Review on Increasing Efficiency of Biogas Production from Sewage Sludge
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Cost Analysis of the Impacts on Municipal Utilities and Biosolids Management to Address PFAS Contamination
Cost Analysis of the Impacts on Municipal Utilities and Biosolids Management to Address PFAS Contamination October 2020 Table of Contents Executive Summary Section 1 Background 1.1 Biosolids ................................................................................................................................................................ 1-1 Section 2 Data on Actual Costs to Wastewater and Biosolids Management Programs from PFAS 2.1 Introduction ......................................................................................................................................................... 2-1 2.2 NEBRA Survey ..................................................................................................................................................... 2-1 2.2.1 Background ............................................................................................................................................. 2-1 2.2.2 Results ...................................................................................................................................................... 2-2 2.3 Expanded Utility Survey ................................................................................................................................. 2-2 2.3.1 Background ............................................................................................................................................. 2-2 2.3.2 Results ..................................................................................................................................................... -
Landfill Leachate Pretreatment Process Evaluation and Pilot Study
Landfill Leachate Pretreatment Process Evaluation and Pilot Study Richard Claus – Hazen and Sawyer, P.C. John Butler – Rumpke Consolidated Companies, Inc. Dan Miklos – Hazen and Sawyer, P.C. Presentation Overview Part 1 – Overview of Study, Piloting, and Design Introduction Timeline of Study, Evaluation, & Disposal Wastewater Characterization & Pretreatment Study Timeline of Piloting and Design Pretreatment Design Presentation Overview Part 2 – Pilot Treatment Sessil Media Trickling Filter Pilot Chemical Treatment Jar Testing and Pilot Considered ElectroCell Piloting Next Steps Introduction Rumpke Sanitary Landfill Cincinnati, OH, Colerain Township, Northwest Hamilton County Rumpke Consolidated Companies, Inc. Family Owned, Operated since 1945 One of the largest landfills in the nation, largest in Ohio Rumpke Colerain Township Landfill Introduction Northwest Area Landfill Portion of landfill undergoing a reaction since August, 2009 Source of extremely strong leachate Averaging 120-degrees Fahrenheit Average Volumes of 120,000 GPD (2010-2011) to 200,000 GPD (2012) Northwest Lift Station Lift Station No. 2 Pilot and Tanker Loadout Locations Northwest Area Landfill Introduction – NW Area Leachate Current Characteristics COD 30,000 to 50,000 mg/L BOD5 20,000 to 30,000 mg/L TSS 1,000 – 2,000 mg/L TKN 1,500 – 2,500 mg/L Fe 250 – 700 mg/L Ca 1,500 – 3,700 mg/L Temperature 120 degrees F Introduction – NW Area Leachate On –Going Issues Pipe scaling/clogging during conveyance Odors during handling/disposal Costs for disposal Study, Evaluation, and Disposal Timeline August, 2009 – Increasing leachate strength from Northwest Area August, 2010 to May, 2011 – Wastewater Characterization & Pretreatment Study August, 2011 to June, 2012 – Treatment Piloting and Pretreatment Design Study, Evaluation, and Disposal Timeline - Continued Historically until October 7, 2011 – “Blended” Flow Sewer Discharge into MSDGC Collection System NW Area Leachate (Approx. -
PFAS in Influent, Effluent, and Residuals of Wastewater Treatment Plants (Wwtps) in Michigan
Evaluation of PFAS in Influent, Effluent, and Residuals of Wastewater Treatment Plants (WWTPs) in Michigan Prepared in association with Project Number: 60588767 Michigan Department of Environment, Great Lakes, and Energy April 2021 Evaluation of PFAS in Influent, Effluent, and Residuals of Project number: 60588767 Wastewater Treatment Plants (WWTPs) in Michigan Prepared for: Michigan Department of Environment, Great Lakes, and Energy Water Resources Division Stephanie Kammer Constitution Hall, 1st Floor, South Tower 525 West Allegan Street P.O. Box 30242 Lansing, MI 48909 Prepared by: Dorin Bogdan, Ph.D. Environmental Engineer, Michigan E-mail: [email protected] AECOM 3950 Sparks Drive Southeast Grand Rapids, MI 49546 aecom.com Prepared in association with: Stephanie Kammer, Jon Russell, Michael Person, Sydney Ruhala, Sarah Campbell, Carla Davidson, Anne Tavalire, Charlie Hill, Cindy Sneller, and Thomas Berdinski. Michigan Department of Environment, Great Lakes, and Energy Water Resources Division Constitution Hall 525 West Allegan P.O. Box 30473 Lansing, MI 48909 Prepared for: Michigan Department of Environment, Great Lakes, and Energy AECOM Evaluation of PFAS in Influent, Effluent, and Residuals of Project number: 60588767 Wastewater Treatment Plants (WWTPs) in Michigan Table of Contents 1. Introduction ......................................................................................................................................... 1 2. Background ........................................................................................................................................ -
