DOCSLIB.ORG

General Environmental Corporation CURE Electrocoagulation Technology

Total Page：16

File Type：pdf, Size：1020Kb

Download full-text PDF Read full-text
General Environmental Corporation CURE Electrocoagulation Technology EPA/540/R-96/502 September 1998 General Environmental Corporation CURE Electrocoagulation Technology Innovative Technology Evaluation Report National Risk Management Research Laboratory Office of Research and Development U.S. Environmental Protection Agency Cincinnati, Ohio 45268 @ Printed on Recycled Paper Notice The information in this document has been funded by the U. S. Environmental Protection Agency (EPA) under Contract No. 68425-0037 to Tetra Tech EM Inc. (formerly PRC Environmental Management, Inc.). It has been subjected to the Agency’s peer and administrative reviews and has been approved for publication as an EPA document. Mention of trade names or commercial products does not constitute an endorsement or recommendation for use. ii Foreword The U. S. Environmental Protection Agency (EPA) is charged by Congress with protecting the Nation’s land, air, and water resources. Under a mandate of national environmental laws, the Agency strives to formulate and implement actions leading to a compatible balance between human activities and the ability of natural systems to nurture life. To meet this mandate, EPA’s research program is providing data and technical support for solving environmental problems today and building a science knowledge base necessary to manage our ecological resources wisely, understand how pollutants affect our health, and prevent or reduce environmental risks in the future. The National Risk Management Research Laboratory is the Agency’s center for investigation of technological and management approaches for reducing risks from threats to human health and the environment. The focus of the Laboratory’s research program is on methods for the prevention and control of pollution to air, land, water and subsurface resources; protection of water quality in public water systems; remediation of contaminated sites and groundwater; and prevention and control of indoor air pollution. The goal of this research effort is to catalyze development and implementation of innovative, cost-effective environmental technologies; develop scientific and engineering information needed by EPA to support regulatory and policy decisions; and provide technical support and information transfer to ensure effective implementation of environmental regulations and strategies. This publication has been produced as part of the Laboratory’s strategic long-term research plan. It is published and made available by EPA’s Office of Research and Development to assist the user community and to link researchers with their clients. E. Timothy Oppelt, Director National Risk Management Research Laboratory . Ill Abstract The CURE electrocoagulation system was evaluated for removal of low levels of the radionuclides uranium, plutonium, and americium as well as other contaminants in wastewater. Economic data from the Superfund Innovative Technology Evaluation (SITE) demonstration are also presented, and the technology is compared to the nine criteria that the U. S. Environmental Protection Agency (EPA) uses to select remedial alternatives for Super-fund sites. The CURE electrocoagulation technology was developed by General Environmental Corporation, Inc. (GEC), of Denver, Colorado. The technology induces the coagulation and precipitation of contaminants by a direct-current electrolytic process followed by settling with or without the addition of coagulation-inducing chemicals. Treated water is discharged from the system for reuse, disposal, or reinjection. Concentrated contaminants in the form of sludge are placed in drums for disposal or reclamation. The CURE technology was demonstrated under the SITE Program at the U.S. Department of Energy’s (DOE) Rocky Flats Environmental Technology Site (formerly the Rocky Flats Plant) near Golden, Colorado. Approximately 4,500 gallons of wastewater containing low levels of the radionuclides uranium, plutonium, and americium were treated in August and September 1995. Water from the solar evaporation ponds was used in the demonstration. Six preruns, five optimization runs, and four demonstration runs were conducted over a 54-day period. The demonstration runs lasted 5.5 to 6 hours each, operating the CURE system at approximately 3 gallons per minute. Filling the clarifier took approximately 2.5 hours of this time. Once the clarifier was filled, untreated influent, and effluent from the clarifier were collected every 20 minutes for 3 hours. Because of the shortened run times, there is uncertainty whether the data represent long-term operating conditions. Results indicated that removal efficiencies for the four runs ranged from 32 to 52 percent for uranium, 63 to 99 percent for plutonium, and 69 to 99 percent for americium. Colorado Water Quality Control Commission (CWQCC) standards were met for plutonium and americium in some, but not all cases. However, CWQCC standards for uranium were not met. Arsenic and calcium concentrations were also decreased by an average of 74 and 50 percent, respectively for the two runs for which metals were measured. Evaluation of the CURE electrocoagulation technology against the nine criteria used by the EPA in evaluating potential remediation alternatives indicates that the CURE system provides both long- and short-term protection of the environment, reduces contaminant mobility and volume, and presents few risks to the community or the environment. Potential sites for applying this technology include Superfund, DOE, U.S. Department of Defense, and other hazardous waste sites where water is contaminated with radionuclides or metals. Economic analysis indicates that remediation cost for a lOO- gallon-per-minute CURE system could range from about $0.003 to $0.009 per gallon, depending on the duration of the remedial action. iv Contents List of Figures and Tables ........................................................................................................................... viii Acronyms, Abbreviations, and Symbols ....................................................................................................... ix Conversion Factors ........................................................................................................................................ xi Acknowledgments.. ....................................................................................................................................... xii Executive Summary ........................................................................................................................................ 