Improved bubbling for membrane fouling control in filtration of palm oil mill effluent anaerobic digester sludge

被引:12
作者
Annuar, Ariffin Mohamad [1 ]
Nawi, Normi Izati Mat [1 ]
Bilad, Muhammad Roil [1 ]
Jaafar, Juhana [2 ]
Marbelia, Lisendra [3 ]
Nandianto, Asep Bayu Dani [4 ]
机构
[1] Univ Teknol PETRONAS, Chem Engn Dept, Seri Iskandar 32610, Perak, Malaysia
[2] Univ Teknol Malaysia, Fac Engn, Adv Membrane Technol Res Ctr AMTEC, Sch Chem & Energy Engn, Utm Johor Bahru 81310, Johor, Malaysia
[3] Univ Gadjah Mada, Chem Engn Dept, Jl Grafika 2, Yogyakarta 55281, Indonesia
[4] Univ Pendidikan Indonesia, Departemen Kimia, Jl Dr Setiabudhi 229, Bandung 40154, Indonesia
关键词
WASTE-WATER TREATMENT; BIOGAS PRODUCTION; TILTED PANEL; PERFORMANCE; SYSTEM; BIOREACTORS; ULTRAFILTRATION; PRESSURE; AERATION; CFD;
D O I
10.1016/j.jwpe.2020.101350
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Application of anaerobic membrane bioreactor is strictly limited by the membrane fouling because of the fouling prone nature of the feed. This study evaluates a method to enhance the effectiveness of a bubbling system for fouling control in filtration of anaerobic digestion sludge treating palm oil mill effluent using a tilted panel system. Such system is expected to enhance the role of biogas recirculation as the bubbling fluid for membrane fouling control. Effect of tilting angle, bubbling rate, intermittent bubbling period, and panel switching period was investigated. The energy consumption for applying such system was also estimated. Results show that the tilted panel with bubbling remarkably enhance permeability by more than double of the vertical system to reach a maximum value of 87 Lm−2h−1bar−1, the highest value reported so far. The panel switching mechanism helps to enhance the system throughput by allowing two-sided membrane panel with intermittently bubbling, in the expense of mechanical switching energy. The estimation of energy consumption of the system has been estimated at 0.247 kWhm−3, corresponding to 0.3 % of total electricity generated from anaerobic treatment of POME, very attractive for full-scale implementation. © 2020 Elsevier Ltd
引用
收藏
页数:9
相关论文
共 53 条
[1]   Development of a membrane anaerobic system (MAS) for palm oil mill effluent (POME) treatment [J].
Abdurahman, N. H. ;
Rosli, Y. M. ;
Azhari, N. H. .
DESALINATION, 2011, 266 (1-3) :208-212
[2]   Membrane treatment for palm oil mill effluent: effect of transmembrane pressure and crossflow velocity [J].
Ahmad, AL ;
Ismail, S ;
Bhatia, S .
DESALINATION, 2005, 179 (1-3) :245-255
[3]  
Ahmad AL, 2003, DESALINATION, V157, P87
[4]  
Amin M. M., 2015, ECOL ENV CONSERV, V21, P7
[5]   Effect of solids retention time on membrane fouling intensity in two-stage submerged anaerobic membrane bioreactors treating palm oil mill effluent [J].
Annop, S. ;
Sridang, P. ;
Puetpaiboon, U. ;
Grasmick, A. .
ENVIRONMENTAL TECHNOLOGY, 2014, 35 (20) :2634-2642
[6]  
[Anonymous], 2004, J TEKNOL, DOI DOI 10.11113/JT.V41.714
[7]   Effect of biogas sparging with different membrane modules on membrane fouling in anaerobic submerged membrane bioreactor (AnSMBR) [J].
Aslan, Mustafa ;
Saatci, Yusuf ;
Hanay, Ozge ;
Hasar, Halil .
ENVIRONMENTAL SCIENCE AND POLLUTION RESEARCH, 2014, 21 (05) :3285-3293
[8]   Harvesting microalgal biomass using a magnetically induced membrane vibration (MMV) system: Filtration performance and energy consumption [J].
Bilad, M. R. ;
Discart, V. ;
Vandamme, D. ;
Foubert, I. ;
Muylaert, K. ;
Vankelecom, Ivo F. J. .
BIORESOURCE TECHNOLOGY, 2013, 138 :329-338
[9]   Shrinkage, defect and membrane distillation performance of composite PVDF membranes [J].
Bilad, Muhammad R. ;
Guillen-Burrieza, Elena ;
Mavukkandy, Musthafa O. ;
Al Marzooqi, Faisal A. ;
Arafat, Hassan A. .
DESALINATION, 2015, 376 :62-72
[10]   Wastewater treatment in a submerged anaerobic membrane bioreactor [J].
Casu, Stefania ;
Crispino, Nedda A. ;
Farina, Roberto ;
Mattioli, Davide ;
Ferraris, Marco ;
Spagni, Alessandro .
JOURNAL OF ENVIRONMENTAL SCIENCE AND HEALTH PART A-TOXIC/HAZARDOUS SUBSTANCES & ENVIRONMENTAL ENGINEERING, 2012, 47 (02) :204-209