Relevant bibliographies by topics / Electrocoagulation

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  1. Journal articles
  2. Dissertations / Theses
  3. Books
  4. Book chapters
  5. Conference papers
  6. Reports

Academic literature on the topic 'Electrocoagulation'

Author: Grafiati
Published: 4 June 2021
Last updated: 31 July 2024

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Journal articles on the topic "Electrocoagulation"

1

Hu, Zhi Jun, and You Ming Li. "A Combined Electrocoagulation-Electrooxidation Treatment on CTMP Wastewater." Advanced Materials Research 233-235 (May 2011): 619–22. http://dx.doi.org/10.4028/www.scientific.net/amr.233-235.619.

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A synergistic combination of electrocoagulation and electrooxidation was introduced for the treatment of CTMP wastewater in which most of the colloids and charged species had been removed by electrocoagulatio, then small organics could be mineralized by electrooxidation effectively.The mainly influencing factors for electrocoagulation such as electrolyte, sodium chloride dosage, voltage intensity, current intensity and reaction time were assessed. The optimum conditions were obtained, and the results showed that sodium chloride dosage of 1g/L, voltage intensity of 7.5V, current intensity of 0.6A, 60 min reaction time, its color removal rate was above 90% and CODCr removal rate was about 40%. After electrocoagulation the electrooxidation could further reduce CODCr above 80%.
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Pebriana, Ratna Budhi, Endang Lukitaningsih, and Siti Mufidatul Khasanah. "Dechlorophyllation of Cosmos caudatus Kunth., Morinda citrifolia, and Mangifera indica L. Leaves Methanolic Extract by Electrocoagulation Technique." Majalah Obat Tradisional 22, no. 3 (December 21, 2017): 190. http://dx.doi.org/10.22146/mot.31555.

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The present of chlorophyll is not expected in the isolation process of plant active constituent. Electrocoagulation is a potential dechlorophyllation method. This research aims to know the effectivity of electrocoagulation in the dechlorophyllation process of Cosmos caudatus Kunth., Morinda citrifolia, and Mangifera indica L. leaves methanolic extract as well as the effect to the total phenolic content. Electrocoagulation are performed using copper, silver, aluminum and iron plates as the electrode. Dechlorophyllation by extraction using n-hexane is performed as reference. The % absorbance of chlorophyll and % of total phenolic content of dechlorophyllated samples are measured spectrophotometrically. Electrocoagulation process reduces % absorbance of chlorophyll in Cosmos caudatus Kunth., Morinda citrifolia, and Mangifera indica L. leaves methanolic extract. The more the duration of electrocoagulaton process the lower the % absorbance of chlorophyll obtained. % absorbance of chlorophyll of the electrocoagulated extract according to paired t-test (P=0.95) are significantly different with the previous. One way ANOVA continued with LSD (P=0.95) shows that the % absorbance of chlorophyll from the electrocoagulated extract are significantly different with those extracted with n-hexane. Electrocoagulation process reduces total phenolic content along with duration of electrocoagulation.
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Kalivel, Parameswari, Jegathambal Palanichamy, and Mano Magdalene Rubella. "Potential of Ti2O3/Zn Electrodes versus Zn by Electrocoagulation Process for Disperse Dye Removal." Asian Journal of Chemistry 31, no. 8 (June 28, 2019): 1835–41. http://dx.doi.org/10.14233/ajchem.2019.22097.

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Electrocoagulation methods are being used for the alternative treatment process for the remediation of textile waste water. This work primarily deals with the treatment of textile dyeing waste water followed by the utilization of waste material. The purpose of the proposed study is to evaluate the potential of electrocoagulatison process using Ti2O3/Zn electrode prepared by spray pyrolysis using TiCl3 and compared the performance with Zn electrodes. The surface morphology, structural analysis and percentage composition of the elements of the Ti2O3/Zn electrode was studied by SEM, XRD and EDS analysis. The efficiency of electrocoagulation treatment process to treat synthetic waste water containing Coralene Navy RDRLSR, Coralene Red 3G, Rubru RD GLFI dye was studied for the effect of operational parameters. The result indicates that this process was able to achieve colour removal (97.2 %) at pH 8.5, with 34.42 % less energy consumption with Ti2O3/Zn compared with zinc electrodes.
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Hrytsiuk, Ivanna Mykhailivna, Andrii Safonyk, Petro Lakus, and Vasyl Pasichnyk. "Modelling of the process of sewage treatment by electrocoagulation method in the temperature conditions." Modeling, Control and Information Technologies, no. 3 (November 5, 2019): 59–60. http://dx.doi.org/10.31713/mcit.2019.63.

