Performance Indicator Analysis As a Basis for Process Optimization and Energy Efficiency in Municipal Wastewater Treatment Plants
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Anaerobic Digestion of Wastewater Sludge (Nazaroff & Alvarez-Cohen, Section 6.E.3)
Anaerobic Digestion of Wastewater Sludge (Nazaroff & Alvarez-Cohen, Section 6.E.3) nice, clean water going to disinfection and then to outdoor body of receiving water (stream, lake or sea) sludge in need of further treatment The goal is to reduce the amount of sludge that needs to be disposed. The most widely employed method for sludge treatment is anaerobic digestion. In this process, a large fraction of the organic matter (cells) is broken down into carbon dioxide (CO2) and methane (CH4), and this is accomplished in the absence of oxygen. About half of the amount is then converted into gases, while the remainder is dried and becomes a residual soil-like material. What the equipment looks like The tank is capped - to prevent oxygen from coming in, - to prevent odors from escaping, and - to capture the methane produced. This methane, a fuel, can be used to meet some of the energy requirements of the wastewater treatment facility (co-generation). What the sludge looks like after anaerobic digestion and subsequent drying. It is rich in nitrates and performs well as a fertilizer. (Photos from http://www.madep-sa.com/english/wwtp.html) 1 (Originally from Metcalf & Eddy, 1991) from & Metcalf Eddy, (Originally 6.E.7) Figure Alvarez-Cohen, & (Nazaroff How the system works The treatment of wastewater sludge, from both primary and secondary treatment steps, consists of two main phases. ● In the 1st step, all incoming flows of sludge are combined, and the mixture is heated to a mild temperature (about body temperature) to accelerate biological conversion. The residence time here ranges from 10 to 20 days. -
Sedimentation and Clarification Sedimentation Is the Next Step in Conventional Filtration Plants
Sedimentation and Clarification Sedimentation is the next step in conventional filtration plants. (Direct filtration plants omit this step.) The purpose of sedimentation is to enhance the filtration process by removing particulates. Sedimentation is the process by which suspended particles are removed from the water by means of gravity or separation. In the sedimentation process, the water passes through a relatively quiet and still basin. In these conditions, the floc particles settle to the bottom of the basin, while “clear” water passes out of the basin over an effluent baffle or weir. Figure 7-5 illustrates a typical rectangular sedimentation basin. The solids collect on the basin bottom and are removed by a mechanical “sludge collection” device. As shown in Figure 7-6, the sludge collection device scrapes the solids (sludge) to a collection point within the basin from which it is pumped to disposal or to a sludge treatment process. Sedimentation involves one or more basins, called “clarifiers.” Clarifiers are relatively large open tanks that are either circular or rectangular in shape. In properly designed clarifiers, the velocity of the water is reduced so that gravity is the predominant force acting on the water/solids suspension. The key factor in this process is speed. The rate at which a floc particle drops out of the water has to be faster than the rate at which the water flows from the tank’s inlet or slow mix end to its outlet or filtration end. The difference in specific gravity between the water and the particles causes the particles to settle to the bottom of the basin. -
Sewage Secondary Treatment After Primary Treatment, the Sewage Water Is Subjected to the Next Phase Called Biological Treatment Or Secondary Treatment
Sewage secondary treatment After primary treatment, the sewage water is subjected to the next phase called biological treatment or secondary treatment. Dissolved and suspended biological materials are removed by indigenous microbial decomposition in a managed environment. In this treatment, BOD is reduced up to 90-95%. Biological treatment is carried out in two important phases: 1. Aerobic phase: oxidation lagoons trickling filters, activated sludge 2. Anaerobic phase: sludge digestion A. Oxidation lagoons /oxidation ponds / stabilization ponds 1. It is outdoor, simple, suspension type aerobic treatment. 2. It is suggested for small societies in rural areas where sufficient low lying land of little real state value is available. 3. It is oldest of the sewage treatment systems used in most of developing countries due to its low cost. 4. In this shallow pond is required which should be maximum of 10 feet depth having inlet and outlet. 5. It consists of three different zones as shown in the following diagram: Requirements of Oxidation pond: 1. Presence of algal growth which produces oxygen. 2. Oxygen is also available from atmosphere. 3. Heterotrophic aerobic and anaerobic microbes for decomposing sewage. 4. Sunlight required for photosynthesis, also has bactericidal properties (UV). Advantages of oxidation pond: 1. Simple 2. Inexpensive 3. Low maintenance Disadvantages of oxidation pond: 1. Effected by environment: low temperature, cloudy sky lowers efficiency 2. Takes longer time(Long retention time) 3. Gives bad odour(H2 S) 4. Not hygienic 5. Just lowers BOD by 25%to 60% B. Trickling Filter Method 1. It is also outdoor, aerobic, relatively simple but of film flow type. -
