S. Zinadini
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9 records found
1
The synthesis of chemically derived bituminous-based activated carbons (ACs) was conducted in this research. The study examined the efficacy of the KOH-2 modified AC by conducting batch experiments under different operating settings. Pollutant concentration, adsorbent dosage and contact time were considered as variables. Bovine serum albumin (BSA), dextrose, and methylene blue (MB) were used as model substances to represent protein, carbon, and textile dyes, respectively. Under optimal conditions, the activated carbon modified with a 2:1 impregnation ratio using KOH showed the best performance among two other ACs, therefore, that was introduced as chosen AC. The optimal parameters were determined as pollutant concentration, adsorbent dosage and contact time obtained to be 600 mg/L, 0.22 g/L and 220 min; 200 mg/L, 0.6 g/L and 180 min; 200 mg/L, 1 g/L and 196 min for MB, BSA and dextrose, respectively. This AC obtained the highest adsorption capacity of 2710.6, 283, and 273 mg/g adsorbing MB, BSA and dextrose, respectively. In the following, column studies were conducted using biologically treated wastewater obtained from a new one-stage hybrid internal circulation airlift A2O bioreactor to eliminate soluble microbial products (SMP). It was seen that the adsorption column, which was filled with the AC under optimal experimental conditions (bed height of 4.5 cm and solution flow rate of 5 mL/min), resulted in a decrease in residual organic substances from 35 mg-TOC/L to 6.6 mg-TOC/L. It is worth mentioning that the utilization of an integrated approach involving sophisticated biological treatment and post-treatment technology has demonstrated efficacy in the elimination of residual organic substances.
This study focuses on the development of an air-lift bio-electrochemical reactor (ALBER) with a continuous feeding regime. The objective is to enhance nitrogen removal from synthetic wastewater with a low carbon-to-nitrogen (C/N) ratio. The chemical oxygen demand (COD) and total nitrogen (TN) of the influent wastewater were 500 and 200 mg/L, respectively. The effect of four independent variables, i.e., temperature, hydraulic retention time (HRT), N−NH4+/TN ratio and current density in the range of 16–32 °C, 6–12 h, 25–75%, and 2–10 A/m2, respectively, at three levels on the bio–electrochemical reactor performance were investigated during the bio–electrochemical reactor operation. The Face Center Cube (FCC) of response surface methodology (RSM) was used for design of experiments and model of obtained data. The ALBER achieved the maximum TN removal of 73% (146 mg/l) using external voltage and zeolite/plastic medium at temperature of 16 °C, HRT of 6 h, current density of 2 A/m2 and N−NH4+/TN ratio of 75%. The results indicated that shortening the HRT from 12 to 6 h, reducing the temperature from 32 °C to 24 °C, increasing the current density from 2 to 6 A/m2 and the reduction of nitrate concentration caused an increase in the TN removal. The results indicated that the performance of air-lift bio-electrochemical for nitrogen removal could be attributed to autotrophic denitrification (AD) and simultaneous nitrification/denitrification (SND). The research findings suggest that the ALBER should be further studied for potential use in treating industrial wastewater at low temperatures.
Concurrent removal of carbon and nutrients in a one-stage dual internal circulation airlift A2O bioreactor from milk processing industrial wastewater
Process optimization, sludge characteristics and operating cost evaluation
In this work, a one-stage dual internal circulation airlift anaerobic/anoxic/aerobic (DCAL-A2O) bioreactor was continuously operated for concurrent removal of nutrients and organics from milk processing wastewater (MPW). Special configuration of the airlift A2O bioreactor created possibility of the formation of desired anaerobic, anoxic and aerobic zones in a single unit. The process functionality of the bioreactor was examined under three influential operating variables i.e. hydraulic retention time (HRT; 7–15 h), air flow rate (AFR; 1–3 L/min) and aerobic volume ratio (AVR; 0.324–0.464). The optimum region was identified at HRT of 13h, AFR of 2L/min and AVR of 0.437, leading to TCOD, TN and TP removal efficiency of 94.5 %, 59.6 %, and 62.2 %, respectively, and effluent turbidity of 8 NTU. The impact of feed biodegradability on the process performance of the bioreactor treating the MPW, soft drink wastewater (SDW) and soybean oil plant wastewater (SOW) was also assessed. From the results, the feed characteristics affected significantly the nutrients removal. Moreover, the feeding location played an effective role in the nutrient removal while treating the MPW at optimum operating conditions. In this study, the change in residual organic matters as soluble microbial products (SMP) was monitored at various operating conditions. In addition, the impact of SMP extracted from sludge, extracellular polymeric substances (EPS) comprising of loosely bound EPS (LB-EPS) and tightly bound EPS (TB-EPS) was analyzed on sludge characteristics as bio-flocculation and settleability properties. According to the obtained data, the increase in operating variables led to the reduction in contents of effluent SMP, sludge SMP, LB-EPS, turbidity, and SVI, thereby, the enhancement in the sludge characteristics. Meanwhile, analysis of microbial communities verified the presence of various functional bacterial species. The cost operating evaluation confirmed the cost effectiveness of the airlift A2O bioreactor in reduction of energy consumption for the MPW treatment.
