Is the Microfiltration Process Suitable As a Method of Removing
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Hauser-Solids.Pdf
l'llAl lllAL MANUAL UI WA'ilLWA IUll I lllMltJ lllY pro<lu ing a truly curvc<l slope (which the graphing prm;edurc attempts to fore(.) into a straightc line). If the sample to be tested is out of range of the standard concentrations normally used forthe test, it is better to dilute the sample than to raise the standard concentrations. • Solids Solids in water are defined as any matter that remains as residue upon evaporation and drying at 103 degrees Celsius. They are separated into two classes: suspended and dissolved. Total Solids = Suspended Solids + Dissolved Solids ( nonfil terable residue) (filterable residue) Each of these has Volatile (organic) and Fixed (inorganic) components which can be separated by burning in a muffle furnace at 550 degrees Celsius. The organic components are converted to carbon dioxide and water, and the ash is left. Weight of the volatile solids can be calculated by subtracting the ash weight from the total dry weight of the solids. DOMESTIC WASTEWATER t 999,000 mg/L Total Solids 1,000 mg/L 41 •! :/.========== l 'l\AI lltAI MANUAi tJ I WA llWAlll\tt!I MI 11\Y •I Total Suspended Solids/Volatile Solids treatment (adequate aeration, proper F/M & MCRT, good return wasting rates) , and the settling capacity of the secondary sludge. Excessivl:and The Total Suspended Solids test is extremely valuable in the analysis of polluted suspended solids in final effluent will adversely affect disinfection capacity . waters. It is one of the two parameters which has federal discharge limits at 30 Volatile component of final effluent suspended solids is also monitored. -
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. -
“Some Things Just DON't Belo
Wilson, NC 27894 Box 10 P.O. Reclamation Facility Water City of Wilson and Treatment System Report System Treatment and Wastewater Collection Wastewater City of Wilson Fiscal Year 2017-2018 Year Fiscal “Some Things Just DON’T Belong in the Toilet” Toilets are meant for one activity, and you know what we’re talking about! When The following is a partial list of items that the wrong thing is flushed, results can include costly backups on your own prop- should not be flushed: erty or problems in the City’s sewer collection system, and at the wastewater 6 Baby wipes, diapers treatment plant. That’s why it is so important to treat toilets properly and flush 6 Cigarette butts only your personal contributions to the City’s wastewater system. 6 Rags and towels 6 Cotton swabs, medicated wipes (all brands) “Disposable Does Not Mean Flushable” 6 Syringes Flushing paper towels and other garbage down the toilet wastes water and can 6 Candy and other food wrappers create sewer backups and SSOs. The related costs associated with these SSOs can 6 Clothing labels be passed on to ratepayers. Even if the label reads “flushable”, you are still safer 6 Cleaning sponges and more environmentally correct to place the item in a trash can. 6 Toys 6 Plastic items 6 Aquarium gravel or kitty litter 6 Rubber items such as latex gloves 6 Sanitary napkins “It’s a Toilet, 6 Hair 6 Underwear 6 Disposable toilet brushes NOT 6 Tissues (nose tissues, all brands) 6 Egg shells, nutshells, coffee grounds a Trash Can!” 6 Food scraps 6 Oil 6 Grease 6 Medicines Wilson, NC 27894 Box 10 P.O. -
Microfiltration of Cutting-Oil Emulsions Enhanced by Electrocoagulation
This article was downloaded by: [Faculty of Chemical Eng & Tech], [Krešimir Košutić] On: 30 April 2015, At: 03:13 Publisher: Taylor & Francis Informa Ltd Registered in England and Wales Registered Number: 1072954 Registered office: Mortimer House, 37-41 Mortimer Street, London W1T 3JH, UK Desalination and Water Treatment Publication details, including instructions for authors and subscription information: http://www.tandfonline.com/loi/tdwt20 Microfiltration of cutting-oil emulsions enhanced by electrocoagulation b a a b Janja Križan Milić , Emil Dražević , Krešimir Košutić & Marjana Simonič a Faculty of Chemical Engineering and Technology, Department of Physical