1 1 Introduction ............................................................................................................................................. 3 1.1 Background ....................................................................................................................................... 3 1.2 Brief Description of the SITE Program and Reports ...................................................................... 3 1.3 Purpose of the Innovative Technology Evaluation Report.............................................................. 4 1.4 Technology Description ................................................................................................................... 4 1.4.1 Theory of Coagulation ....................................................................................................... 5 1.4.2 Theory of Electrocoagulation ............................................................................................ 5 1.4.3 System Components and Function .................................................................................... 6 1.5 Key Contacts..................................................................................................................................... 8 2 Technology Applications Analysis ......................................................................................................... 9 2.1 Key Features of the CURE Electrocoagulation Technology ........................................................... 9 2.2 Technology Performance .................................................................................................................. 9 2.2.1 Historical Performance ...................................................................................................... 9 2.2.2 Bench-Scale Study Results .............................................................................................. 10 2.2.3 SITE Demonstration Results ........................................................................................... 10 2.3 Evaluation of Technology Against RI/FS Criteria ........................................................................ 11 2.4 Factors Influencing Performance ................................................................................................... 11 2.4.1 Influent Water Chemistry ................................................................................................ 11 2.4.2 Operating Parameters ...................................................................................................... 11 2.4.3 Maintenance of Equipment ............................................................................................. 11 2.5 Applicable Wastes .......................................................................................................................... 11 2.6 Site Requirements............................................................................................................................ 11 2.7 Materials Handling Requirements
Load more

Recommended publications
  • Electrocoagulation Pretreatment for Microfiltration: an Innovative Combination to Enhance Water Quality and Reduce Fouling in Integrated Membrane Systems
    Desalination and Water Purification Research and Development Report No. 139 Electrocoagulation Pretreatment for Microfiltration: An Innovative Combination to Enhance Water Quality and Reduce Fouling in Integrated Membrane Systems University of Houston U.S. Department of the Interior Bureau of Reclamation Technical Service Center Denver, Colorado September 2007 Form Approved REPORT DOCUMENTATION PAGE OMB No. 0704-0188 The public reporting burden for this collection of information is estimated to average 1 hour per response, including the time for reviewing instructions, searching existing data sources, gathering and maintaining the data needed, and completing and reviewing the collection of information. Send comments regarding this burden estimate or any other aspect of this collection of information, including suggestions for reducing the burden, to Department of Defense, Washington Headquarters Services, Directorate for Information Operations and Reports (0704-0188), 1215 Jefferson Davis Highway, Suite 1204, Arlington, VA 22202-4302. Respondents should be aware that notwithstanding any other provision of law, no person shall be subject to any penalty for failing to comply with a collection of information if it does not display a currently valid OMB control number. PLEASE DO NOT RETURN YOUR FORM TO THE ABOVE ADDRESS. 2. REPORT TYPE 1. REPORT DATE (DD-MM-YYYY) 3. DATES COVERED (From - To) Final September 2007 October 2005 – September 2007 4. TITLE AND SUBTITLE 5a. CONTRACT NUMBER Electrocoagulation Pretreatment for Microfiltration: An Innovative Combination Agreement No. 05-FC-81-1172 to Enhance Water Quality and Reduce Fouling in Integrated Membrane Systems 5b. GRANT NUMBER 5c. PROGRAM ELEMENT NUMBER 6. AUTHOR(S) 5d. PROJECT NUMBER Shankar Chellam, Principal Investigator Dennis A.
