More Than You Ever Wanted to Know About Your Aeration Septic System
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Effects of Leachate Recirculation and Ph Adjustment
Distributed Model of Solid Waste Anaerobic Digestion Effects of Leachate Recirculation and pH Adjustment Vasily A. Vavilin,1 Sergey V. Rytov,1 Ljudmila Ya. Lokshina,1 Spyros G. Pavlostathis,2 Morton A. Barlaz3 1Water Problems Institute, Russian Academy of Sciences, Moscow 119991, Russia; e-mail: [email protected] 2Georgia Institute of Technology, Atlanta, Georgia 30332-0512 3North Carolina State University, Raleigh, North Carolina 27695-7908 Received 25 March 2002; accepted 5 June 2002 DOI: 10.1002/bit.10450 Abstract: A distributed model of solid waste digestion bioreactors have been operated for over a decade. However, in a 1-D bioreactor with leachate recirculation and pH the cost of these systems is relatively high (Westegard and adjustment was developed to analyze the balance be- tween the rates of polymer hydrolysis/acidogenesis and Teir, 1999). In “wet” complete mixed systems, the organic methanogenesis during the anaerobic digestion of mu- solid waste is diluted with water to less than 15% total nicipal solid waste (MSW). The model was calibrated on solids (TS), while in “dry” systems, the waste mass within previously published experimental data generated in 2-L the reactor is kept at a solids content in the range of 20–40% reactors filled with shredded refuse and operated with TS. Because batch digesters are technically simple, the capi- leachate recirculation and neutralization. Based on model simulations, both waste degradation and meth- tal cost is significantly lower than for continuously fed di- ane production were stimulated when inhibition was pre- gesters, though some technical problems still exist (ten vented rapidly from the start, throughout the reactor vol- Brummeler, 2000). -
Sequencing Batch Reactors: Principles, Design/Operation and Case Studies - S
WATER AND WASTEWATER TREATMENT TECHNOLOGIES - Sequencing Batch Reactors: Principles, Design/Operation and Case Studies - S. Vigneswaran, M. Sundaravadivel, D. S. Chaudhary SEQUENCING BATCH REACTORS: PRINCIPLES, DESIGN/OPERATION AND CASE STUDIES S. Vigneswaran, M. Sundaravadivel, and D. S. Chaudhary Faculty of Engineering and Information Technology, School of Civil and Environmental Engineering and Information Technology, University of Technology Sydney, Australia Keywords: Activated sludge process, return activated sludge, sludge settling, wastewater treatment, Contents 1. Background 2. The SBR technology for wastewater treatment 3. Physical description of the SBR system 3.1 FILL Phase 3.2 REACT Phase 3.3 SETTLE Phase 3.4 DRAW or DECANT Phase 3.5 IDLE Phase 4. Components and configuration of SBR system 5. Control of biological reactions through operating strategies 6. Design of SBR reactor 7. Costs of SBR 8. Case studies 8.1 Quakers Hill STP 8.2 SBR for Nutrient Removal at Bathhurst Sewage Treatment Plant 8.3 St Marys Sewage Treatment plant 8.4 A Small Cheese-Making Dairy in France 8.5 A Full-scale Sequencing Batch Reactor System for Swine Wastewater Treatment, Lo and Liao (2007) 8.6 Sequencing Batch Reactor for Biological Treatment of Grey Water, Lamin et al. (2007) 8.7 SBR Processes in Wastewater Plants, Larrea et al (2007) 9. Conclusion GlossaryUNESCO – EOLSS Bibliography Biographical Sketches SAMPLE CHAPTERS Summary Sequencing batch reactor (SBR) is a fill-and-draw activated sludge treatment system. Although the processes involved in SBR are identical to the conventional activated sludge process, SBR is compact and time oriented system, and all the processes are carried out sequentially in the same tank. -
Troubleshooting Activated Sludge Processes Introduction
Troubleshooting Activated Sludge Processes Introduction Excess Foam High Effluent Suspended Solids High Effluent Soluble BOD or Ammonia Low effluent pH Introduction Review of the literature shows that the activated sludge process has experienced operational problems since its inception. Although they did not experience settling problems with their activated sludge, Ardern and Lockett (Ardern and Lockett, 1914a) did note increased turbidity and reduced nitrification with reduced temperatures. By the early 1920s continuous-flow systems were having to deal with the scourge of activated sludge, bulking (Ardem and Lockett, 1914b, Martin 1927) and effluent suspended solids problems. Martin (1927) also describes effluent quality problems due to toxic and/or high-organic- strength industrial wastes. Oxygen demanding materials would bleedthrough the process. More recently, Jenkins, Richard and Daigger (1993) discussed severe foaming problems in activated sludge systems. Experience shows that controlling the activated sludge process is still difficult for many plants in the United States. However, improved process control can be obtained by systematically looking at the problems and their potential causes. Once the cause is defined, control actions can be initiated to eliminate the problem. Problems associated with the activated sludge process can usually be related to four conditions (Schuyler, 1995). Any of these can occur by themselves or with any of the other conditions. The first is foam. So much foam can accumulate that it becomes a safety problem by spilling out onto walkways. It becomes a regulatory problem as it spills from clarifier surfaces into the effluent. The second, high effluent suspended solids, can be caused by many things. It is the most common problem found in activated sludge systems. -