Chemistry, University of Zagreb, Marulićev trg 19, HR-10000 Zagreb, Croatia, Tel. +385 1 459 7240 b Faculty of Chemistry and Chemical Engineering, Laboratory for Water Treatment, University of Maribor, Smetanova 17, SI-2000 Maribor, Slovenia Published online: 30 Apr 2015. Click for updates To cite this article: Janja Križan Milić, Emil Dražević, Krešimir Košutić & Marjana Simonič (2015): Microfiltration of cutting-oil emulsions enhanced by electrocoagulation, Desalination and Water Treatment, DOI: 10.1080/19443994.2015.1042067 To link to this article: http://dx.doi.org/10.1080/19443994.2015.1042067 PLEASE SCROLL DOWN FOR ARTICLE Taylor & Francis makes every effort to ensure the accuracy of all the information (the “Content”) contained in the publications on our platform. However, Taylor & Francis, our agents, and our licensors make no representations or warranties whatsoever as to the accuracy, completeness, or suitability for any purpose of the Content. Any opinions and views expressed in this publication are the opinions and views of the authors, and are not the views of or endorsed by Taylor & Francis. -
Monitoring Microfiltration Processes for Water Treatment Quantifying Nanoparticle Concentration and Size to Optimize Filtration Processes
APPLICATION NOTE Monitoring Microfiltration Processes for Water Treatment Quantifying Nanoparticle Concentration and Size to Optimize Filtration Processes PARTICLE Introduction CONCENTRATION With the increasing demands on water supplies and tighter regulations, much PARTICLE SIZE research is being done in to water treatment processes. Subjects of study include improving processes to allow treated water to be used in secondary applications, optimizing filtration processes to remove biological contaminants and reduce membrane fouling, monitoring filter breakthrough to minimize maintenance requirements or contamination, and verifying ability to remove the increasing load of nano-particulates in the waste water stream. Due to the massive quantities processed, even small improvements in process performance and efficiency have a large impact on resulting water quality and energy consumption. Numerous technologies exist for monitoring particle size and concentration in the micron size range, but Nanoparticle Tracking Analysis (NTA) is a unique technology that provides greater insight into the sub-micron size range that is so important to many of these advanced water treatment processes. Detecting and Counting Particles Both Dynamic Light Scattering (DLS) and NTA measure the Brownian motion of nanoparticles whose speed of motion, or diffusion coefficient (Dt), is related to particle size through the Stokes-Einstein equation. In NTA, laser light scatters from particles in suspension and a video camera captures the images of those particles moving under Brownian motion. By tracking and quantifying the particles’ diffusion, the particle diameter can be determined through the Stokes-Einstein equation. The direct view of the Malvern Instruments Worldwide Sales and service centres in over 65 countries www.malvern.com/contact ©2016 Malvern Instruments Limited APPLICATION NOTE sample also allows visual inspection of the sample for an additional qualitative confirmation. -
Mitigation of Membrane Fouling in Microfiltration
MITIGATION OF MEMBRANE FOULING IN MICROFILTRATION & ULTRAFILTRATION OF ACTIVATED SLUDGE EFFLUENT FOR WATER REUSE A thesis submitted in fulfilment of the requirement for the degree of Doctor of Philosophy (PhD) Sy Thuy Nguyen Bachelor of Engineering (Chemical), RMIT University, Melbourne School of Civil, Environmental & Chemical Engineering Department of Chemical Engineering RMIT University, Melbourne, Australia December 2012 i DECLARATION I hereby declare that: the work presented in this thesis is my own work except where due acknowledgement has been made; the work has not been submitted previously, in whole or in part, to qualify for any other academic award; the content of the thesis is the result of work which has been carried out since the official commencement date of the approved research program Signed by Sy T. Nguyen ii ACKNOWLEDGEMENTS