scholarly journals High Loaded Bioflocculation Membrane Reactor of Novel Structure for Organic Matter Recovery from Sewage: Effect of Temperature on Bioflocculation and Membrane Fouling

Water ◽  
2020 ◽  
Vol 12 (9) ◽  
pp. 2497
Author(s):  
Liguo Wan ◽  
Ling Xiong ◽  
Lijun Zhang ◽  
Wenxi Lu
Keyword(s):  
Organic Matter ◽  
Low Temperature ◽  
Membrane Fouling ◽  
Membrane Reactor ◽  
Municipal Wastewater ◽  
Fine Particles ◽  
Effect Of Temperature ◽  
Recovery Efficiency ◽  
Solid Retention Time ◽  
Novel Structure

The effect of temperature on the efficiency of high loaded bioflocculation membrane reactor (HLB-MR) flocculation and concentration of organic matter in municipal wastewater was analyzed using parallel comparative experiments. The study investigated organic matter recovery efficiency, bioflocculation effect, and membrane fouling status of the reactor at 8 °C and 15 °C. It was observed that at a low temperature of 8 °C, the organic matter recovery efficiency of HLB-MR was 80%, which was equivalent to that at 15 °C. However, the bioflocculation efficiency at 8 °C was only 65%, which was significantly lower than that of 85% achieved at 15 °C. The poor flocculation effect was related to the low yield of the extracellular polymer under low-temperature conditions and the low content of cations (sodium, calcium, and aluminum) in the sludge matrix. At the low temperature of 8 °C, the membrane fouling of the HLB-MR was more serious than that at 15 °C. Poor bioflocculation effect led to an increase in the number of fine particles (≤1 μm) in the reactor, which might be the main reason for the aggravation of membrane fouling. To overcome the adverse effects of low temperature on membrane fouling, it is recommended to adopt engineering measures, such as an appropriate increase in the solid retention time, increase in the aeration intensity, using powdered activated carbon, or enhancing the intensity of backwashing.

Tracking particle size distributions in a moving bed biofilm membrane reactor for treatment of municipal wastewater

2006 ◽  
Vol 53 (7) ◽  
pp. 33-42 ◽  
Author(s):  
R.M. Åhl ◽  
T. Leiknes ◽  
H. Ødegaard
Keyword(s):  
Particle Size ◽  
Membrane Fouling ◽  
Membrane Reactor ◽  
Colloidal Particles ◽  
Municipal Wastewater ◽  
Operating Conditions ◽  
Size Distributions ◽  
Particle Size Distributions ◽  
Moving Bed ◽  
Loading Rates

A study has been conducted to investigate the effect of loading rates on membrane fouling in a moving bed biofilm membrane reactor process for municipal wastewater treatment, especially analysing the fate of submicron colloidal particles and their influence on membrane fouling. Two operating conditions defined as low and high organic loading rates were tested where the development and fate of the particulate material was characterised analysing the particle size distributions throughout the process. Analysis of the membrane performance showed higher fouling rates for the high-rate conditions. The fraction of colloidal submicron particles was higher in the membrane reactor indicating that fouling by these particles was a dominant contribution to membrane fouling.

scholarly journals The membrane fouling mechanisms of the PAC/BPAC-UF combined process used to treat the secondary effluent from municipal wastewater treatment plant

2017 ◽  
Vol 77 (1) ◽  
pp. 211-219 ◽  
Author(s):  
Lihua Sun ◽  
Ning He ◽  
Xi Duan ◽  
Bingbing Yang ◽  
Cuimin Feng ◽  
...  
Keyword(s):  
Molecular Weight ◽  
Organic Matter ◽  
Activated Carbon ◽  
Membrane Fouling ◽  
Municipal Wastewater ◽  
Membrane Surface ◽  
Treatment Plant ◽  
Powdered Activated Carbon ◽  
Combined Processes ◽  
Secondary Effluent

Abstract The combined processes of powdered activated carbon/biological powdered activated carbon- ultrafiltration (PAC/BPAC-UF) were used to treat secondary effluent. In this study, the effect of PAC and BPAC on membrane flux, membrane resistance and the removal of different molecular weight organic compounds were investigated. In addition, the structure characteristics of the microorganisms of the BPAC were analyzed. The results showed that the optimum dosage of PAC and BPAC was 10 mg/L and 40 mg/L respectively. The reversible membrane fouling resistance of BPAC-UF was higher than that of PAC-UF, and the two processes had the least irreversible resistance at the best dosage. The biodegradation of BPAC increased the concentration of small molecular weight organic matter up to 10,000 Da in the membrane effluent. So the dissolved organic carbon (DOC) removal effect of BPAC-UF process worsened. Microorganisms such as Proteobacteria, Bacteroidetes, Planctomycetes and other microorganisms on the surface of the BPAC enhanced the removal of organic matter in water. The results of scanning electron microscopy (SEM) scans showed that there was net mucus membrane on the UF membrane surface before the backwashing of the BPAC-UF process which increased the proportion of reversible pollution resistance. The physical flushing effect of BPAC-UF was better than that of direct UF and PAC-UF processes.