    [Show full text]
  • Overview of the Technology 2 2 2. Electrocoagulation
    1. ELECTROCOAGULATION – OVERVIEW OF THE TECHNOLOGY 2 1.1 Coagulation 2 1.2 Electrocoagulation - the process 2 2. ELECTROCOAGULATION (EC) – ADVANTAGES OF THE SYSTEM 3 2.1 Applications 4 2.2 Benefits of the technology 5 3. EXAMPLES OF PERCENTAGE REMOVAL RATES ACHIEVED IN VARIOUS ELECTROCOAGULATION TRIALS 5 3.1Treatment of abattoir processing line wastewater and stick water (wastewater from a low temperature rendering plant) 5 3.2 Copper products manufacturer 6 3.3 Nickel smelter 6 3.4 Concentrated wastewater from tannery 7 3.5 Concentrations of ions in a wastewater before and after electrocoagulation 7 4 OPERATING PROCEDURES AND COST 7 5 CONCLUSIONS 8 6 CONTACTS 8 1 Electrocoagulation – overview of the technology 1.1Coagulation Coagulation is one of the important methods used in water treatment. It is a process used to cause the destabilization and subsequent aggregation of smaller particles into larger complexes. Water contaminants such as ions (heavy metals) and colloids (organic and inorganic) are primarily held in solution by electrical charges. In 1882 Schulze showed that colloidal systems could be destabilised by the addition of ions of the charge opposite to that of the colloid (Benefield et al, 1982), The destabilized colloids can then aggregate and subsequently be separated from the wastewater. Coagulation can be achieved by both the chemical or electrical means. Chemical coagulation has been used for decades to destabilize suspensions and to effect precipitation of soluble species and other pollutants from aqueous streams. Alum, lime and polymers are some of the chemical coagulants used. These processes, however, tend to generate large volumes of sludge with high bound water content which can be difficult to separate and dewater.
    [Show full text]
  • Electrocoagulation Followed by Ion Exchange Or Membrane Separation Techniques for Recycle of Textile Wastewater
    Open Access Advance Research in Textile Engineering Review Article Electrocoagulation Followed by Ion Exchange or Membrane Separation Techniques for Recycle of Textile Wastewater Arega Y and Chavan RB* Ethiopian Institute of Textile Garment and Fashion Abstract Technology, Bahir Dar University, Ethiopia Traditionally, physical, biological, chemical coagulation, adsorption and *Corresponding author: Chavan RB, Ethiopian advanced oxidation processes are used for the treatment of textile wastewater Institute of Textile Garment and Fashion Technology, and dye removal. Many of these processes are not cost effective and are Bahir Dar University, Bahir Dar, Ethiopia responsible for secondary pollution. Electrocoagulation (EC) has recently attracted the attention as a potential technique for treating textile and other Received: January 22, 2018; Accepted: February 28, industrial effluents due to its versatility, cost effectiveness and environmental 2018; Published: March 08, 2018 compatibility. In this paper an attempt has been made to discuss history, basic principle, mechanism, advantages, and disadvantages, effect of various parameters on the process efficiency and applications of electrocoagulation. The aim of this paper is not to review the electrocoagulation process as several comprehensive reviews have been published covering different aspects of EC applications. Most of the information available in the literature is based on the use of batch flow reactor using Electrocoagulation (EC) process alone to treat the textile wastewater to a level that meets the discharge standards. The focus of the present paper is to throw light on the combined electrocoagulation–ion exchange and combined electrocoagulation-membrane separation processes for the recycling of textile wastewater. Though the combined processes discussed in the present paper are at the conceptual stage, they have the potentials for scaling up to a commercial level.