Guide for Owners of Package Extended Aeration Sewage Treatment Plants
State of Ohio Environmental Protection Agency OPERATION AND MAINTENANCE GUIDE FOR OWNERS OF PACKAGE EXTENDED AERATION SEWAGE TREATMENT PLANTS Division of Surface Water 2000 TABLE OF CONTENTS I. UNDERSTANDING YOUR EXTENDED AERATION...................................................................................................2 SEWAGE DISPOSAL SYSTEM II. INSTALLATION.............................................................................................................................................................3-4 III. INITIAL OPERATION - START-UP.................................................................................................................................5 IV. PLANT MAINTENANCE PROCEDURE....................................................................................................................6-10 VISUAL CHECK LIST AERATION TANK.....................................................................................................................8 VISUAL CHECK LIST SETTLING TANK.......................................................................................................................9 MONTHLY OPERATION AND MAINTENANCE RECORD......................................................................................10 V. SAFETY............................................................................................................................................................................11 VI. SPECIAL PROCEDURES FOLLOWING PLANT SHUTDOWN..................................................................................11 -
Phosphorus Removal in Extended Aeration Systems by Chemical Precipitation
July 1977 Report No. Env. E. 56-77-2 Phosphorus Removal in Extended Aeration Systems by Chemical Precipitation C. James AAartel Francis A. DiGiano Robert E. Pariseau Report to the Division of Water Pollution Control Massachusetts Water Resources Commission Department of Environmental Quality Engineering Contract Number 76-10(1) ENVIRONMENTAL ENGINEERING DEPARTMENT OF CIVIL ENGINEERING UNIVERSITY OF MASSACHUSETTS AMHERST, MASSACHUSETTS PHOSPHORUS REMOVAL IN EXTENDED AERATION SYSTEMS BY CHEMICAL PRECIPITATION By C. James Martel Research Associate Francis A. DiGiano Associate Professor of Civil Engineering Robert E. Pariseau Research Chemist Division of Water Pollution Control Massachusetts Water Resources Commission Department of Environmental Quality Engineering Contract Number MDWPC 76-10(1) Environmental Engineering Program Department of Civil Engineering University of Massachusetts Amherst, Massachusetts 01003 PREFACE This report represents the combined results of many studies on phosphorus removal in extended aeration systems conducted at the University of Massachusetts Wastewater Pilot Plant by Environmental Engineering Program graduate students. Robert M. Burke (12) conducted the first study with alum and concluded that there was insufficient alkalinity in Amherst wastewater to ensure pH values compatible with biological treatment. Alan J. Roy (13) examined the effect of alum addition on sludge accumulation and determined that a dosage of 200 mg/£ would triple the sludge accumulation rate. Raymond A. Noga (8) tried a lower alum dose (100 rng/n) but pH was still depressed and sludge production again tripled. Finally, a study was conducted inhouse by Mr. C. James Martel, Research Associate, and Robert E. Pariseau, Research Chemist, during which lime was added for pH control. Most of the data on alum addition presented in this report is the result of this latter study. -
Utilization of Ultraviolet-Visible Spectroscopy and Rheology for Sludge Characterization and Monitoring
Utilization of ultraviolet-visible spectroscopy and rheology for sludge characterization and monitoring by Jordan Smyth A thesis submitted to the Faculty of Graduate and Postdoctoral Affairs in partial fulfillment of the requirements for the degree of Master of Applied Science in Environmental Engineering Department of Civil and Environmental Engineering Ottawa-Carleton Institute for Environmental Engineering Carleton University Ottawa, Ontario © Jordan Smyth, 2018 Abstract Operation of sludge treatment processes mainly relies on manual control, which is far from ideal. There is a need for new approaches to optimize the operation of sludge treatment processes and wastewater plants. This research aims to identify new tools and methods that can be used for in- line and real-time characterization and monitoring of sludge. Two methods that were examined in this thesis that have potential to be used as monitoring technologies were ultraviolet/visible spectrophotometry and torque