Bio-entrapped membrane reactor for organic matter removal and membrane fouling reduction

2012 ◽  
Vol 50 (1-3) ◽  
pp. 59-66 ◽  
Author(s):  
Kok-Kwang Ng ◽  
Chien-Ju Wu ◽  
Li-Yuan You ◽  
Chin-Sheng Kuo ◽  
Cheng-Fang Lin ◽  
...  
Keyword(s):  
Organic Matter ◽  
Membrane Fouling ◽  
Membrane Reactor ◽  
Organic Matter Removal ◽  
Fouling Reduction

scholarly journals Removal characteristics of dissolved organic matter and membrane fouling in ultrafiltration and reverse osmosis membrane combine processes treating the secondary effluent of wastewater treatment plant

2020 ◽  
Author(s):  
Jianwei Liu ◽  
Mengfei Zhao ◽  
Cui Duan ◽  
Peng Yue ◽  
Tinggang Li
Keyword(s):  
Organic Matter ◽  
Wastewater Treatment ◽  
Humic Acid ◽  
Fulvic Acid ◽  
Reverse Osmosis ◽  
Membrane Fouling ◽  
Municipal Wastewater ◽  
Treatment Plant ◽  
Municipal Wastewater Treatment ◽  
Ro Membrane

Abstract The widespread implementation of municipal wastewater treatment and reuse must first ensure the safety of reused wastewater. The effluent of the municipal wastewater treatment plant contains a large amount of dissolved organic matter (DOM), which adversely affects the reuse of wastewater. In this study, the ultrafiltration (UF) + reverse osmosis (RO) process was used to treat the effluent from wastewater treatment plants. The relationship between the removal performance, membrane fouling of the UF + RO process, and DOM characteristics of influent were studied. The results show that DOM can be removed effectively by UF + RO process. The UF mainly removes DOM with a molecular weight greater than 10 kDa, while RO has a significant removal effect on low-molecular DOM, which mainly cause UF and RO membrane fouling. The UF + RO process has a significant removal rate on fulvic acid, humic acid, tyrosine, and tryptophan, and the order is humic acid > fulvic acid > tyrosine > tryptophan. Fulvic acid contributed the most to the UF membrane fouling, while fulvic acid and protein-like proteins contributed mainly to the RO membrane fouling.

scholarly journals Influence of temperature on the start-up of membrane bioreactor: kinetic study

2017 ◽  
Vol 77 (2) ◽  
pp. 448-455 ◽  
Author(s):  
J. C. Leyva-Díaz ◽  
J. Martín-Pascual ◽  
G. Calero-Díaz ◽  
J. C. Torres ◽  
J. M. Poyatos
Keyword(s):  
Organic Matter ◽  
Membrane Bioreactor ◽  
Municipal Wastewater ◽  
Effect Of Temperature ◽  
Municipal Wastewater Treatment ◽  
Organic Matter Removal ◽  
Influence Of Temperature ◽  
Operation Conditions ◽  
Start Up ◽  
Influence Of Temperature On

Abstract The start-up phase of a membrane bioreactor (MBR) for municipal wastewater treatment was studied to determine the effect of temperature on the organic matter removal and heterotrophic kinetics. The MBR system was analyzed during four start-up phases with values of hydraulic retention time (HRT) of 6 h and 10 h, mixed liquor suspended solids (MLSS) concentrations of 4,000 mg L−1 and 7,000 mg L−1 in the steady state, and temperature values of 11.5, 14.2, 22.9 and 30.1 °C. The influence of temperature on the biological process of organic matter removal was determined through the Arrhenius equation and Monod model. At the most favorable operation conditions of HRT (10 h) and MLSS (7,000 mg L−1) corresponding to phase 4, the effect of these variables dominated over the temperature. Heterotrophic biomass from phase 2 (HRT = 10 h, MLSS = 4,000 mg L−1 and T = 30.1 °C) had the highest values of chemical oxygen demand (COD) degradation rate (rsu,H), implying less time to remove organic matter and shorter duration of the start-up phase.