    [Show full text]
  • Electrocoagulation Treatment for Removal of Color and Chemical Oxygen Demand in Landfill Leachate Using Aluminum Electrode
    International Journal of Recent Technology and Engineering (IJRTE) ISSN: 2277-3878, Volume-8 Issue-4, November 2019 Electrocoagulation Treatment for Removal of Color and Chemical Oxygen Demand in Landfill Leachate using Aluminum Electrode Bharath M, Krishna B M, Shiva Kumar B P Abstract: The present research work mainly deals with the classification and characterization of landfill leachate removal percentage of Color and Chemical Oxygen Demand based on age are depicted in Table 1. Based on the literature (COD) on landfill leachate by using electrocoagulation (EC) survey, some of the treatment methods such as process. An EC process was carried out with an aluminium electrode and it act as both anode and cathode. The study mainly coagulation-flocculation [1], membrane processes [2-3] targets the factors affecting on electrode material, electrolysis activated carbon adsorption [4]. combined time, initial pH, applied voltage, inter-electrode distance. The physicochemical-nanofiltration [5]. biological treatment [6]. experimental result reveals that there was raise in BOD/COD have been reported in the literature. Electrocoagulation (EC) ratio from 0.11 to 0.66 and the maximum percentage removal process treating various types of wastewater, for example achieved were COD and Color 78.4% and 77.0% respectively. electroplating wastewater [7], Distillery wastewater [8] [9], The optimum inter-electrode distance 1cm with electrode surface area 35 cm2 and optimum electrolysis time of 90 min at optimum Dairy wastewater [10]. The main importance of research applied voltage 10V, stirring speed 250 rpm and pH is 9.3. These work is to optimize the parameters like initial pH, results showed that the EC process is appropriate and electrolysis time, current density, inter-electrode distance on well-organized approach for the landfill leachate treatment.
    [Show full text]
  • Application of Electrocoagulation and Electrolysis on the Precipitation of Heavy Metals and Particulate Solids in Washwater from the Soil Washing
    Journal of Agricultural Chemistry and Environment, 2014, 3, 130-138 Published Online November 2014 in SciRes. http://www.scirp.org/journal/jacen http://dx.doi.org/10.4236/jacen.2014.34015 Application of Electrocoagulation and Electrolysis on the Precipitation of Heavy Metals and Particulate Solids in Washwater from the Soil Washing Ho Y. Shim, Kyo S. Lee, Dong S. Lee, Dae S. Jeon, Mi S. Park, Ji S. Shin, Yun K. Lee, Ji W. Goo, Soo B. Kim, Doug Y. Chung* Department of Bio-Environmental Chemistry, College of Agriculture and Life Science, Chungnam National University, Daejeon, Korea Email: *[email protected] Received 28 August 2014; revised 29 September 2014; accepted 7 October 2014 Copyright © 2014 by authors and Scientific Research Publishing Inc. This work is licensed under the Creative Commons Attribution International License (CC BY). http://creativecommons.org/licenses/by/4.0/ Abstract Soil washing, ex situ mechanical technique, is one of the few permanent treatment alternatives to remove metal contaminants from soils by employing physical separation based on mineral pro- cessing technologies to remove discrete particles or metal-bearing particles and/or chemical ex- traction based on leaching or dissolving process to extract the metals from the soils into an aqueous solution. However, washwater remained from soil washing process contains discrete particulate particles along with heavy metals as solution phase to be treated separately, as well as this pro- cess can produce large amount of sludge that requires further treatment, slow metal precipitation, poor settling, the aggregation of metal precipitates. Electrical treatments including electrocoagu- lation and electrolysis can be effective in removing these substances from washwater.