Firstly, I would like to thank Prof. Felicity Roddick, my senior supervisor, for giving me the opportunity to do a PhD in water science and technology and her scientific input in every stage of this work. I am also grateful to Dr John Harris and Dr Linhua Fan, my co-supervisors, for their ponderable advice and positive criticisms. The Australian Research Council (ARC) and RMIT University are acknowledged for providing the funding and research facilities to make this project and thesis possible. I also wish to thank the staff of the School of Civil, Environmental and Chemical Engineering, the Department of Applied Physics and the Department of Applied Chemistry, RMIT University, for the valuable academic, administrative and technical assistance. Lastly, my parents are thanked for the encouragement and support I most needed during the time this research was carried out. -
BASICS of the TOTAL SUSPENDED SOLIDS (TSS) WASTEWATER ANALYTICAL TEST November 2016 Dr
BASICS OF THE TOTAL SUSPENDED SOLIDS (TSS) WASTEWATER ANALYTICAL TEST November 2016 Dr. Brian Kiepper Associate Professor Since the implementation of the Clean Water Act and subsequent creation of the United States Environmental Protection Agency (USEPA) in the early 1970s, poultry processing plants have been required to continually improve the quality of their process wastewater effluent discharges. The determination of wastewater quality set forth in environmental permits has been established in a series of laboratory analytical tests focused in four (4) major categories: organics, solids, nutrients and physical properties. For most poultry professionals a complete understanding of the standard methods required to accurately complete critical wastewater analytical tests is not necessary. However, a fundamental understanding of the theory behind and working knowledge of the basic procedures used to complete these wastewater tests, and the answers to commonly asked questions about each test can be a valuable tool for anyone involved in generating, monitoring, treating or discharging process wastewater. Measuring SOLIDS in Wastewater A number of analytical tests have been developed and are used to determine the concentration (typically in milligrams per liter - mg/L - or the equivalent unit of parts per million - ppm) of the various forms SOLIDS can exist within a wastewater sample. One of the laboratory test most widely used to establish and monitor environmental permit limits for the concentration of SOLIDS in wastewater samples is total suspended solids (TSS). SOLIDS in wastewater can be viewed in two basic ways: particulate size or particulate composition. The TSS test is based within the category of particulate size and is represented in the following formula: Total Solids (TS) = Total Suspended Solids (TSS) + Total Dissolved Solids (TDS) Basics of the TSS Test As the formula above shows, TS in a wastewater sample can be separated based on particulate size into TSS and TDS fractions. -
Modeling of Filtration Processes—Microfiltration and Depth Filtration for Harvest of a Therapeutic Protein Expressed in Pichia Pastoris at Constant Pressure
Bioengineering 2014, 1, 260-277; doi:10.3390/bioengineering1040260 OPEN ACCESS bioengineering ISSN 2306-5354 www.mdpi.com/journal/bioengineering Article Modeling of Filtration Processes—Microfiltration and Depth Filtration for Harvest of a Therapeutic Protein Expressed in Pichia pastoris at Constant Pressure Muthukumar Sampath, Anupam Shukla and Anurag S. Rathore * Department of Chemical Engineering, Indian Institute of Technology, Hauz Khas, New Delhi, 110016, India * Author to whom correspondence should be addressed; E-Mail: [email protected]; Tel.: +91-96-5077-0650. External Editor: Christoph Herwig Received: 20 October 2014; in revised form: 28 November 2014 / Accepted: 3 December 2014 / Published: 8 December 2014 Abstract: Filtration steps are ubiquitous in biotech processes due to the simplicity of operation, ease of scalability and the myriad of operations that they can be used for. Microfiltration, depth filtration, ultrafiltration and diafiltration are some of the most commonly