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The paper suggests an approach to modelling the electrocoagulation process taking into account the ratio between the values of the parameters which characterize the domination of convective and mass-exchange components of the process over diffusion. Computer simulation of the distribution of iron concentration inside the electrocoagulator that allows predicting various hydrodynamic phenomena such as internal recirculation that affects the formation of a coagulant was conducted
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Rahman, Nazzeri Abdul, Allene Albania Linus, Calvin Jose Jol, Nur Syahida Abdul Jalal, Wan Wafi Shahanney, and Nooranisha Baharudin. "Characterization of Peat Water Electrocoagulation Flocs from Sarawak Southern Region." Applied Mechanics and Materials 920 (March 5, 2024): 197–208. http://dx.doi.org/10.4028/p-4vuy8n.

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Sarawak located in Borneo is endowed with the vast availability of peat water sources, particularly for the state southern region. Several investigations have shown that electrocoagulation treatment with aluminium electrodes is feasible to treat peat water in which the quality is comparable to the National Water Quality Standard (NWQS). Even though electrocoagulation treatment is feasible to treat peat water, the characteristics of peat water electrocoagulation flocs have not been reported. As such, this study aims to investigate the characteristics of the electrocoagulation flocs from peat water derived from the Sarawak southern region by using batch electrocoagulation treatment. The objectives of this study are to conduct an experimental study analysis of and identify the minerals on the electrocoagulation flocs along with operating energy cost analysis of peat water batch electrocoagulation treatment. Consequently, this study has found that reaction time and current density affect the production of flocs in which the amount of flocs increases with the increasing reaction time and current density. The flocs produced are found to consist of a large fraction of oxygen (O), carbon (C), iron (Fe), and aluminium (Al) along with a small fraction of potassium (K), magnesium (Mg), calcium (Ca) and Silicon (Si). The presence of Al observed in the flocs is due to the aluminium hydroxide generated during the electrocoagulation process. The total operating cost for peat electrocoagulation with a current density of 5A and reaction time of 20 minutes is about RM0.31 per m3. As a result, the electrocoagulation of peat water process is able to treat peat water as well as produce flocs in which earth elements and heavy metals could be recovered.
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Khuê, Võ Anh. "RESEARCH ON ELECTROCHEMICAL METHODS TO REMOVE FLUORIDE FROM WATER." Hue University Journal of Science: Natural Science 126, no. 1C (October 24, 2017): 85. http://dx.doi.org/10.26459/hueuni-jns.v126i1c.4623.

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<p>The use of electrochemical methods such as micro-electrolysis, electrocoagulation, and micro-electrolysis combined with electrocoagulation to remove fluoride from water were studied in this paper. The results indicated that the micro-electrolysis (using Fe/C particles) and the electrocoagulation (using iron electrodes) are not suitable for removal of fluoride from water solution. The electrocoagulation method with aluminum electrodes for removal efficiency of fluoride is very good. But it is not as good as the micro-electrolysis (using Fe/C particles) combined with the electrocoagulation method (using aluminum electrodes). At the optimal condition of the micro-electrolysis (using Fe/C particles) combined with the electrocoagulation method (using aluminum electrodes) and the initial concentration of fluoride ion of 50 mg/L, the removal efficiency of fluoride ion is 94.03% and the residual concentration is 2.986 mg/L.</p>
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Sampliner, Richard E. "Multipolar electrocoagulation." Gastrointestinal Endoscopy Clinics of North America 13, no. 3 (July 2003): 449–55. http://dx.doi.org/10.1016/s1052-5157(03)00048-5.

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Setyawati, Harimbi, Dinda Galuh, and Erni Yunita. "EFFECT OF ELECTRODE DISTANCE AND VOLTAGE ON CR, COD, and TSS REDUCTION IN WASTE WATER TANNING INDUSTRY USING ELECTROCOAGULATOR BATCH." Journal of Sustainable Technology and Applied Science (JSTAS) 2, no. 1 (May 23, 2021): 24–30. http://dx.doi.org/10.36040/jstas.v2i1.3574.