    [Show full text]
  • Chemical Or Electrochemical Techniques, Followed by Ion Exchange, for Recycle of Textile Dye Wastewater S
    Journal of Hazardous Materials 149 (2007) 324–330 Chemical or electrochemical techniques, followed by ion exchange, for recycle of textile dye wastewater S. Raghu, C. Ahmed Basha ∗ Central Electrochemical Research Institute, Karaikudi 630 006, Tamilnadu, India Received 13 December 2006; received in revised form 30 March 2007; accepted 30 March 2007 Available online 8 April 2007 Abstract This paper examines the use of chemical or electrocoagulation treatment process followed by ion-exchange process of the textile dye effluent. The dye effluent was treated using polymeric coagulant (cationic dye-fixing agent) or electrocoagulation (iron and aluminum electrode) process under various conditions such as various current densities and effect of pH. Efficiencies of COD reduction, colour removal and power consumption were studied for each process. The chemical or electrochemical treatment are indented primarily to remove colour and COD of wastewater while ion exchange is used to further improve the removal efficiency of the colour, COD, Fe concentration, conductivity, alkalinity and total dissolved solids (TDS). From the results chemical coagulation, maximum COD reduction of about 81.3% was obtained at 300 mg/l of coagulant whereas in electrocoagulation process, maximum COD removal of about 92.31% (0.25 A/dm2) was achieved with energy consumption of about 19.29 kWh/kg of COD and 80% (1 A/dm2) COD removal was obtained with energy consumption of about 130.095 kWh/kg of COD at iron and aluminum electrodes, respectively. All the experimental results, throughout the present study, have indicated that chemical or electrocoagulation treatment followed by ion-exchange methods were very effective and were capable of elevating quality of the treated wastewater effluent to the reuse standard of the textile industry.
    [Show full text]
  • Electrocoagulation
    Proceedings of Western Dredging Association and Texas A&M University Center for Dredging Studies' "Dredging Summit and Expo 2015" ELECTROCOAGULATION (EC) AND CHITOSAN ENHANCED SAND FILTRATION (CESF) TREATMENT TECHNOLOGIES FOR DREDGE RETURN WATER: TWO CASE STUDIES ON THE LOWER DUWAMISH WATERWAY IN SEATTLE, WASHINGTON L.M. Doty1 ABSTRACT Thirteen years ago, the Lower Duwamish Waterway in Seattle, Washington was designated as a superfund site due to contamination with heavy metals, PCBs/cPAHs, and dioxins/furans, the result of heavy industrial use in the area over the last century. Comprehensive clean-up is still a few years out, however the Environmental Protection Agency (EPA) designated 29 acres of “hot spots” that posed enough threat to human and environmental health to warrant Early Action. Two specific Early Action Areas (EAA) conducted environmental dredging activities from 2013 to 2014. Due to contamination levels, specifically heavy metals and PCBs, traditional methods of on-barge dewatering were not allowed. Site 1 had limited upland real estate and implemented an Electrocoagulation (EC) treatment train. Geotubes with polymers, an established dewatering technique, was considered for Site 1, however potential toxicity of the polymers and lack of sufficient real estate made this option unfeasible. Site 2 had no upland real estate and deployed a barge mounted Chitosan Enhanced Sand Filtration (CESF) system. Both the EC and CESF treatment technologies carry a General Use Level Designation (GULD) granted by the Washington State Department of Ecology for turbidity removal on construction sites. The GULD status of these technologies helped streamline the permitting approval process. Site 1 operated for 48 days without any water violations, discharging 6,300,000 gallons of treated water back to the Duwamish River.
    [Show full text]
  • Electrocoagulation
    Electrocoagulation Achieving clean, clear, treated and reusable water: The process, technology and benefits. WWW.AWWTCORP.COM CALL US (631) 213-1324 12 SEWAGE WASTE Clean water is vital to virtually all living things on oxygen back in is also necessary for the proper this planet. While nature has the remarkable ability treatment of wastewater. to cope with small amounts of water wastes and pollution, it would be overwhelmed if we didn’t treat A more detailed process of this method includes the billions of gallons of wastewater and sewage screening, pumping, aerating, removal of sludge, produced every day before releasing it back to the and the killing of bacteria 2. The most common environment. Water treatment facilities serve to means of killing bacteria in wastewater quite often reduce the level of pollutants in wastewater. involves using chemicals, which are sometimes Further, with the capacity and abundance of clean toxic. While this represents the primary method in water shrinking on a global scale due to various treating wastewater, new technological factors such as drought and pollution, the advancements in this field have made the process importance of advancing new techniques and more cost effective and more efficient than ever methodologies in water treatment has never been before. more critical than it is today. This white paper will provide a discussion about According to the USGS (the U.S. Geological Survey), what Electrocoagulation is, the process of how it the major aim of sewage treatment is to remove as works and the technology behind it. Additionally, much of the suspended solids as possible before the this paper will discuss the various benefits in remaining water, called effluent, is discharged back utilizing this form of water treatment option.
