TY  - JOUR
T1  - Anaerobik biyofilm proseslerde organik yüklemeye bağlı mikrobiyal büyüme ve gelişim
TT  - Microbial growth depending on organic loading rate at the anaerobic biofilm processes
AU  - Gülşen, Hakki
PY  - 2016
DA  - March
JF  - Dicle Üniversitesi Fen Bilimleri Enstitüsü Dergisi
JO  - DUFED
PB  - Dicle University
WT  - DergiPark
SN  - 2146-4693
SP  - 41
EP  - 46
VL  - 5
IS  - 1
LA  - tr
AB  - Bu çalışmada, İstanbul Avrupa yakası, Kemerburgaz  Odayeri  katı atık düzenli depolama alanı  sızıntı sularının anaerobik akışkan yataklı reaktörde  AAYR  arıtılmasında organik yüklemeye bağlı  biyofilm oluşumu ve gelişimi araştırılmıştır. Bu amaçla laboratuvar ölçekli bir anaerobik akışkan  yataklı reaktör kurulmuştur. Çalışmanın yapıldığı akışkan yataklı reaktörün çapı 10 cm, yüksekliği  165 cm, etkili hacmi 13 litre olup yatak malzemesi olarak 0,5 mm’ lik filtre kumu kullanılmış ve sabit  yatak yüksekliği 70 cm’ dir. Yapılan çalışmada AAYR, organik yükleme  OLR  4–37 kgKOİ/m3.gün  aralığında ve hidrolik bekletme süresi 1 gün olarak işletilmiştir. Orijinal hacimsel organik yükleme 20  kg KOİ/m3.gün iken yapılan biyofilm çalışmalarında tutunmuş biyokütle konsantrasyonu ortalama  21,25kg/m3 ve biyokütleye dönüşüm oranı  Y  0,57 gUAKMtut/gKOİgid.gün olarak bulunmuştur
KW  - Anaerobik akışkan yataklı reaktör
KW  - Organik yükleme
KW  - Biyofilm
KW  - Dönüşüm oranı
N2  - In this study, microbial growth depending on organic loading rate and treatability of leachate from Odayeri Sanitary Landfill located on the European part of Istanbul was investigated in an anaerobic fluidized bed reactor  AFBR . The experiments have been performed in a pilot-scale fluidized bed reactor having an inner diameter of 10 cm, a height of 165 cm and an effective volume of 13 l. The reactor media was typical filter sand having an arithmetic mean diameter of 0.5 mm and a fixed bed height of 70 cm. The AFBR experiments were carried out by increasing the organic loading rate  OLR  from 2 to 37 kg COD/m3.day at the hydraulic retention time  HRT  1 day. The mean attached biomass concentration also increased up to 21,25kgAVSS/m3 for the original landfill leachate  OLR=20 kgCOD/m3.day  and the biomass transformation rate  Y  is 0,57 gVSSatt/gCODrem.day
CR  - Hjelmar, O., Johanessen, J.M., Knox, K., Ehrig, H.J., Flyvberg, J., Winther. P. Christensen, T.H., 1995. Composition and Managementof Leachate from Landfills within the EU. In Proc. 5th International Landfill Symposium, Sardinia 95, Italy, 1, 243-262
CR  - CH2M Hill İnternational Ltd., Antel Arıtma A.Ş., 1992. Municipal of Greater Istanbul Waste Management Study, İstanbul Anakenti Katı Atık Yönetimi Etüdü, İstanbul.
CR  - Fadel, M., Bou-Zeid, E., Chahine, W., Alaylı, B., 2002. Temporal Variation of Leachate Quality from Pre-Sorted and Baled Municipal Solid Waste with High Organic and Moisture Content, Waste Management, 22, 269-282
CR  - Öztürk, İ., Altınbaş, M., Arıkan, O., Tüylüoğlu, B.S.,and Baştürk, A., 1999. Anaerobic and Chemical Treatability of Young Landfill Leachate in 7th International Waste Management and Landfill Symposium, October 4-8, Cagligari, Italy.