rheology. Effluent and filtrate absorbance measurements in the ultraviolet/visible range were successful in monitoring the progress of aerobic digestion. Torque rheology was not found to be sensitive enough for monitoring aerobic digestion of sludge, however it was able to detect changes in the total solids content of anaerobically digested sludge. Torque rheology detected significant changes in anaerobically digested sludge when trivalent cations were added, but not when divalent cations were added. i Acknowledgements First off, I would like to thank my supervisor Dr. Banu Ormeci. Her guidance, knowledge and motivation throughout the entire process was so helpful. She has had such a positive influence on my life and I will forever be grateful. I would also like to thank Dr. -
Wastewater Systems
Wastewater Systems Wastewater Systems 4100 Idela Ave. McAllen, Tx. 78503 Phone: (956)681-1750 Fax: (956)681-1767 Web: https://mcallenpublicutility.com/departments/wastewater-systems/ Table of Contents Welcome ............................................................................................1 Biological Nutrient Removal (BNR) ....................................................2 Reclaimed Water Extended Aeration ............................................................................3 Reclaimed water, which can also be called reuse water or recycle water, is converting wastewater into water that can be reused for Wastewater Collection .......................................................................4 landscaping, industry, fire protection, construction (soil compaction and Reclaimed Water ..............................................................................5 dust control), etc., but where reclaimed water’s true benefit arises for a city is conserving water. With the Rio Grande Valley prone to droughts; McAllen Public Utility (MPU) has always been a leader in the conservation of water and is the first Valley city to create a residential reclaimed water irrigation program to conserve potable water. MPU is the first city south of San Antonio to provided reclaimed water to a residential subdivision to irrigate their lawns; furthermore, MPU is already saving over 1.0 billion gallons of water per year distributing reclaim water too Calpine energy. Calpine energy uses reclaimed water for their electrical plant in their cooling towers. There are two types of reclaimed water: Type I and Type II. Type I is superior than Type II, and Type I is used for the above mentioned. Reclaimed water is regulated by Texas Commission of Environmental Quality (TCEQ) and our WWTPs must meet strict regulations to produce this water. Many other cities use reclaimed water such as: San Antonio uses reclaimed water to augment stream flow in the San Antonio River along the famous River Walk. -
Anaerobic Treatment of Food Waste Leachate for Biogas Production Using a Novel Digestion System
Environ. Eng. Res. 2012 March,17(1) : 41-46 Research Paper http://dx.doi.org/10.4491/eer.2012.17.1.041 pISSN 1226-1025 eISSN 2005-968X Anaerobic Treatment of Food Waste Leachate for Biogas Production Using a Novel Digestion System Bong Su Lim1†, Byungchul Kim2, In Chung1 1Environmental Engineering, Daejeon University, Daejeon 300-716, Korea 2EnTechs, Seoul 135-240, Korea Abstract In this study, the performance of new digestion system (NDS) for the treatment of food waste leachate was evaluated. The food waste leachate was fed intermittently to an anaerobic reactor at increasing steps of 3.3 L/day (hydraulic retention time [HRT] = 30 day), 5 L/ day (HRT = 20 day), and finally 10 L/day (HRT = 10 day). In the anaerobic reactor, the pH and alkalinity were maintained at 7.6 to 8.2 and 8,940-14,400 mg/L, respectively. Maximum methane yield determined to be 0.686L CH4/g volatile solids (VS) containing HRT over 20 day. In the digester, 102,328 mg chemical oxygen demand (COD)/L was removed to produce 350 L/day (70% of the total) of biogas, but in the digested sludge reduction (DSR) unit, only 3,471 mg COD/L was removed with a biogas production of 158 L/day. Without adding any chemicals, 25% of total nitrogen (TN) and 31% of total phosphorus (TP) were removed after the DSR, while only 48% of TN and 32% of TP were removed in the nitrogen, phosphorus, and heavy metals (NPHM) removal unit. Total removal of TN was 73% and total removal of TP was 63%. -
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. -
The Activated Sludge Process Part 1 Revised July 2014