Eutectic Freeze Crystallization for Table Salt
Eutectic Freeze Crystallization on Sodium Chloride Analysis of a full experimental cycle Master of Science Thesis Document number: 2461 Bruno (J.J.) Verbeek Wb1179829 29-07-2011 Eutectic Freeze Crystallization on Sodium Chloride 2 Eutectic Freeze Crystallization on Sodium Chloride Faculty: Process Equipment For obtaining the degree of Master of Science in Sustainable Process- & Energy Technology Exam committee: Prof. dr. G.J. Witkamp Dr. L Hartmann K. Yasadi Copyright © BJJ Verbeek All rights reserved 3 Eutectic Freeze Crystallization on Sodium Chloride Contents Acknowledgement ........................................................................................................................................ 6 Abstract ......................................................................................................................................................... 7 Table of figures ............................................................................................................................................. 9 Nomenclature ............................................................................................................................................. 11 1. Introduction ........................................................................................................................................ 13 1.1. Eutectic freeze crystallization ..................................................................................................... 14 1.2. Sodium chloride solutions .......................................................................................................... -
The Imhoflot G-Cell – an Advanced Pneumatic Flotation Technology for the Recovery of Coal Slurry from Impoundments
THE IMHOFLOT G-CELL – AN ADVANCED PNEUMATIC FLOTATION TECHNOLOGY FOR THE RECOVERY OF COAL SLURRY FROM IMPOUNDMENTS M. J. G. Battersby Maelgwyn Mineral Services Ltd Llandudno, Wales, UK J. V. Brown Maelgwyn Mineral Services Limited Llandudno, Wales, UK R. M. Imhof Maelgwyn Mineral Services Ltd Dorsten, Germany 2 ABSTRACT large amounts of ultra fine high volatility coal there is the possibility that these ponds can give rise to spontaneous There is a plethora of former industrial sites where coal combustion at some time in the future. Both these mining operations have left large slurry impoundments. possibilities pose a major risk to the environment. These contain raw washed fines, which have previously been too expensive to process to requisite grades for There have been many attempts to recover coal from commercial use. New technology has been developed for tailings impoundments. Very few have been economically fine material processing, namely the Imhoflot pneumatic successful no matter which technology has been applied. flotation G-Cell. This froth flotation technique is a highly Whilst there are many different and valid reasons efficient means of concentrating coal and is particularly recorded for their failure the most common is that the appropriate to the nature of materials encountered in project had not been able to bear the burden of the capital tailings ponds. The high volumetric throughput resulting cost of a plant required to process the material to an from the vastly reduced residence time in the cell allows acceptable standard. Unlike a new mine where a planned for drastically reduced equipment sizes when compared to life of mine of twenty years would not be uncommon, a conventional flotation cells. -
Liquid / Solids Separation in Wastewater Treatment & Biosolids Dewatering
LIQUID / SOLIDS SEPARATION IN WASTEWATER TREATMENT & BIOSOLIDS DEWATERING Chemical Products Lab Testing Plant Trials LIQUID / SOLIDS SEPARATION APPLICATIONS Influent Water Clarification Process Water Recycling Primary Wastewater Clarification Secondary Clarification Sludge Thickening Sludge Dewatering LIQUID / SOLIDS SEPARATION UNIT OPERATIONS Clarifiers (Many Types) WATER Filters (Many Types) OR WASTE Dissolved Air Flotation Units WATER Induced Air/Gas Flotation Units Belt Presses Centrifuges SLUDGE Screw Presses DEWATERING Plate and Frame Presses Vacuum Filters (Rotary & Horizontal) LIQUID / SOLIDS SEPARATION PRODUCT TYPES Coagulants (+) Low Mol Wt Organic Inorganic Blended Flocculants (+ , ---, 0 ) High Mol Wt Dry Emulsion Solution OilOil----FreeFree Flocculants COAGULANTS AND FLOCCULANTS Act on Insoluble Particles in Water Oils, Grease, Blood, Insoluble Organics, Clay, Silicates, Metal Oxides/Hydroxides Dirt, Dust, Rust & Metal Filings Can Act on Charged Organic Compounds Anionic Surfactants, Soaps & Dispersants Do Not Act on Most Dissolved Solids Salts, Acids, Nonionic Surfactants, Ammonia or Soluble Organic Compounds such as Sugar, Alcohols, etc. SUSPENSION CHEMISTRY THE KEY TO EFFECTIVE LIQUID / SOLIDS SEPARATION SUSPENDED SOLIDS VARIABLES Surface Charge MOST Charge Density Particle Size IMPORTANCE Composition Particle Density Particle Shape LEAST MICROSCOPIC FORCES ELECTROSTATIC BROWNIAN VAN DER WAALS GRAVITY Colloidal Particle in Water +++ +++ +++ +++ +++ +++ +++ +++ +++ +++ Almost all Particles +++ -