used biotech unit operations. For clean feed streams, when fouling is minimal, scaling of these unit operations is performed linearly based on the filter area per unit volume of feed stream. However, for cases when considerable fouling occurs, such as the case of harvesting a therapeutic product expressed in Pichia pastoris, linear scaling may not be possible and current industrial practices involve use of 20–30% excess filter area over and above the calculated filter area to account for the uncertainty in scaling. In view of the fact that filters used for harvest are likely to have a very limited lifetime, this oversizing of the filters can add considerable cost of goods for the manufacturer. Modeling offers a way out of this conundrum. -
Microfiltration Membranes for the Laboratory
Millipore offers a complete selection of filter holders to match any application. • Glass, stainless steel or plastic formats • Compatible with most chemicals ProductData Sheet Selection Guide • Diameters from 13 mm to 293 mm to suit a wide range of volumes Microfiltration Membranes for the • Visit www.millipore.com for more information on filter Laboratory holders and accessories www.millipore.com/offices Millipore, Durapore, Multiscreen, Ultrafree, Millex, Steriflip, Stericup are registered trademarks of Millipore Corporation The M mark, Advancing Life Sciences Together, Fluoropore, Mitex, Omnip- FSC Logo Here ore, Isopore, Express, Solvinert are trademarks of Millipore Corporation Lit. No. DS2194EN00 Rev. - 05/09 BS-GEN-09-01826 Printed in U.S.A. © 2009 Millipore Corporation, Billerica, MA 01821 U.S.A. All rights reserved. Millipore’s expert team of scientists understands the complexity of collection, separation and purification processes and supports your most difficult challenges in life science, environmental and industrial research. Choosing the proper membrane device Membrane Selection for Mobile Phase Preparation: Chemical Compatibility for your laboratory process is an SoLventS Diluent Buffers important first step in any successful MoBiLe PhaSe Sample Modifiers analysis. To help you identify the filtra- 10 mM 50 mM Membrane 2% Fomic 0.1% Phosphate 50 mM ammonium tion device best suited to your specific Material Meoh Water aCn iPa DMSo DMF acid tea Buffer ammonia 0.1% tFa acetate application we created a this handy PtFe Q Q Q Q Q Q Q Q Q Q Q Q membrane selection guide that will help PvDF Q Q Q Q Q Q Q Q Q Q Q Q you choose the Millipore® membrane PeS that will provide you with the highest Q Q Q Q Q N N Q Q Q Q N quality, consistent results from down- nYLon N Q Q N Q Q Q Q Q N Q Q stream analyses. -
Leachate Treatability Study
Leachate Treatability Study HOD LANDFILL Antioch, Illinois r. „'- <••> ••• o ••» j^ V u v/v >• \.'l» Waste Management of North America- Midwest Two Westbrook Corporate Center • Suite 1000 • Westchester, Illinois 60154 Prepared by: RUST ENVIRONMENT & INFRASTRUCTURE, INC. Formerly SEC Donohve, Inc. Solid Waste Division 1240 Dichl Road • Naperville, Illinois 60563 • 708/955-6600 March 1993 Waste Management of North America- Midwest HOD LANDFILL LEACHATE TREATABILITY STUDY [; tr Project No. 70006 0 n I : ir • n [ J Prepared by: ! , RUST Environment & Infrastructure [ Formerfy SEC Donohue, Inc. ^ 1240 East Diehl Road n Naperville, Illinois 60563 MARCH 1993 0.0 Executive Summary A treatability study was conducted for HOD Landfill to determine the ability of a preliminary treatment facility design to reduce contaminants to limits acceptable for discharge to the City of Antioch POTW. Two pilot scale Sequencing Batch Reactors (SBRs) were operated at varying loading conditions between 0.1 and 0.7 g Chemical Oxygen Demand (COD)/g Mixed Liquor Volatile Suspended Solids (MLVSS) per day and the r reactors were monitored for treatability performance and optimal operating conditions. r: Optimal design/ operating conditions were evaluated during the study as well. The full- scale system should be designed with a loading of 0.2 gCOD/gMLVSS for conservative purposes. The reactor will be capable of successfully operating at varying loadings between 0.1-0.4 gCOD/gMLVSS with a pH range of 7.0-8.0 and temperature between 20-30 *C in the reactor. Table 11 presents the optimal design/operating conditions for the full-scale process. During higher loading conditions, pH control will be necessary to maximize the process efficiency and reduce effluent concentrations. -