Wastewater Treatment Plant Operator Certification Training Module 15: The Activated Sludge Process Part 1 Revised July 2014 This course includes content developed by the Pennsylvania Department of Environmental Protection (Pa. DEP) in cooperation with the following contractors, subcontractors, or grantees: The Pennsylvania State Association of Township Supervisors (PSATS) Gannett Fleming, Inc. Dering Consulting Group Penn State Harrisburg Environmental Training Center MODULE 15: THE ACTIVATED SLUDGE PROCESS - PART 1 Topical Outline Unit 1 – General Description of the Activated Sludge Process I. Definitions A. Activated Sludge B. Activated Sludge Process II. The Activated Sludge Process Description A. Organisms B. Secondary Clarification C. Activated Sludge Process Control III. Activated Sludge Plants A. Types of Plants B. Factors that Upset Plant Operation IV. Unit Review V. References Unit 2 – Aeration I. Purpose of Aeration II. Aeration Methods A. Mechanical B. Diffused III. Aeration Systems A. Mechanical Aeration Systems B. Diffused Aeration Systems Bureau of Safe Drinking Water, Department of Environmental Protection Wastewater Treatment Plant Operator Training i MODULE 15: THE ACTIVATED SLUDGE PROCESS - PART 1 IV. Safety Procedures A. Aeration Tanks and Clarifiers B. Surface Aerators C. Air Filters D. Blowers E. Air Distribution System F. Air Headers and Diffusers V. Review VI. References Unit 3 – New Plant Start-Up Procedures I. Purpose of Plant and Equipment Review A. Document Familiarization B. Equipment Familiarization II. Equipment and Structures Check A. Flow Control Gates and Valves B. Piping and Channels C. Weirs D. Froth Control System E. Air System F. Secondary Clarifier III. Process Start-Up A. Process Units B. Process Control IV. Unit Review V. -
Anaerobic / Aerobic Digestion for Enhanced Solids and Nitrogen Removal
Anaerobic / Aerobic Digestion for Enhanced Solids and Nitrogen Removal Sarita Banjade Thesis submitted to the faculty of the Virginia Polytechnic Institute and State University in partial fulfillment of the requirements for the degree of Master of Science In Environmental Engineering Dr. John T. Novak, Chair Dr. Gregory D. Boardman Dr. Clifford W. Randall December 4, 2008 Blacksburg, VA Keywords: mesophilic anaerobic digestion, aerobic digestion, solids removal, nitrogen removal, dewatering and biosolids odors Copyright © 2008, Sarita Banjade Anaerobic / Aerobic Digestion for Enhanced Solids and Nitrogen Removal Sarita Banjade Abstract Anaerobic digestion of wastewater sludge has widely been in application for stabilization of sludge. With the increase in hauling cost and many environmental and health concerns regarding land application of biosolids, digestion processes generating minimized sludge with better effluent characteristics is becoming important for many public and wastewater utilities. This study was designed to investigate the performance of anaerobic-aerobic-anaerobic digestion of sludge and compare it to anaerobic-aerobic digestion and single stage mesophilic digestion of sludge. Experiments were carried out in three stages: Single-stage mesophilic anaerobic digestion (MAD) 20d SRT; Sequential Anaerobic/Aerobic digestion (Ana/Aer); and Anaerobic/Aerobic/Anaerobic digestion (An/Aer/An). The Anaerobic/Aerobic/Anaerobic digestion of sludge was studied with two options to determine the best option in terms of effluent characteristics. The two sludge withdrawal options were to withdraw effluent from the anaerobic digester (An/Aer/An –A) or withdraw effluent from the aerobic digester (An/Aer/An – B). Different operational parameters, such as COD removal, VS destruction, biogas production, Nitrogen removal, odor removal and dewatering properties of the resulting biosolids were studied and the results were compared among different processes. -
Extended Aeration Treatment System
Extended Aeration Treatment System – Low-loaded activated sludge technology – High oxygen transfer efficiency delivery system – Exceptional mixing energy from controlled aeration chain movement – Simple system construction – Low biosolids production Extended sludge age biological technology The Biolac® system is an innovative activated sludge process using extended retention of biological solids to create an extremely stable, easily operated system. The capabilities of this unique technology far exceed ordinary extended aeration treatment. The Biolac® process maximizes the stability of the operating environment and provides high-efficiency treatment. The design ensures the lowest-cost construction and guarantees operational simplicity. Over 800 Biolac® systems are installed throughout North America treating municipal wastewater and many types of industrial wastewater. The Biolac® system utilizes a long sludge age design. Sludge age, also known as SRT (Solids Retention Time) or MCRT (Mean Cell Residence Time), defines the operating characteristics of any aerobic biological treatment system. A longer sludge age dramatically lowers effluent BOD and ammonia levels, especially Conventional extended aeration, batch reactors and oxidation ditches Biolac System in colder climates. The Biolac® long sludge age process produces Treatment BOD levels of less than 10 mg/L and complete nitrification (less efciency (BOD and than 1 mg/L ammonia).Minor modifications to the system will NH3 removal) Process extend its capabilities to denitrification and biological phosphorus stability removal. While most extended aeration systems reach their maximum mixing capability at sludge ages of approximately 15-25 days, the Biolac® system efficiently and uniformly mixes the aeration volumes associated with a 30-70 day sludge age. Sludge production Operator The large quantity of biomass treats widely fluctuating loads with attention very few operational changes.