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Wastewater from the tanning industry has relatively high Cr, COD, and TSS metal pollutants. According to the regulation of the Minister of Environment of the Republic of Indonesia No. 5 of 2014 concerning the quality standard of wastewater for industrial activities, the standard quality value is 0.6 mg/L of Cr, 110 mg/L of COD, and 60 mg/L of TSS. This research aimed to determine the effect of electrode distance and voltage on reducing Cr, COD, and TSS levels in the wastewater from the tanning industry using batch electrocoagulation. The electrocoagulation method used in this research with fixed variables was the number of 2 plate electrodes and the changing variables; it was the distance between the electrodes (1, 1.5, 2, 2.5 and 3 cm) and the electric voltage (3, 6 and 9 volts). The research was conducted on a laboratory scale in batches with a capacity of 10 litres. The electrodes used were aluminium (Al) as the anode and the cathode in plates. The analysis showed that the highest percentage reduction in COD reached 88.8889% and the highest Cr reached 83.4712% occurred at a distance of 2 cm with 9 volts voltage, the highest percentage reduction in TSS reached 85.0746% with a distance of 3 cm with 9 volts voltage. From the results of this research, it could be concluded that the electrocoagulation method in the batch electrocoagulator was efficient enough to reduce the levels of Cr, COD, and TSS with variable electrode distance and electric voltage.
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Akter, Hasina, Hasina Akhter Simol, and Shaila Salahuddin. "Treatment of Wastewater Containing Brilliant Orange H2R and Brilliant Red M5B by Electrocoagulation." Dhaka University Journal of Science 64, no. 2 (July 31, 2016): 153–56. http://dx.doi.org/10.3329/dujs.v64i2.54494.

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Treatment of dyeing wastewater containing reactive Brilliant Orange H2R and Brilliant Red M5B dyes were investigated by using electrocoagulation process. The experimental results were analysed in terms of percent removal of dye with time. Electrocoagulation of dye containing wastewater was carried out in a two-electrode monopolar electrocoagulation cell using iron as sacrificial anode and 0.01 M NaCl as internal electrolyte in which the electrolyte concentration was maintained constant during the experiment. In electrocoagulation the effects of concentration of dye and applied current strength on dye removal efficiency were tested and found that both have significant effects on the electrocoagulation of dye from wastewater. Dhaka Univ. J. Sci. 64(2): 153-156, 2016 (July)
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L.Toruan, Ino Eben Lasroha, Sirajudin Haji Abdullah, Sukmawaty Sukmawaty, and Diah Ajeng Setiawati. "Application of Electrocoagulation for Wastewater Treatment of Tofu Production." Protech Biosystems Journal 1, no. 1 (June 30, 2021): 9. http://dx.doi.org/10.31764/protech.v1i1.6001.

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This study aims to process tofu wastewater by using the electrocoagulation method and determine TSS, TDS, and pH efficiency. The Electrocoagulation system was designed based on an electrocoagulation general standard called batch systems. This study used voltage variations of 10, 20, and 30 volts and exposure time during 60, 120, and 180 minutes. The parameters observed were Total Suspended Solid (TSS), Total Dissolved Solid (TDS), and acidity (pH). This study used fresh tofu wastewater with temperature 40-50oC, with a volume of 2000 ml wastewater in one time of electrocoagulation process. The results showed that the designed electrocoagulation system could reduce TSS concentration until 72.2% and TDS 15.4% and increasing pH approaching the neutral value. However, the concentration value of TSS and TDS was still above the quality standard. Initial characteristics of tofu wastewater with pH 4.6, TSS 2396.4 mg/L, and TDS 2975.1 mg/L after electrocoagulation process gained pH values 6.5, TSS 1072.7 mg/L, and TDS 2621.6 mg/L.
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Dissertations / Theses on the topic "Electrocoagulation"

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Kukunoor, Nagesh Sri. "Separation of ultrafines in dispersions using electrocoagulation." Thesis, Georgia Institute of Technology, 1990. http://hdl.handle.net/1853/11755.

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Dobson, Regina Louise. "Electrocoagulation concept for the separation of ultrafines." Thesis, Georgia Institute of Technology, 1989. http://hdl.handle.net/1853/11855.

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Gunukula, Sampath Reddy. "ELECTROCOAGULATION/FLOTATION TREATMENT OF SYNTHETIC SURFACE WATER." Cleveland State University / OhioLINK, 2011. http://rave.ohiolink.edu/etdc/view?acc_num=csu1304363574.