    [Show full text]
  • Electrocoagulation Treatment of Real Mining Waters and Solid-Liquid Separation of Solids Formed
    Lappeenranta, Finland Mine Water and Circular Economy IMWA 2017 Electrocoagulation treatment of real mining waters and solid-liquid separation of solids formed Maria A. Mamelkina1, Ritva Tuunila1, Mika Sillänpää1,2, Antti Häkkinen1 1 LUT School of Engineering Science, Lappeenranta University of Technology, P.O.Box 20 FI-53851, Lappeenranta, Finland 2 Florida International University, Department of Civil and Environmental Engineering Abstract This research was aimed at studying the possibility of mining water treatment using electrocoagulation and pressure filtration. Batch experiments took place at 1L and 70L reactors. Filtration properties of the slurries were studied using a laboratory scale Nutsche filter. The highest sulfate removal was obtained using Al electrodes after 5h treatment, while for nitrate after 3h. Most metals were removed almost completely after 1h. Cake formed during filtration had high porosity and moisture content. It is worth mentioning that not only the treatment of waters, but also residue processing is an important issue once talking about sustainable water treatment technologies. Introduction Electrocoagulation finds its wide application for treatment of wastewaters generated during tannery, electroplating, diary and textile processes (Chen 2004). Electrocoagulation (EC) en- ables efficient treatment of wastewater containing metals, anionic contaminants, foodstuff, organic matter, polymeric wastes, oil wastes, textile dyes, lignin, chemical and mechanical pol- ishing wastes, phenolic wastes and aqueous suspensions containing ultrafine particles (Emam- jomeh 2009;Lacasa 2011). Currently, with the successful application of electrocoagulation in different fields a rising interest is given to it as a possible technique for treatment of mining waters containing sulfate, nitrate, cyanide, various metals and other harmful contaminants. EC can be classified as an active, abiotic water treatment technique.
    [Show full text]
  • Application of Electrocoagulation with a New Steel-Swarf-Based Electrode for the Removal of Heavy Metals and Total Coliforms from Sanitary Landfill Leachate
    applied sciences Article Application of Electrocoagulation with a New Steel-Swarf-Based Electrode for the Removal of Heavy Metals and Total Coliforms from Sanitary Landfill Leachate Mayk Teles de Oliveira 1 , Ieda Maria Sapateiro Torres 1, Humberto Ruggeri 2, Paulo Scalize 2 , Antonio Albuquerque 3,* and Eric de Souza Gil 1 1 Faculty of Pharmacy, Federal University of Goiás, Goiânia 74605-170, Brazil; [email protected] (M.T.d.O.); [email protected] (I.M.S.T.); [email protected] (E.d.S.G.) 2 School of Civil and Environmental Engineering, Federal University of Goiás, Goiânia 74605-170, Brazil; [email protected] (H.R.); [email protected] (P.S.) 3 Department of Civil Engineering and Architecture, FibEnTech, GeoBioTec, University of Beira Interior, 6200-358 Covilhã, Portugal * Correspondence: [email protected] Featured Application: A new and innovative steel-swarf-based electrode is proposed for the re- moval of heavy metal and total coliforms in sanitary landfill leachate. Abstract: Sanitary landfill leachate (LL) composition varies according to climate variables variation, Citation: de Oliveira, M.T.; Torres, solid waste characteristics and composition, and landfill age. Leachate treatment is essentially carried I.M.S.; Ruggeri, H.; Scalize, P.; out trough biological and physicochemical processes, which have showed variability in efficiency Albuquerque, A.; Gil, E.d.S. and appear a costly solution for the management authorities. Electrocoagulation (EC) seems a Application of Electrocoagulation suitable solution for leachate treatment taking into account the characteristics of the liquor. One with a New Steel-Swarf-Based Electrode for the Removal of Heavy of the problems of EC is the electrode passivation, which affects the longevity of the process.
