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Supervised by Ministry of Industry and Information Technology of The People's Republic of China Sponsored by Harbin Institute of Technology Editor-in-chief Yu Zhou ISSNISSN 1005-9113 CNCN 23-1378/T

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Related citation:YAO Jie,HE Zhi-ru,LUO An-guo,ZHAO Qi,SHAO Ze-hui,JIA Li,LI Biao-ming.An experimental investigation on phenol wastewater treatment from coal gasification by pervaporation with NaY molecular Sieve filling membrane[J].Journal of Harbin Institute Of Technology(New Series),2012,19(1):121-124.DOI:10.11916/j.issn.1005-9113.2012.01.024.
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An experimental investigation on phenol wastewater treatment from coal gasification by pervaporation with NaY molecular Sieve filling membrane
Author NameAffiliation
YAO Jie School of Municipal and Environmental Engineering,Harbin Institute of Technology,Harbin 150090,China
National Engineering Center of Urban Water Resources,Harbin Institute of Technology,Harbin 150090,China 
HE Zhi-ru National Engineering Center of Urban Water Resources,Harbin Institute of Technology,Harbin 150090,China 
LUO An-guo Dongying Running Water Company,Dongying 257091,China 
ZHAO Qi National Engineering Center of Urban Water Resources,Harbin Institute of Technology,Harbin 150090,China 
SHAO Ze-hui School of Municipal and Environmental Engineering,Harbin Institute of Technology,Harbin 150090,China 
JIA Li School of Municipal and Environmental Engineering,Harbin Institute of Technology,Harbin 150090,China 
LI Biao-ming School of Municipal and Environmental Engineering,Harbin Institute of Technology,Harbin 150090,China 
Abstract:
In the experiment,PDMS membrane with NaY molecular sieve filling were chosen as the experimental objects and the flux of phenol and removal efficiency of phenol as evaluation index,the effect of the system operating temperature,the flow rate,liquid membrane downstream pressure,operation time,and filling proportion of NaY molecular sieve on pervaporation treatment efficiency for wastewater from coal gasification were investigated. With the increase of temperature and feed flow rate,pervaporation flux and phenol removal efficiency increases. The decrease of the membrane downstream pressure and elevating NaY molecular sieve filling proportion may result in the increase of flux and then phenol removal efficiency improves. When NaY molecular sieve filling proportion is 45% ,treatment efficiency is the best for coal gasification wastewater containing 1850 mg/L phenol as the flux of phenol was 12948. 23 mg/(h·m2) .
Key words:  coal gasification wastewater  pervaporation  PDMS membrane  NaY molecular sieve filling mem- brane
DOI:10.11916/j.issn.1005-9113.2012.01.024
Clc Number:X703
Fund:

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