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Thole, Andile. "Application and evaluation of electrocoagulation techniques for the treatment of dyehouse effluents." Thesis, Cape Peninsula University of Technology, 2015. http://hdl.handle.net/20.500.11838/923.

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Thesis submitted in fulfillment of the requirements for the degree Master of Technology Chemical Engineering In the Faculty of Engineering at the Cape Peninsula University of Technology
Wet textile processing (WTP), is faced with many challenges that are related to operating costs and market competiveness. WTP uses large amounts of water and electricity, which constitute a big portion of operating costs of dyehouses and other costs are related to releasing large quantities of water, high concentrations of dyes and chemicals into the textile effluents with possible effluents discharge limits (EDL) penalty charges if EDL are exceeded. EDL penalty costs had become a normative part of the operating costs for some WTP textile factories, making the EDL penalties, a monthly cost item, because water utilities and the effluent discharge are not controlled and optimized. Cotton dyeing is a complicated chemi-physical-sorption process that is not easy to perform efficiently. Inefficient dyeing (off-shades and un-level dyeing) sometimes results in several reprocessing steps, leading to mega litres of water and chemical usage. Inefficient dyeing can also lead to higher concentrations of dyes and chemicals in the dyeing effluents. The main objectives of this study were to investigate the applicability of electrocoagulation (EC) in treatment of reactive dyes textile effluents for safe discharge into sewers or forreuse and also to evaluate EC reaction kinetics in removal of various pollutants from reactive dyes textile effluent with a batch electrocoagulation reactor (ECR). To achieve these objectives; textile effluents to be used had to be created instead of using factory effluents because textile effluents vary between dyeing batches and reaction kinetics study require constant and consistent composition of effluents. This was done by following the standard commercial sample cotton-dyeing procedures. The dyeing and pre-bleaching procedures were formulated from literature sources. The dyeing and pre-bleaching were done to create the reactive dyes textile effluents with commercial sample dyeing machines; Washtec-P and Pyrotec-MB2 at liquor ratios of 10:1 and 20:1.
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Rincon, Guillermo. "Kinetics of the electrocoagulation of oil and grease." ScholarWorks@UNO, 2011. http://scholarworks.uno.edu/td/131.

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Research on the electrocoagulation (EC) of hexane extractable materials (HEM) has been conducted at the University of New Orleans using a proprietary bench-scale EC reactor. The original reactor configuration forced the fluid to follow a vertical upward-downward path. An alternate electrode arrangement was introduced so that the path of flow became horizontal. Both configurations were evaluated by comparing the residence time distribution (RTD) data generated in each case. These data produced indication of internal recirculation and stagnant water when the fluid followed a vertical path. These anomalies were attenuated when the fluid flowed horizontally and at a velocity higher than 0.032 m s-1 . A series of EC experiments were performed using a synthetic emulsion with a HEM concentration of approximately 700 mg l-1. It was confirmed that EC of HEM follows first-order kinetics, and kinetic constants of 0.0441 s-1 and 0.0443 s-1 were obtained from applying both the dispersion and tanks-in-series (TIS) models, respectively. In both cases R2 was 0.97. Also, the TIS model indicated that each cell of the EC behaves as an independent continuous-stirred-tank reactor.
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Mechelhoff, Martin. "Electrochemical investigation of electrocoagulation reactors for water purification." Thesis, Imperial College London, 2009. http://hdl.handle.net/10044/1/8896.

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Holt, Peter Kevin. "ELECTROCOAGULATION: UNRAVELLING AND SYNTHESISING THE MECHANISMS BEHIND A WATER TREATMENT PROCESS." Thesis, The University of Sydney, 2002. http://hdl.handle.net/2123/624.