    [Show full text]
  • Electrocoagulation: a Promising Method to Treat and Reuse Mineral Processing Wastewater with High COD
    water Article Electrocoagulation: A Promising Method to Treat and Reuse Mineral Processing Wastewater with High COD Gaogui Jing 1,2, Shuai Ren 1,2, Yuesheng Gao 3 , Wei Sun 1,2 and Zhiyong Gao 1,2,* 1 School of Minerals Processing and Bioengineering, Central South University, Changsha 410083, China; [email protected] (G.J.); [email protected] (S.R.); [email protected] (W.S.) 2 Key Laboratory of Hunan Province for Clean and Efficient Utilization of Strategic Calcium-Containing Mineral Resources, Central South University, Changsha 410083, China 3 Department of Chemical Engineering, Michigan Technological University, Houghton, MI 49931, USA; [email protected] * Correspondence: [email protected] Received: 23 January 2020; Accepted: 18 February 2020; Published: 21 February 2020 Abstract: Mineral processing wastewater contains large amounts of reagents which can lead to severe environmental problems, such as high chemical oxygen demand (COD). Inspired by the wastewater treatment in such industries as those of textiles, food, and petrochemistry, in the present work, electrocoagulation (EC) is applied for the first time to explore its feasibility in the treatment of wastewater with an initial COD of 424.29 mg/L from a Pb/Zn sulfide mineral flotation plant and its effect on water reuse. Typical parameters, such as anode materials, current density, initial pH, and additives, were characterized to evaluate the performance of the EC method. The results showed that, under optimal conditions, i.e., iron anode, pH 7.1, electrolysis time 70 min, 19.23 mA/cm2 current density, and 4.1 g/L activated carbon, the initial COD can be reduced to 72.9 mg/L, corresponding to a removal rate of 82.8%.
    [Show full text]
  • Thesis Development of an Electrocoagulation Based
    THESIS DEVELOPMENT OF AN ELECTROCOAGULATION BASED TREATMENT TRAIN FOR PRODUCED WATER WITH HIGH CONCENTRATIONS OF ORGANIC MATTER Submitted by Richard Andrew Caschette Department of Civil and Environmental Engineering In partial fulfillment of the requirements For the Degree of Master of Science Colorado State University Fort Collins, Colorado Fall 2016 Master’s Committee: Advisor: Kenneth Carlson Sybil Sharvelle Tom Bradley Copyright by Richard Andrew Caschette 2016 All Rights Reserved ABSTRACT DEVELOPMENT OF AN ELECTROCOAGULATION BASED TREATMENT TRAIN FOR PRODUCED WATER WITH HIGH CONCENTRATIONS OF ORGANIC MATTER Well stimulation in the form of hydraulic fracturing has made unconventional oil and gas extraction economically feasible, significantly increasing the number of producing oil and gas wells in the United States in the last several decades. Both the hydraulic fracturing process and shale play development has created a large amount of oil and gas associated wastewater. Deep well injection or disposal wells are the preferred and most widely used method for managing produced water. This industry standard both eliminates valuable water resources from the hydrologic cycle and can be linked to the increasing frequency of seismic events in parts of the United States. This paper investigates water treatment processes in the context of beneficial reuse towards irrigation. Treating produced water on well pad locations followed by agricultural use within close proximity minimizes trucking costs and environmental impacts as well as recycles industrial wastewater back into the hydrologic cycle. High concentrations of salts and organic matter must be removed in addition to other contaminants (Benzene, Boron, Calcium, and Magnesium) from produced water collected from Noble Energy's Wells Ranch Central Processing Facility (CPF) before being applied towards a secondary use.
    [Show full text]