2011-5-10 · Theoretical Performance of Fluidized Bed Biological Reactors 757 Sizing a Fluidized Bed Biological Reactor 759 Key Points 761 Study Questions 762 References 763 Part V applications: attached Growth reactors Chapter 19 Process Description 767 .
Chemical and Biological Engineering. The University of British Columbia. Fixed Bed Reactor . Over some time, solids either replaced or regenerated. 1. 2. CA, . – A free PowerPoint PPT presentation (displayed as a Flash slide show) on PowerShow.com - id: 25112f-ZDc1Z
2020-5-28 · 400±50 μm. Since the nitrogen removal performance and the microbial community were relatively stable during the entire experiment, it is reasonable to assume that the biofilm thickness is also stable during the long-term operation. Therefore, the biofilm thickness is set to be 400 μm in the model constantly. Figure S3.
Two laboratory-scale high performance fluidized bed biofilm reactors (FBBR) with sand as the biofilm carrier were used to investigate the denitrification of high-strength nitrate wastewater with .
2013-11-30 · Performance of Fluidized Bed Biofilm Reactor For Nitrate Removal 40 | Page NO 1.08CH OH H 0.065C H NO 0.467N 0.76CO 2.44H O 3 3 5 7 2 2 2 2 o (5) Extension of Equation 5 to take also nitrite and oxygen, which often keep company with nitrate in the feed, into
Performance of Fluidized Bed Biofilm Reacto r For Nitrate Removal 43 | Page In t he prese nt st udy, t he nitrogen loading rate s varied from 0.48 kg N m -3 d -1 to 28.80 kg N m -3 d .
@article{osti_5260480, title = {Design of fluidized-bed fermentors}, author = {Andrews, G F and Przezdziecki, J}, abstractNote = {Designing a fluidized-bed bioreactor requires choosing the best support particle (if any). Effectiveness factors (proportional to reactor volumetric productivity) are derived for flocs, solid spherical supports, porous supports, and adsorbent supports.
In order to obtain a stable nitrogen removal performance at low temperatures, it is necessary to immobilize anammox bacteria in the reactor, because the growth rates (Isaka et al., 2006) and activities of anammox bacteria are extremely low at low temperatures. In view of this, we used a gel carrier in which anammox bacteria were entrapped, and .
The reactor includes a hollow fiber membrane bundle. Pressurized hydrogen and water are introduced into a volume containing the fiber bundle. The fibers are free to separate and more independently over most of their length. The fibers have microporous inner and outer layers and a nonporous layer sandwiched between the inner and outer layers and are sealed on one end.
Herein, the progress of nitrate removal by a heterotrophic culture in a batch reactor and continuous-flow fixed-biofilm reactor was examined. Two batch experiments for nitrate reduction with acetate degradation using 250 mL batch reactors with acclimated denitrifying biomass were conducted. The experimental results indicated that the nitrate was completely reduced; however, the acetate .
In order to obtain a stable nitrogen removal performance at low temperatures, it is necessary to immobilize anammox bacteria in the reactor, because the growth rates (Isaka et al., 2006) and activities of anammox bacteria are extremely low at low temperatures. In view of this, we used a gel carrier in which anammox bacteria were entrapped, and .
Nitrate is present in the majority of water resources, and has reached serious level in many parts of the world, which is responsible for environmental problems. Hence it is necessary to remove nitrate. Biological denitrification provides the most
The effect of upflow velocity on performance and biofilm characteristics of an Anaerobic Fluidized Bed Reactor was studied in treating Currant wastewater at various loading rates. The reactor used this study was made of a plexiglass column being 60 mm diameter, 140 cm height, and a volume of 3.95 L.
In addition, one of our previous works demonstrated that 99.5% nitrate removal could be achieved at a C/N ratio as low as 1.5 in a continuous-operation biofilm-electrode reactor with sodium acetate as the carbon source (Peng et al. 2015). In that case, the heterotrophic denitrification accounted for 92% of nitrate removal.
2018-4-18 · Nitrogen Removal in Biological Wastewater Treatment Plant Courtney Greyn . second anomaly from the data analysis is the difference in treatment performance between the two Moving Bed Biofilm Reactors (MBBRs). . fluidized bed reactor, moving bed biofilm reactor. iii Dedication I wish to thank my parents for all of their love and support .
(2004). Nitrate removal characteristics of high performance fluidized-bed biofilm reactors. (2001). Nonlinear parameter estimation through particle swarm optimization. (1989). Novel pathway of toluene catabolism in the trichloroethylene-degrading bacterium (1996).