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Electrocoagulation is an empirical (and largely heuristic) water treatment technology that has had many different applications over the last century. It has proven its viability by removing a wide range of pollutants. The approach to reactor design has been haphazard, however, with little or no reference to previous designs or underlying principles. This thesis reviewed these reactor designs, identifying key commonalities and synthesising a new design hierarchy, summarised by three main decisions: 1. Batch or continuous operation; 2. Coagulation only or coagulation plus flotation reactors, and; 3. Associated separation process if required. This design decision hierarchy thereby provides a consistent basis for future electrocoagulation reactor designs. Electrochemistry, coagulation, and flotation are identified as the key foundation sciences for electrocoagulation, and the relevant mechanisms (and their interactions) are extracted and applied in an electrocoagulation context. This innovative approach was applied to a 7 L batch electrocoagulation reactor treating clay-polluted water. Structured macroscopic experiments identified current (density), time, and mixing as the key operating parameters for electrocoagulation. A dynamic mass balance was conducted over the batch reactor, for the first time, thereby enabling the extraction of a concentration profile. For this batch system, three operating stages were then identifiable: lag, reactive, and stable stages. Each stage was systematically investigated (in contrast to the previous ad hoc approach) with reference to each of the foundation sciences and the key parameters of current and time. Electrochemical behaviour characterised both coagulant and bubble generation. Polarisation experiments were used to determine the rate-limiting step at each electrode's surface. Consequently the appropriate Tafel parameters were extracted and hence the cell potential. At low currents both electrodes (anode and cathode) operated in the charge-transfer region. As the current increased, the mechanism shifted towards the diffusion-limited region, which increased the required potential. Polarisation experiments also define the operating potential at each electrode thereby enabling aluminium's dissolution behaviour to be thermodynamically characterised on potential-pH (Pourbaix) diagrams. Active and passive regions were defined and hence the aluminium's behaviour in an aqueous environment can now be predicted for electrocoagulation. Novel and detailed solution chemistry modelling of the metastable and stable aluminium species revealed the importance of oligomer formation and their rates in electrocoagulation. In particular, formation of the positively trimeric aluminium species increased solution pH (to pH 10.6), beyond the experimentally observed operable pH of 9. Thereby signifying the importance of the formation kinetics to the trimer as the active coagulant specie in electrocoagulation. Further leading insights to the changing coagulation mechanism in electrocoagulation were possible by comparison and contrast with the conventional coagulation method of alum dosing. Initially in the lag stage, little aggregation is observed until the coagulant concentration reaches a critical level. Simultaneously, the measured zeta potential increases with coagulant addition and the isoelectric point is attained in the reactive stage. Here a sorption coagulation mechanism is postulated; probably charge neutralisation, that quickly aggregates pollutant particles forming open structured aggregates as indicated by the low fractal dimension. As time progresses, pollutant concentration decreases and aluminium addition continues hence aluminium hydroxide/oxide precipitates. The bubbles gently sweep the precipitate through the solution, resulting in coagulation by an enmeshment mechanism (sweep coagulation). Consequently compact aggregates are formed, indicating by the high fractal dimension. Flotation is an inherent aspect of the batch electrocoagulation reactor via the production of electrolytic gases. In the reactor, pollutant separation occurs in situ, either by flotation or settling. From the concentration profiles extracted, original kinetic expressions were formulated to quantify these competing removal processes. As current increases, both settling and flotation rate constants increased due to the additional coagulant generation. This faster removal was offset by a decrease in the coagulant efficiency. Consequently a trade-off exists between removal time and coagulant efficiency that can be evaluated economically. A conceptual framework of electrocoagulation is developed from the synthesis of the systematic study to enable a priori prediction. This framework creates predictability for electrocoagulation, which is innovative and original for the technology. Predictability provides insights to knowledge transfer (between batch and continuous), efficient coagulant and separation path, to name just a few examples. This predictability demystifies electrocoagulation by providing a powerful design tool for the future development of scaleable, industrial electrocoagulation water treatment design and operation process.
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Perng, Yuan-Shing, and Ha-Manh Bui. "Decolorization of Reactive Red 195 solution by electrocoagulation process." Saechsische Landesbibliothek- Staats- und Universitaetsbibliothek Dresden, 2015. http://nbn-resolving.de/urn:nbn:de:bsz:14-qucosa-176597.

