.
Abstract
Ceramic ultrafiltration membranes were used to separate titanium silicalite-1(TS-1) catalysts from the slurry of catalytic ammoximation of cyclohexanone to oxime.Silica was shown to have a great effect on membrane fouling in the alkaline environment of this system.In the ammoximation system
there are three main silica sources
which are residual silica on the catalyst particles surface during preparation
silica dissolved from TS-1 catalyst particles by ammonia solvent
and silica sol added into the reaction slurry to inhibit the dissolution erosion of the TS-1 catalyst.The silica dissolved by ammonia has been proved to influence membrane fouling most among the three silica sources.This was because the amount of silica dissolved by ammonia was the largest
and the polymerization of silica monomers at high concentration caused colloid particles formation
which led to a dense cake layer depositing on the membrane surface.Meanwhile
the size reduction of catalyst particles caused by alkaline dissolution also increased specific resistances of cake layers.
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