A pilot biological fluidized‐bed plant with a capacity of 40 m 3 /h has been in operation since January 1988 at De Blankaart drinking water production center for removing nitrate from surface water. Methanol is used as the reductant. With a nitrate removal efficiency of 9.0 kg NO 3 − /m 3 reactor.day at 3.5°C, the system has shown superior performance compared with conventional fixed .
A moving bed biofilm reactor (MBBR) is a process utilizing a basin filled with a carrier medium that promotes attachment and growth of biofilm carrying out biological treatment. MBBRs have been extensively used for BOD/COD removal, as well as for nitrification and denitrification in municipal and industrial wastewater treatment.
Theoretical Performance of Fluidized Bed Biological Reactors 757 Sizing a Fluidized Bed Biological Reactor 759 Key Points 761 Study Questions 762 References 763 Part V applications: attached Growth reactors Chapter 19 Process Description 767 .
A steady‐state biofilm is defined as one that has neither net growth nor decay over time. The model, developed for steady‐state‐biofilm kinetics with a single substrate, couples the flux of substrate into a biofilm to the mass (or thickness) of biofilm that would exist at .
The reactor includes a hollow fiber membrane bundle. Pressurized hydrogen and water are introduced into a volume containing the fiber bundle. The fibers are free to separate and more independently over most of their length. The fibers have microporous inner and outer layers and a nonporous layer sandwiched between the inner and outer layers and are sealed on one end.
Fixed Bed Reactor. FBR Design 8 (7a) FBR design equation (7b) First order, irreversible reaction Thiele modulus is independent of concentration (7c) Effectiveness factor is constant along the axial length. 64 Fixed Bed Reactor. FBR Design 9 (7d) Concentration in term of molar flow (7e) Substituting into the FBR design equation. 65 Fixed Bed Reactor
Microbial bioremediation of petroleum wastewater by phenol-degrading-bacteria holds promise in circumventing the issue of petroleum-spill related pollution. Herein, biodegradation of petroleum wastewater samples collected from oil refinery site was carried out in a fluidized bed bioreactor by Ca-alginate immobilized biomass of phenol-degrading strains of Bacillus cereus (AKG1 MTCC9817 and .
2017-11-21 · FLUIDIZED BED FS-BIO-007 Page 2 of 16 1.- DESCRIPTION This fact sheet describes the design criteria and operation of fluidized bed reactors in order to oxidize organic matter in waste water from the textile industry. Fluidized beds are biofilm reactors with a wide range of applications in biological aerobic, anoxic and anaerobic treatment.
The lab-scale upflow anaerobic biofilm reactor was successfully operated for the treatment of synthetic wastewater with high nitrogen load by Anammox (anaerobic ammonium oxidation) process. During the entire period of operation, the reactor temperature was kept at 35±1°C. The operational strategy consisted of both increasing the ammonium and nitrite concentrations from 60 to 700mgN/L and .
2004-12-7 · Chapter ll 15 2.3 BIOFILM FROM INORGANIC TREATMENT 2.3.1 MATERIALS AND METHODS 2.3.1.1 Reactor System The above-described substrate (600 -N/m3) was gcontinuously fed at 1.0 L/day to a fluidized bed bioreactor with an effective volume of 2 L.
2004-12-7 · There are two advantages of biological wastewater treatment using a fluidized bed reactor with a biofilm fixed on particles: 1) the reactor has active transfer phenomena accelerated by fluidizing materials, and 2) the reactor retains 5-10 times higher biomass concentration than conventional activated sludge reactors [5, 6].
Long-term performance evaluation of an anoxic sulfur oxidizing moving bed biofilm reactor under nitrate limited conditions†. Ramita Khanongnuch * a, Francesco Di Capua c, Aino-Maija Lakaniemi a, Eldon R. Rene b and Piet N. L. Lens ab a Tampere University, Faculty of Engineering and Natural Sciences, P.O. Box 541, FI-33014 Tampere, Finland.
2017-11-21 · FLUIDIZED BED FS-BIO-007 Page 2 of 16 1.- DESCRIPTION This fact sheet describes the design criteria and operation of fluidized bed reactors in order to oxidize organic matter in waste water from the textile industry. Fluidized beds are biofilm reactors with a wide range of applications in biological aerobic, anoxic and anaerobic treatment.
Read "Denitrification Performance of Pseudomonas denitrificans in a Fluidized‐Bed Biofilm Reactor and in a Stirred Tank Reactor, Engineering in Life Sciences" on DeepDyve, the largest online rental service for scholarly research with thousands of academic publications available at your fingertips.