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In this study, the application of bipolar electrocoagulation (EC) with iron electrode has been assessed for color removal of simulated wastewater containing Reactive Red 195. The influence of initial pH, sodium sulfate concentration, initial dye concentration, electrolysis time, and electric current were examined. The optimum operational parameters were found to be pH =11, concentration of dye = 50 mg L-1, sodium sulfate concentration = 1200 mg L-1, electrolysis time = 5 min and electric current = 4 A. In such condition, color removal efficiency achieved over 99%. This result indicates that EC can be used as an efficient and “green” method for color removal from reactive dye solution
Trong nghiên cứu này, quá trình khử màu nhuộm hoạt tính (Reactive Red 195) được khảo sát bằng hệ thống keo tụ điện hóa điện cực kép, với vật liệu sắt. Các yếu tố ảnh hưởng đến quá trình khử màu như pH, nồng độ màu nhuộm, nồng độ muối Na2SO4, thời gian phản ứng và cường độ dòng được lựa chọn nghiên cứu. Kết quả cho thấy hệ thống điện hóa trên loại gần như hoàn toàn màu nhuộm với hiệu suất đạt trên 99 % tại pH 11, nồng độ màu 50 mgL-1 và nống độ muối Na2SO4 1200 mgL-1 trong khoảng thời gian 5phút. Kết quả trên cho thấy keo tụ điện hóa có thể xem là một phương pháp xử lý hiệu quả và “xanh” trong việc loại bỏ hoàn toàn màu từ nước thải nhuộm hoạt tính
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Andrade, Milton. "Heavy metal removal from bilge water by electrocoagulation treatment." ScholarWorks@UNO, 2009. http://scholarworks.uno.edu/td/1092.

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The purpose of this research was to observe the removal efficiency for copper (Cu), nickel (Ni), and zinc (Zn) using Electrocoagulation (EC) technique in a continuous flow reactor with a synthetic bilge water emulsion; and additionally, to discuss the operation cost of the treatment. The optimal configuration for EC treatment used combined electrodes, aluminum and carbon steel; flow rate of 1 L/min; effluent recycling and 7.5 amps; this optimal configuration achieved 99% of zinc removal efficiency, 70% of both, copper and nickel removal efficiency, and low operation costs. The current intensity did not have significance incidence on the removal efficiency. The analysis of cost per gram of removed contaminant indicated that nickel had an average cost of $1.95 per gram removed, zinc and copper had $0.60 and $0.88 per gram removed, respectively. To develop additional experiments with the EC reactor are required in order to optimize metal removal efficiency.
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MAMBRINI, PIERRE. "Traitement palliatif des stenoses neoplasiques oesophagiennes par sonde d'electrocoagulation bipolaire." Aix-Marseille 2, 1994. http://www.theses.fr/1994AIX20838.

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Books on the topic "Electrocoagulation"

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Systems, Inc Electro-Pure. Alternating current electrocoagulation. Cincinnati, OH: U.S. Environmental Protection Agency, Center for Environmental Research Information, 1992.

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Superfund Innovative Technology Evaluation Program (U.S.), ed. CURE electrocoagulation technology. Cincinnati, OH: U.S. Environmental Protection Agency, Office of Research and Development, 1998.

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Superfund Innovative Technology Evaluation Program (U.S.), ed. CURE electrocoagulation technology. Cincinnati, OH: U.S. Environmental Protection Agency, Office of Research and Development, 1998.

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Clifton, Farrell, Williams Tracie, and Superfund Innovative Technology Evaluation Program (U.S.), eds. Electro-pure alternating current electrocoagulation. Cincinnati, OH: U.S. Environmental Protection Agency, Superfund Innovative Technology Evaluation, 1993.

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Clifton, Farrell, Williams Tracie, and Superfund Innovative Technology Evaluation Program (U.S.), eds. Electro-pure alternating current electrocoagulation. Cincinnati, OH: U.S. Environmental Protection Agency, Superfund Innovative Technology Evaluation, 1993.

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Clifton, Farrell, Williams Tracie, and Superfund Innovative Technology Evaluation Program (U.S.), eds. Electro-pure alternating current electrocoagulation. Cincinnati, OH: U.S. Environmental Protection Agency, Superfund Innovative Technology Evaluation, 1993.

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National Risk Management Research Laboratory (U.S.) and Tetra Tech EM Inc, eds. General Environmental Corporation: CURE electrocoagulation technology. Cincinnati, Ohio: National Risk Management Research Laboratory, Office of Research and Development, U.S. Environmental Protection Agency, 1998.

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National Center for Health Services Research and Health Care Technology Assessment (U.S.), ed. Endoscopic electrocoagulation in the treatment of upper gastrointestinal bleeding. Rockville, MD: National Center for Health Services Research and Health Care Technology Assessment, U.S. Dept. of Health and Human Services, Public Health Service, 1987.

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Pacific Northwest Pollution Prevention Research Center. and Alaska. Dept. of Environmental Conservation., eds. Solids recovery from seafood processing stick water using electrocoagulation: A joint project of. Anchorage, Alaska: Alaska Department of Environmental Conservation, 1996.

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Walter, Prendiville, ed. Large loop excision of the transformation zone: A practical guide to LLETZ. London: Chapman & Hall, 1993.