Modeling fine particles and alkali metal compound behavior in a kraft recovery boiler

TAPPI Journal ◽  
2012 ◽  
Vol 11 (7) ◽  
pp. 9-14 ◽  
Author(s):  
AINO LEPPÄNEN ◽  
ERKKI VÄLIMÄKI ◽  
ANTTI OKSANEN
Keyword(s):  
Alkali Metal ◽  
Computational Models ◽  
Fine Particles ◽  
Black Liquor ◽  
Melting Behavior ◽  
Metal Compound ◽  
Effect Of Temperature ◽  
Particle Model ◽  
Boiler Furnace ◽  
Recovery Boiler

Under certain conditions, ash in black liquor forms a locally corrosive environment in a kraft recovery boiler. The ash also might cause efficiency losses and even boiler shutdown because of plugging of the flue gas passages. The most troublesome compounds in a fuel such as black liquor are potassium and chlorine because they change the melting behavior of the ash. Fouling and corrosion of the kraft recovery boiler have been researched extensively, but few computational models have been developed to deal with the subject. This report describes a computational fluid dynamics-based method for modeling the reactions between alkali metal compounds and for the formation of fine fume particles in a kraft recovery boiler furnace. The modeling method is developed from ANSYS/FLUENT software and its Fine Particle Model extension. We used the method to examine gaseous alkali metal compound and fine fume particle distributions in a kraft recovery boiler furnace. The effect of temperature and the boiler design on these variables, for example, can be predicted with the model. We also present some preliminary results obtained with the model. When the model is developed further, it can be extended to the superheater area of the kraft recovery boiler. This will give new insight into the variables that increase or decrease fouling and corrosion

Coagulation/flocculation/ultrafiltration for natural organic matter removal in drinking water production

2004 ◽  
Vol 4 (5-6) ◽  
pp. 215-222 ◽  
Author(s):  
A.R. Costa ◽  
M.N. de Pinho
Keyword(s):  
Drinking Water ◽  
Organic Matter ◽  
Natural Organic Matter ◽  
Membrane Fouling ◽  
Membrane Filtration ◽  
Membrane Surface ◽  
Water Production ◽  
Cellulose Acetate Membranes ◽  
Wide Range ◽  
Drinking Water Production

Membrane fouling by natural organic matter (NOM), namely by humic substances (HS), is a major problem in water treatment for drinking water production using membrane processes. Membrane fouling is dependent on membrane morphology like pore size and on water characteristics namely NOM nature. This work addresses the evaluation of the efficiency of ultrafiltration (UF) and Coagulation/Flocculation/UF performance in terms of permeation fluxes and HS removal, of the water from Tagus River (Valada). The operation of coagulation with chitosan was evaluated as a pretreatment for minimization of membrane fouling. UF experiments were carried out in flat cells of 13.2×10−4 m2 of membrane surface area and at transmembrane pressures from 1 to 4 bar. Five cellulose acetate membranes were laboratory made to cover a wide range of molecular weight cut-off (MWCO): 2,300, 11,000, 28,000, 60,000 and 75,000 Da. Severe fouling is observed for the membranes with the highest cut-off. In the permeation experiments of raw water, coagulation prior to membrane filtration led to a significant improvement of the permeation performance of the membranes with the highest MWCO due to the particles and colloidal matter removal.

Study on the performance of an up-flow aerated biofilter (UAB) in municipal wastewater treatments

1994 ◽  
Vol 30 (11) ◽  
pp. 25-33 ◽  
Author(s):  
Yoshimasa Watanabe ◽  
Satoshi Okabe ◽  
Tomochika Arata ◽  
Yuji Haruta
Keyword(s):  
Organic Matter ◽  
Suspended Solids ◽  
Municipal Wastewater ◽  
Unique Feature ◽  
Aeration Rate ◽  
Loading Rates ◽  
Hydraulic Loading ◽  
Running Cost ◽  
And Performance ◽  
Activated Sludge Systems

A comprehensive wastewater treatment system that accomplishes oxidation of organic matter, nitrification, and denitrification was developed, and its characteristics and performance were investigated. A municipal wastewater was treated by an up-flow aerated biofilter (UAB), in which biofilms were developed on stainless meshes installed horizontally. This UAB exhibited a great potential ability of oxidation of organic matter, SS stabilization, and nitrification due to a unique aeration mechanism giving high DO concentrations with relatively low aeration rates. Another unique feature of the UAB was that attached biofilms on stainless meshes physically filtered out and/or adsorbed suspended solids in the wastewater in addition to the biological oxidation of organic matter. A stable nitrification could be achieved at HRT=10 hours corresponding to a hydraulic loading of 86 L m−2 d−1 and at a ratio of aeration rate to wastewater flow rate (A/W) of 2, which is considerably low as compared to aeration rates of typical activated sludge systems. This UAB system also could handle relatively high hydraulic loading rates. The UAB used in this study still have enough space to install more stainless meshes so as to reduce hydraulic loading rates resulting in the reduction of HRT and aeration rate, which leads to improvement of the system performance as well as reduction of the running cost.

Sign in / Sign up

Export Citation Format

Share Document