Analysis of petroleum biodesulfurization in an airlift bioreactor using response surface methodology

被引:36
作者
Irani, Zahra Azimzadeh [1 ,2 ]
Mehrnia, Mohammad Reza [1 ]
Yazdian, Fatemeh [3 ]
Soheily, Majid [2 ]
Mohebali, Ghasemali [2 ]
Rasekh, Behnam [2 ]
机构
[1] Univ Tehran, Univ Coll Engn, Sch Chem Engn, Tehran, Iran
[2] Res Inst Petr Ind, Tehran, Iran
[3] Univ Tehran, Fac Disciplinary New Sci & Technol, Dept Life Sci Engn, Tehran, Iran
关键词
Petroleum biodesulfurization; Gordonia alkanivorans RIPI90A; Airlift bioreactor; Volumetric gas liquid mass transfer coefficient; Response Surface Methodology; TRICKLE-BED REACTOR; SULFUR-COMPOUNDS; OXYGEN-TRANSFER; SP STRAIN; DIESEL; DESULFURIZATION; MODEL; BACTERIUM; DESIGN; CELLS;
D O I
10.1016/j.biortech.2011.08.120
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
For the first time, growing cells of Gordonia alkanivorans RIPI90A were used for biodesulfurization (BDS) of diesel. This process was carried out in an internal airlift bioreactor. BDS parameters (oil/water phase ratio and initial sulfur concentration) were optimized in flasks using response surface methodology. Predicted results were found to be in good agreement with experimental results. Initial sulfur concentration had a remarkable effect on BDS process. Maximum removal of sulfur (21 mg/l) can be achieved at oil/ water phase ratio of 25% (v/v) and initial sulfur concentration of 28 mg/l. Moreover, effect of superficial gas velocity (U-g) and working volume (v) on volumetric gas liquid mass transfer coefficient was studied in an airlift bioreactor for BDS of diesel. The best results were achieved at U-g and v of 2.51/min and 6.61, respectively. Subsequently, BDS of diesel was investigated in an airlift bioreactor under optimized conditions. Sulfur reduction after 30 h was 14 mg/l. (C) 2011 Elsevier Ltd. All rights reserved.
引用
收藏
页码:10585 / 10591
页数:7
相关论文
共 35 条
[1]   Biology of the metabolically diverse genus Gordonia [J].
Arenskötter, M ;
Bröker, D ;
Steinbüchel, A .
APPLIED AND ENVIRONMENTAL MICROBIOLOGY, 2004, 70 (06) :3195-3204
[2]   Biodesulfurization of dibenzothiophene by growing cells of Pseudomonas putida CECT 5279 in biphasic media [J].
Caro, Ainhoa ;
Boltes, Karina ;
Leton, Pedro ;
Garcia-Calvo, Eloy .
CHEMOSPHERE, 2008, 73 (05) :663-669
[3]   Production of a desulfurization biocatalyst by two-stage fermentation and its application for the treatment of model and diesel oils [J].
Chang, JH ;
Kim, YJ ;
Lee, BH ;
Cho, KS ;
Ryu, HW ;
Chang, YK ;
Chang, HN .
BIOTECHNOLOGY PROGRESS, 2001, 17 (05) :876-880
[4]   Trickle-bed reactor model for desulfurization and dearomatization of diesel [J].
Chowdhury, R ;
Pedernera, E ;
Reimert, R .
AICHE JOURNAL, 2002, 48 (01) :126-135
[5]  
Folsom BR, 1999, APPL ENVIRON MICROB, V65, P4967
[6]   Bio-desulfurization of model organo-sulfur compounds and hydrotreated diesel - Experiments and modeling [J].
Guchhait, S ;
Biswas, D ;
Bhattacharya, P ;
Chowdhury, R .
CHEMICAL ENGINEERING JOURNAL, 2005, 112 (1-3) :145-151
[7]  
Guobin S., 2006, Biochem. Eng. J, V27, P305
[8]  
Hasan SH, 2010, BIORESOURCES, V5, P563
[9]   The scale-up of microbial batch and fed-batch fermentation processes [J].
Hewitt, Christopher ;
Nienow, Alvin .
JOURNAL OF BIOTECHNOLOGY, 2007, 131 (02) :S134-S135
[10]   Determination of Growth Kinetic Parameters of a Desulfurizing Bacterium, Gordonia Alkanivorans RIPI90A [J].
Irani, Zahra Azimzadeh ;
Yazdian, Fatemeh ;
Mohebali, Ghasemali ;
Soheili, Majid ;
Mehrnia, Mohammad Reza .
ICHEAP-10: 10TH INTERNATIONAL CONFERENCE ON CHEMICAL AND PROCESS ENGINEERING, PTS 1-3, 2011, 24 :937-+