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Book chapters on the topic "Electrocoagulation"

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Mondal, Sourav, Mihir Kumar Purkait, and Sirshendu De. "Electrocoagulation." In Green Chemistry and Sustainable Technology, 289–312. Singapore: Springer Singapore, 2017. http://dx.doi.org/10.1007/978-981-10-6293-3_9.

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Hmida, Emna Selmane Bel Hadj, Houyem Abderrazak, and Takoua Ounissi. "Electrocoagulation." In Clean Water: Next Generation Technologies, 227–37. Cham: Springer International Publishing, 2024. http://dx.doi.org/10.1007/978-3-031-48228-1_15.

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Yasri, Nael, Jinguang Hu, Md Golam Kibria, and Edward P. L. Roberts. "Electrocoagulation Separation Processes." In Multidisciplinary Advances in Efficient Separation Processes, 167–203. Washington, DC: American Chemical Society, 2020. http://dx.doi.org/10.1021/bk-2020-1348.ch006.

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Guevara, Héctor M., and Smarajit Roy. "Electrocoagulation Introduction and Overview." In Waste Water Recycling and Management, 217–32. Singapore: Springer Singapore, 2019. http://dx.doi.org/10.1007/978-981-13-2619-6_17.

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Liu, Huijuan, Xu Zhao, and Jiuhui Qu. "Electrocoagulation in Water Treatment." In Electrochemistry for the Environment, 245–62. New York, NY: Springer New York, 2009. http://dx.doi.org/10.1007/978-0-387-68318-8_10.

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Vong, Yunny Meas, and Darlene G. Garey. "Wastewater Treatment by Electrocoagulation." In Encyclopedia of Applied Electrochemistry, 2117–22. New York, NY: Springer New York, 2014. http://dx.doi.org/10.1007/978-1-4419-6996-5_137.

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Shammas, Nazih K., Marie-Florence Pouet, and Alain Grasmick. "Wastewater Treatment by Electrocoagulation–Flotation." In Flotation Technology, 199–220. Totowa, NJ: Humana Press, 2010. http://dx.doi.org/10.1007/978-1-60327-133-2_6.

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Gomes, Jewel Andrew, Md Islam, Paul Bernazzani, George Irwin, Dan Rutman, David Cocke, and Mohammad R. Islam. "Recapturing Metals from Electrocoagulation Floc." In Supplemental Proceedings, 203–10. Hoboken, NJ, USA: John Wiley & Sons, Inc., 2011. http://dx.doi.org/10.1002/9781118062111.ch21.

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Gomes, Jewel Andrew, Sadia Afrin Jame, Daniel Chen, Venkata Palla, Paul Bernazzani, and David Cocke. "Removal of Textile Dye Using Electrocoagulation." In EPD Congress 2011, 835–44. Hoboken, NJ, USA: John Wiley & Sons, Inc., 2012. http://dx.doi.org/10.1002/9781118495285.ch91.

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Madi-Azegagh, K., F. Aissani-Benissad, and I. Yahiaoui. "Treatment of Medical Waste Using Electrocoagulation Process." In Proceedings of the Third International Symposium on Materials and Sustainable Development, 527–39. Cham: Springer International Publishing, 2018. http://dx.doi.org/10.1007/978-3-319-89707-3_57.

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Conference papers on the topic "Electrocoagulation"

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Yerby, Cooper J., Maxime Blatter, Kenneth H. Nealson, Christos Comninellis, and Fabian Fischer. "USING LOW CURRENT DENSITY ARSENIC ELECTROCOAGULATION KINETICS TO MODEL MICROBIALLY MEDIATED ARSENIC ELECTROCOAGULATION." In GSA Annual Meeting in Indianapolis, Indiana, USA - 2018. Geological Society of America, 2018. http://dx.doi.org/10.1130/abs/2018am-321384.

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Nair, Devika S., and Sanju Sreedharan. "Reduction of Turbidity by Electrocoagulation." In Proceedings of the Advances in Technology, Engineering and Computing A Multinational Colloquium - 2017. Singapore: Research Publishing Services, 2017. http://dx.doi.org/10.3850/978-981-11-0744-3_c17-11.

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Yan-jiao Gao. "Landfill leachate treatment by electrocoagulation." In 2011 Second International Conference on Mechanic Automation and Control Engineering (MACE). IEEE, 2011. http://dx.doi.org/10.1109/mace.2011.5987671.