Developing an effective and stable separation membrane for water treatment is of much interest while challenging because of the restrictions of membrane fouling and water flux reduction. To minimize this problem, in this work, highly porous and hydrophilic nanostructure of NH2-modified MCM-41 (NH2-MCM-41) was embedded successfully into the nanofiltration (NF) membrane body via commonly used phase inversion method. The unmodified and modified nanofiller was analyzed by Fourier Transform Infrared (FTIR) spectroscopy, X-Ray powder diffractometry (XRD), field emission scanning electron microscopy (FE-SEM), thermogravimetric analysis (TGA), and nitrogen adsorption–desorption. Furthermore, the modified membranes were characterized through surface and cross section FE-SEM images, the membrane surface roughness, hydrophilicity, antifouling properties and dye rejection. Benefiting from porous networks and enhanced hydrophilicity, the mixed matrix membranes (MMMs) revealed more prominent hydrophilic property as well as higher pure water flux (PWF) compared with naked membrane. The polysulphone (PSf) membrane modified with NH2-MCM-41-1.0 exhibited the highest pure water flux (PWF) of 65.43 kg/m2.h and superior antifouling characteristics with a flux recovery ratio (FRR) of around 97.0% and an irreversible fouling resistance (Rir) of 3.2%. Furthermore, the optimal membrane possessed high dye rejection (100%) and antifouling capacity (FRR of 97%) while filtering a field sample, effluent from a local stabilization pond treating municipal wastewater. The fabricated membrane in this study is believed to pave pathways for constructing NF membranes with superior effectiveness for other municipal and industrial wastewaters treatment.
The aim of this study was to remove non-biodegradable colored compounds from biologically treated baker's yeast effluent using an antifouling membrane in order to facilitate reuse of the wastewater. To get this purpose, in a facile effort, a new nanofiller, citric acid functionalized tannic acid (CA-f-TA), was synthesized by employing a simple, economical and green method. The produced nanofiller was used in the fabrication of polyethersulfone (PES) nanofiltration (NF) membranes. The influence of CA-f-TA on the cross section morphology, pore size, porosity, water content, hydrophilic properties, and roughness of the modified PES/NF membrane was evaluated. The performance of the fabricated membranes was analyzed as pure water flux (PWF), antifouling and dye rejection capacity. Based on obtained results, incorporation of the CA-f-TA nanofiller resulted in an increase in the PWF from 23.5 to 23.6 and 34.4 kg m-2 h-1 for the membranes blended with CA-f-TA-1, CA-f-TA-0.5 and CA-f-TA-0.1, respectively, in contrast to 16.4 kg m-2 h-1 for the reference membrane. The antifouling characteristics of the prepared membranes dramatically raised owing to improvement in smoothness and hydrophilicity of membrane surface. The synthesized NF membrane with 1 wt% CA-f-TA nanofiller had the highest flux recovery ratio (FRR, 93.2%) and dye rejection (95.7% for Direct Red 16 (DR 16) and 97% for biologically treated baker's yeast wastewater), and the lowest irreversible fouling resistance (6.8%). Furthermore, PWF of 34 kg m-2 h-1, FRR of 97%, TSS and turbidity removal efficiencies of 100%, and COD removal efficiency of 80% were obtained using the 1 wt% CA-f-TA membrane after filtration of a field sample i.e. biologically treated baker's yeast wastewater over a 1-h filtration.
In this research, the manufacture and properties of polyethersulfone (PES)-based mixed matrix nanofiltration (MM-NF) membranes modified with β-cyclodextrin functionalized multiwalled carbon nanotubes (β-CD/MWCNTs) were studied. The β-CD/MWCNTs nanocomposite was synthesized using the soft cutting method. Stable dispersivity of the resulting nanocomposite was checked for 12 h. Then, the membranes containing up to 1 wt% β-CD/MWCNTs were prepared using conventional phase inversion method. The impact of varied mass loadings of the β-CD/MWCNTs on the morphological features and performance of the amended membranes was evaluated. It was deduced that membrane hydrophilicity, porosity, pore size, water contents, dye rejection and antifouling capacity were noticeably improved after incorporating the β-CD/MWCNTs nanomaterials. In comparison with the bare membrane, the β-CD/MWCNTs amended membranes displayed higher hydrophilicity, and consequently pure water flux (PWF). Since β-CD can exploit the structure advantages of MWCNTs via enhancement of the dispersivity, devoting unique features to the β-CD/MWCNTs nanomaterial. The 0.1 wt% nanocomposite membrane sample revealed the highest pure water flux of 21.5 Kg/m2.h due to increase in pore size (5.0 nm). While, the membrane contributed with the β-CD/MWCNTs-0.5 revealed better performance in terms of dye rejection and antifouling capability than the bare and modified membranes. It indicated a dye rejection of above 92%, flux recovery ratio (FRR) of 89% and an irreversible resistance of 11.1%. The β-CD/MWCNTs-0.5 acted as a potential nanofiller in nanofiltration (NF) membranes improving their antifouling performance at different operational conditions.