title: Consecutive reaction kinetics involving a layered structure of the granule in UASB reactors.
abstract: A consecutive-reaction kinetic model for the sucrose-fed upflow anaerobic sludge bed (UASB) reactor that accounts for a layered structure of the granule and the mass fraction of methanogens (f) is proposed. When the UASB reactor was maintained at the volumetric loading rates (VLR) of 7.9-13.8 kg chemical oxygen demand (COD)/m(3) d, the accumulated volatile fatty acids (VFAs) increased with increasing VLR, whereas the experimental f decreased with increasing VLR. This was primarily because methanogenesis was the rate-limiting step and the sucrose-fed granule was a layered structure. The calculated residual concentrations of sucrose and the intermediates VFAs using the layered-structure model are less deviated from the experimental measurements than those using the homogeneous-structure model. The calculated effectiveness factors for sucrose uptake and intermediates VFAs uptake (eta(1); eta(2)) ranged from 0.18 to 0.35 and 0.65 to 0.96, respectively, indicating that the overall substrate (sucrose or intermediates VFAs) removal in the UASB reactor was diffusion-controlled, especially at the VLRs of 7.9-10.6. kg COD/m(3) d. This finding was also confirmed by the simulated concentration profiles of sucrose and VFAs in the UASB-granule. From the simulation results, the effect of internal mass transfer resistance on overall substrate (sucrose) removal should not be neglected, especially for a granule size of greater than 2.0 mm.
authors.affiliation: Department of Environmental Engineering, Kun Shan University, Tainan County 710, Taiwan, ROC. huangjsd@mail.ncku.edu.tw
authors.forename: Ju-Sheng
authors.initials: JS
authors.lastname: Huang
authors.forename: Hsin-Hsien
authors.initials: HH
authors.lastname: Chou
authors.forename: Reiko
authors.initials: R
authors.lastname: Ohara
authors.forename: Chun-Sheng
authors.initials: CS
authors.lastname: Wu
mesh_terms: D019149:Bioreactors; D007218:Industrial Microbiology; D007220:Industrial Waste; D007700:Kinetics; D008956:Models, Chemical; D008962:Models, Theoretical; D010100:Oxygen / Q000378:metabolism; D013395:Sucrose / Q000032:analysis; D014865:Waste Disposal, Fluid / Q000295:instrumentation / Q000379:methods*; D018508:Water Purification / Q000295:instrumentation / Q000379:methods*
chemical_list: D007220:Industrial Waste; D013395:Sucrose; D010100:Oxygen