NAWI Technology Roadmap: Resource Extraction Sector
RESOURCE EXTRACTION SECTOR TECHNOLOGY ROADMAP Tzahi Cath Cameron McKay Colorado School of Mines The University of Texas–Austin Shankar Chellam Kaleisha Miller Texas A&M University Texas A&M University Lynn Katz Jason Monnell The University of Texas–Austin Electric Power Research Institute Richard Breckenridge Nalini Rao Electric Power Research Institute Electric Power Research Institute Carolyn A. Cooper James Rosenblum The University of Texas–Austin Colorado School of Mines Kirk Ellison David Sedlak Electric Power Research Institute University of California–Berkeley Jordan Macknick Jennifer Stokes-Draut National Renewable Energy Laboratory Lawrence Berkeley National Laboratory Acknowledgements This material is based upon work supported by the National Alliance for Water Innovation (NAWI), funded by the U.S. Department of Energy, Office of Energy Efficiency and Renewable Energy (EERE), Advanced Manufacturing Office, under Funding Opportunity Announcement Number DE-FOA-0001905. NAWI would like to thank the Department of Energy Technical Monitor Melissa Klembara for guidance and support throughout the roadmapping process. This roadmap was developed under the guidance of the National Alliance for Water Innovation (NAWI) Desalination Hub executive team, cartographers, and technical staff as well as the NAWI’s Research Advisory Council (RAC). Those from industry, academia, national laboratories, and government who made crucial contributions through participation in workshops, surveys, phone interviews, and roadmap reviews are identified in Appendix F of this report. Nexight Group supported the overall roadmapping process. Suggested citation Tzahi Cath; Shankar Chellam; Lynn Katz; Richard Breckenridge; Carolyn A. Cooper; Kirk Ellison; Jordan Macknick; Cameron McKay; Kaleisha Miller; Jason Monnell; Nalini Rao; James Rosenblum; David Sedlak; Jennifer Stokes-Draut. -
Development of Solid-Liquid Separation Technologies in Bioprocessing Christopher Robert Koza Iowa State University
Iowa State University Capstones, Theses and Graduate Theses and Dissertations Dissertations 2012 Development of solid-liquid separation technologies in bioprocessing Christopher Robert Koza Iowa State University Follow this and additional works at: https://lib.dr.iastate.edu/etd Part of the Chemical Engineering Commons, and the Environmental Engineering Commons Recommended Citation Koza, Christopher Robert, "Development of solid-liquid separation technologies in bioprocessing" (2012). Graduate Theses and Dissertations. 12813. https://lib.dr.iastate.edu/etd/12813 This Thesis is brought to you for free and open access by the Iowa State University Capstones, Theses and Dissertations at Iowa State University Digital Repository. It has been accepted for inclusion in Graduate Theses and Dissertations by an authorized administrator of Iowa State University Digital Repository. For more information, please contact [email protected]. Development of solid-liquid separation technologies in bioprocessing by Christopher Robert Koza A thesis submitted to the graduate faculty in partial fulfillment of the requirements for the degree of MASTER OF SCIENCE Major: Civil Engineering (Environmental Engineering) Program of Study Committee: Hans van Leeuwen, Co-major Professor Stephanie Jung, Co-major Professor Shihwu Sung Iowa State University Ames, Iowa 2012 Copyright © Christopher Robert Koza, 2012. All rights reserved ii TABLE OF CONTENTS ABSTRACT iii CHAPTER 1. INTRODUCTION 1 Introduction 1 Thesis Organization 3 CHAPTER 2. LITERATURE REVIEW 4 Ethanol Industry 4 Solid-Liquid Separation 26 References 41 CHAPTER 3. A PILOT STUDY ON DEWATERING FUNGAL BIOMASS FROM A NOVEL CORN ETHANOL BIOPROCESS 45 Abstract 45 Introduction 46 Methods and Materials 49 Results and Discussion 57 Conclusion 65 Acknowledgements 66 References 67 CHAPTER 4. -
National Manual of Good Practice for Biosolids