CR  - Buffiére, P., Fonade, C., and Moletta, R., 1998. Mixing and Phase Hold-Ups Variations due to Gas Production in Anaerobic Fluidized-Bed Digesters: Influence on Reactor Performance. Biotechnol Bioeng, 60(1), 36-43.
CR  - Cooper, P., Crabtree, H.E., Austin, E.P. and Green, M.K., 1984. Some Recent Developments in Sewage Treatment in UK with CAPTOR and Biological Fluidised Bed, in La Biomasse Fixee Dans Le Traitement des Eaux, 37es Journees Int., CEBEDEAU, Liege, 23-25 Mai, pp: 307-339.
CR  - Heijnen, J.J., Mulder, A., Weltevrede, R., Hols, J. and van Leeuwen, H., 1991. Large Scale Anaerobic- Aerobik Treatment of Complex Industrial Wastewater Using Biofilm Reactors, Wat. Sci. Technol. 23, 1427- 1436.
CR  - Shieh, W.K. and Keenan, J.D., 1986. Fluidized Bed Biofilm Reactor for Wastewater Treatment, in Advances in Biochemical Engineering / Biotechnology, ed: Fiechter A., 33, Springer, Berlin, p: 131-169.
CR  - Encina, P.A.G., Hidalgo, M.D., 2005. Influence of Substrate Feed Patterns on Biofilm Development in Anaerobic Fluidized Bed Reactors (AFBR), Process Biochemistry, 40(7), 2509-2516.
CR  - Mussati, M., Thompson, C., Fuentes, M., Aguirre, P., Scenna, N., 2005. Characteristics of a Methanogenic Biofilm on Sand Particles in a Fluidized Bed Reactor, Latin American Applied Research, 35(4), 265-272.
CR  - Arnaiz, C., Gutierrez, J.C., Lebrato, J., 2006. Support Material Selection for Anaerobic Fluidized Bed Reactors by Phospholipid Analysis, Biochemical Engineering Journal, 27(3), 240-245.
CR  - Cresson, R., Carrere, H., Delgenes, J.P., Bernet, N., 2006. Biofilm Formation During the Start-Up Period of an Anaerobic Biofilm Reactor - Impact of Nutrient Complementation, Biochemical Engineering Journal, 30(1), 55-62.
CR  - Hsu, Y., and Shieh, W.K., 1993. Startup of Anaerobic Fluidized Bed Reactors With Acetic Acid as the Substrate, Biotechnol. Bioengng., 41, 347-363.
CR  - Ro, K.S., and Neethling, J.B., 1994. Biological Fluidized Beds Containing Widely Different Bioparticles, J. Environ. Engrg. ASCE. 120(6), 1416-1426.
CR  - Turan, M., 2000. Mechanisms of Biofilm Detachment in an Anaerobic Fluidized Bed Reactor, Environ. Technol., 21, 177-183.
CR  - Gulsen, H., Turan, M., Armagan, B., 2004. Anaerobic Fluidized Bed Reactor for the Treatment of Landfill Leachates, Journal of Environmental Science and Health A, 39(8), 2195 – 2204.
CR  - Borja, R., Martín, A., Banks, C.J., Alonso, V., and Chica, A., 1995. A Kinetic Study of Anaerobic Digestion of Olive Mill Wastewater at Mesophilic and Thermophilic Temperatures, Environ. Pollut., 88(1), 13-18.
CR  - Diez, V., García, P.A., and Fdz-Polanco, F., 1999. Evaluation of methanogenic kinetics in an anaerobic fluidized bed reactor (AFBR), Process Biochemistry, 34(3), 213-219.
UR  - https://dergipark.org.tr/en/pub/dufed/issue//698225
L1  - https://dergipark.org.tr/en/download/article-file/991977
ER  -