Individual Home Wastewater Characterization and Treatment
INDIVIDUAL HOME WASTEWATER CHARACTERIZATION AND TREATMENT Edwin R. Bennett and K. Daniel Linstedt Completion Report No. 66 INDIVIDUAL HDME WASTEWATER CHARACTERIZATION AND TREATMENT Completion Report OWRT Project No. A-021-COLO July 1975 by Edwin R. Bennett and K. Daniel Linstedt Department of Civil and Environmental Engineering University of Colorado Boulder, Colorado submitted to Office of Water Research and Technology U. S. Department of the Interior Washington, D. C. The work upon which this report is based was supported by funds provided by the U. S. Department of the Interior, Office of Water Research and Technology, as authorized by the Water Resources Research Act of 1964, and pursuant to Grant Agreement Nos. 14-31-0001-3806, 14-31-0001-4006, and 14-31-0001-5006. Colorado Water Resources Research Institute Colorado State University Fort Collins. Colorado 80523 Norman A. Evans, Director TABLE OF CONTENTS Page Chapter I. Introduction 1 Chapter II. Water Use in the Home 6 Comparison with Published Data ". 23 Discussion ...... .. 26 Chapter III. Wastewater Po11utiona1 Strength Characteristics 28 Work of Other Researchers. 37 Summary. ... 43 Chapter IV. Individual Home Treatment Systems 45 Septic Tanks . 45 Discussion 60 Aerobic Treatment Units 61 Evapo-Transpiration Systems 67 Water Saving Appliances and In-Home Reuse. 74 Cost Considerations.•.......• 78 Chapter V. Recycling Potential of Home Wastewater Streams. 81 Experimental Procedures and Results. 85 Phase 1. 86 Phase 2. 91 Results 98 Biological Oxidation . 98 Dual Media Filtration .101 Carbon Adsorption. .. .109 Work of Other Researchers .119 Discussion ... .126 Chapter VI. Summary .132 References . .134 LIST OF TABLES Page 1. Composition of Families in Homes Studied 6 2. -
Reduction in Median Load of Total Suspended Solids (TSS) Due To
Reduction in Median Load of Total Suspended Solids [TSS] Due to Tree Cover This EnviroAtlas community map estimates the annual reduction in kilograms of the median load of total suspended solids (TSS) in urban stormwater runoff due to filtration by trees within each census block group. Estimates were produced with the i-Tree Hydro analysis tool developed by the USDA Forest Service. Why is total suspended solids reduction important? Urban stormwater runoff is a major source of total suspended solids (or TSS) entering streams and lakes near developed areas. Sources of TSS in urban runoff include soil from pavement, overland flow, and landfills; airborne dust and chemical compounds; organic debris; and sewage.1,2 TSS from aerial and terrestrial sources accumulates on urban land and pavement until runoff from precipitation carries the Besides degrading water quality, polluted stormwater runoff pollutants into stormwater drains and directly to local affects recreational opportunities, community aesthetics, and waterbodies. The highest TSS loadings originate from sense of well-being for local residents.1 Urban tree cover can construction sites (a typical load is 6000 lbs/acre/year) and benefit communities by reducing the influx of total suspended impervious surfaces (e.g., commercial properties, freeways, solids. The proportions of tree cover relative to impervious and industrial sites [at ≤ 1000 lbs/acre/year]).2 Sediment surfaces in community neighborhoods influence the quantity particles also carry molecules of nutrients, pesticides, heavy and speed of urban stormwater runoff entering nearby metals, and volatile chemicals such as petroleum products, waterbodies. Trees planted along roadways, in retention which may be released by disturbance or microbial activity.3 basins, or riparian buffers intercept runoff, slow the passage of stormwater to drains, and filter significant quantities of Impervious surfaces greatly increase peak runoff velocity and sediment.