Material Matters, Inc. Material Matters, Inc. Material Matters, Inc. Material Matters, Inc. Material Matters, Inc. Material Matters, Inc. Material Matters, Inc. Material Matters, Inc. Material Matters, Inc. National Manual of Good Practice for Biosolids Material Matters, Inc. Material Matters, Inc. Material Matters, Inc. Last Updated January 2005 View the Document Control Log for a Summary of Revisions Material Matters, Inc. Material Matters, Inc. Material Matters, Inc. Material Matters, Inc. Material Matters, Inc. Material Matters, Inc. NATIONAL MANUAL OF GOOD PRACTICE FOR BIOSOLIDS Table of Contents Material Matters, Inc. Material Matters, Inc. Material Matters, Inc. Introduction Acknowledgements 1 Public Acceptance 1.1 Sharing Public Perception 1.1.1 Environmental Benefits 1.1.2 Community Benefits 1.2 Analyzing Operations 1.3 Dealing with Odors 1.4 Developing Effective Communication 1.4.1 Communication Approaches: Proactive Reactive 1.4.2 Communication Tools 1.5 Environmental Management System Connections Material Matters, Inc. 1.6 MessageMaterial DevelopmentMatters, Inc. Material Matters, Inc. 1.6.1 Risk Communications 1.6.2 Information Examples with Land Application 1.6.3 Presenting Messages Effectively 1.6.4 Developing Outreach 1.7 Maintaining Support 2 Federal and State Regulations 2.1 Federal Regulations 2.1.1 History and Background 2.1.2 Standards for the use or Disposal of Biosolids 2.2 General Requirements – 40CFR Part 503.12 2.2.1 Land Application 2.2.2 Surface Disposal 2.2.3 Incineration Material Matters, Inc. 2.3 RiskMaterial -
Proven Solutions for the Produced Water Industry
CECO Peerless PROVEN SOLUTIONS FOR THE PRODUCED WATER INDUSTRY WITH OVER 80 OF YEARS EXPERIENCE, CECO PEERLESS IS THE GLOBAL LEADER IN SEPARATION TECHNOLOGIES FOR THE OIL, GAS AND PETROCHEMICAL MARKETS. Offering treatment systems for both onshore and offshore applications, CECO Peerless designs and supplies a wide range of compact, engineered, high-efficiency, processing, separation and filtration equipment for the global oil and gas industry. CECO Environmental’s energy solutions include leading technologies such as CECO Peerless separation and filtration, Burgess Manning oil and gas processing technologies and Skimovex oily water separation. Key CECO Peerless Facts • Over 80 years of experience • 1000s of successful installations and millions of hours of engineering excellence • Experienced in technology, process, engineering and turnkey solutions • Expertise from concept through commissioning stages • Worldwide delivery capability and vast network of local / regional / global partners • Global presence, multi-cultural teams with localised approach to attain clean, safe, efficient and sustainable solutions within budget and schedule CECO Peerless provides you with the seamless end-to-end solution. We combine our technologies, process experience and R&D with our multi-disciplined engineering experience to give you every advantage: • Concept / FEED studies • Fast track delivery • Detailed engineering • Achieve overall performance • Engineered packages • Customer satisfaction • Modular / skid design and supply • After sales service • Turnkey solutions for EPF / CPF / topsides www.cecopeerless.com PRODUCED WATER TREATMENT WITH DECADES OF EXPERIENCE AND EXPERTISE, CECO PEERLESS DELIVERS RELIABLE AND ECONOMICAL COMPONENTS OR COMPLETE WATER TREATMENT SOLUTIONS TO ENSURE OPTIMAL PERFORMANCE AND OIL AND WATER SEPARATION EFFICIENCY. PRIMARY TREATMENT CORRUGATED PLATE INTERCEPTORS CECO Peerless Corrugated Plate Interceptors (CPI) as Oily Water Separators can be designed with various configurations, i.e., in a steel tank, in a concrete basin, or in a pressure vessel. -
A White Paper Describing Produced Water from Production of Crude Oil
AAA WWWhhhiiittteee PPPaaapppeeerrr DDDeeessscccrrriiibbbiiinnnggg PPPrrroooddduuuccceeeddd WWWaaattteeerrr fffrrrooommm PPPrrroooddduuuccctttiiiooonnn ooofff CCCrrruuudddeee OOOiiilll,,, NNNaaatttuuurrraaalll GGGaaasss,,, aaannnddd CCCoooaaalll BBBeeeddd MMMeeettthhhaaannneee Prepared for: U.S. Department of Energy National Energy Technology Laboratory Under Contract W-31-109-Eng-38 Prepared by: Argonne National Laboratory John A. Veil Markus G. Puder Deborah Elcock Robert J. Redweik, Jr. January 2004 Produce Water White Paper i TABLE OF CONTENT Executive Summary............................................................................................................ v 1 Introduction............................................................................................................. 1 1.1 What Is Produced Water? ................................................................................... 1 1.2 Purpose................................................................................................................ 1 1.3 Layout of White Paper........................................................................................ 2 1.4 Acknowledgments .............................................................................................. 2 2 Produced Water Characteristics.............................................................................. 3 2.1 Major Components of Produced Water .............................................................. 3 2.1.1 Produced Water from Oil Production ............................................................ -
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