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Mussa, Zainab Haider, Mohamed Rozali Othman, and Md Pauzi Abdullah. "Electrocoagulation and decolorization of landfill leachate." In THE 2013 UKM FST POSTGRADUATE COLLOQUIUM: Proceedings of the Universiti Kebangsaan Malaysia, Faculty of Science and Technology 2013 Postgraduate Colloquium. AIP Publishing LLC, 2013. http://dx.doi.org/10.1063/1.4858758.

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"PERSPECTIVES OF ELECTROCOAGULATION IN WATER DISINFECTION." In International Conference on Bio-inspired Systems and Signal Processing. SciTePress - Science and and Technology Publications, 2009. http://dx.doi.org/10.5220/0001511602540258.

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"Suspended Organic Removal by Electrocoagulation Process." In International Seminar of Research Month Science and Technology in Publication, Implementation and Commercialization. Galaxy Science, 2018. http://dx.doi.org/10.11594/nstp.2018.0140.

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Simonič, Marjana. "Electrocoagulation Implementation for Textile Wastewater Treatment Processes." In International Conference on Technologies & Business Models for Circular Economy. University of Maribor Press, 2023. http://dx.doi.org/10.18690/um.fkkt.1.2023.6.

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Abstract:
Electrocoagulation (EC) has been employed recently to treat tannery, textile, and coloured wastewater. Three main processes are gathered in EC process, namely electrochemistry, coagulation, and flotation. This technique uses DC currents source between metal electrodes immersed in the textile effluent, which causes the dissolution of electrode plates into the effluent. The main advantage of EC compared to chemical coagulation technique is that EC generates less sludge. The objective of the present manuscript is to review the potential of electrocoagulation for the treatment of textile effluent. The most influential factors on removal efficiency, such as initial pH, time of EC, conductivity, current density, initial dye concentration and periodically reversal current on electrodes were discussed. Considering the circular economy concept, which focuses on positive society-wide benefits, manufacturing brick or ceramic materials is feasible method for disposing sludge.
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Zhian, Hassan. "FILTERING WASTEWATER INDUSTRIAL USING OF ELECTROCOAGULATION METHOD." In SGEM2011 11th International Multidisciplinary Scientific GeoConference and EXPO. Stef92 Technology, 2011. http://dx.doi.org/10.5593/sgem2011/s20.128.

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Elawwad, Abdelsalam, and Ahmed Hamdy. "Removal of Cyanide from Wastewater Using Electrocoagulation." In The 6th World Congress on Civil, Structural, and Environmental Engineering. Avestia Publishing, 2021. http://dx.doi.org/10.11159/iceptp21.lx.110.

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Hajar, Ibnu, Fadarina, Mustain Zamhari, and Selastia Yuliati. "Tofu Industrial Wastewater Treatment by Electrocoagulation Method." In 4th Forum in Research, Science, and Technology (FIRST-T1-T2-2020). Paris, France: Atlantis Press, 2021. http://dx.doi.org/10.2991/ahe.k.210205.008.

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Reports on the topic "Electrocoagulation"

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Domini, J. C., J. Kan, J. Szynkarczuk, T. A. Hassan, and K L Kar. The cost of electrocoagulation. Natural Resources Canada/ESS/Scientific and Technical Publishing Services, 1993. http://dx.doi.org/10.4095/305311.

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Mickley, Michael. Pretreatment Capabilities and Benefits of Electrocoagulation. Fort Belvoir, VA: Defense Technical Information Center, December 2004. http://dx.doi.org/10.21236/ada433998.

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Tuggle, K., M. Humenick, and F. Barker. Treatment of produced waters by electrocoagulation and reverse osmosis. Office of Scientific and Technical Information (OSTI), August 1992. http://dx.doi.org/10.2172/10187607.

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Angle, C. W., and J. C. Donini. Electrokinetics of samples treated by electrocoagulation methods - part 1. concentrated dispersions of clay particles. Natural Resources Canada/ESS/Scientific and Technical Publishing Services, 1992. http://dx.doi.org/10.4095/305297.

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PETERSEN SW. TREATABILITY TEST REPORT FOR THE REMOVAL OF CHROMIUM FROM GROUNDWATER AT 100-D AREA USING ELECTROCOAGULATION. Office of Scientific and Technical Information (OSTI), September 2009. http://dx.doi.org/10.2172/966148.

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