How Is Wastewater Treated (PDF)
FOLD FOLD FOLD We Need Your Help Industrial Service Area How is Pretreatment Here are three easy things you can do to protect The City of Everett’s wastewater treatment Wastewater water quality and minimize treatment cost. plant, called the Everett Water Pollution Control unicipal treatment plants like the EWPCF are Facility (EWPCF), is located on Smith Island 1. Keep trash out of the system. designed to treat residential and commercial in North Everett. The EWPCF serves more than Treated? ■ M Put hair, feminine hygiene products, wastewater. However, some industrial 133,000 people including all of Everett and cotton swabs and grease in the wastewater contains pollutants that primary and parts of Mukilteo, Silver Lake and Alderwood. garbage. secondary treatment cannot remove. The plant treats an average of 20 million 2. Reduce your water consumption. This wastewater requires industrial pretreatment gallons of wastewater per day, although the ■ Conserving water saves money and to remove metals, acids or other chemicals, influent volume to the plant can increase to protects the environment since the less or in the case of food services, most fats almost 100 million gallons on rainy days. water you use, the less wastewater we and grease. City staff work with industrial have to treat. customers to remove these pollutants before the 3. Keep hazardous waste out of the system. wastewater is sent to the treatment plant. ■ Never put hazardous waste down the drain. Hazardous waste includes pesticides, herbicides, solvents, paint thinners and engine oil. Hazardous Biosolids waste is any material that can catch fire, Port explode, corrode or is toxic. -
Anaerobic Digestion of Primary Sewage Effluent
Anaerobic Digestion of Primary Sewage Effluent Prepared for the U.S. Department of Energy Office of Electricity Delivery and Energy Reliability Under Cooperative Agreement No. DE-EE0003507 Hawai‘i Energy Sustainability Program Subtask 3.4: Biomass Submitted by Hawai‘i Natural Energy Institute School of Ocean and Earth Science and Technology University of Hawai‘i September 2014 Acknowledgement: This material is based upon work supported by the United States Department of Energy under Cooperative Agreement Number DE-EE0003507. Disclaimer: This report was prepared as an account of work sponsored by an agency of the United States Government. Neither the United States Government nor any agency thereof, nor any of their employees, makes any warranty, express or implied, or assumes any legal liability or responsibility for the accuracy, completeness, or usefulness of any information, apparatus, product, or process disclosed, or represents that its use would not infringe privately owned rights. Reference here in to any specific commercial product, process, or service by tradename, trademark, manufacturer, or otherwise does not necessarily constitute or imply its endorsement, recommendation, or favoring by the United States Government or any agency thereof. The views and opinions of authors expressed herein do not necessarily state or reflect those of the United States Government or any agency thereof. SUMMARY A hybrid system comprised an up-flow packed bed anaerobic reactor and a down-flow trickling-filter reactor connected in series was shown to effectively treat primary clarifier effluent. When a clarifier and sand filter were added to the system, the effluent water quality achieved values of BOD5 and TSS that were below the EPA’s water discharge limits of 30 mg/l and equivalent to highly efficient activated sludge systems. -
Phase Transitions in Multicomponent Systems
Physics 127b: Statistical Mechanics Phase Transitions in Multicomponent Systems The Gibbs Phase Rule Consider a system with n components (different types of molecules) with r phases in equilibrium. The state of each phase is defined by P,T and then (n − 1) concentration variables in each phase. The phase equilibrium at given P,T is defined by the equality of n chemical potentials between the r phases. Thus there are n(r − 1) constraints on (n − 1)r + 2 variables. This gives the Gibbs phase rule for the number of degrees of freedom f f = 2 + n − r A Simple Model of a Binary Mixture Consider a condensed phase (liquid or solid). As an estimate of the coordination number (number of nearest neighbors) think of a cubic arrangement in d dimensions giving a coordination number 2d. Suppose there are a total of N molecules, with fraction xB of type B and xA = 1 − xB of type A. In the mixture we assume a completely random arrangement of A and B. We just consider “bond” contributions to the internal energy U, given by εAA for A − A nearest neighbors, εBB for B − B nearest neighbors, and εAB for A − B nearest neighbors. We neglect other contributions to the internal energy (or suppose them unchanged between phases, etc.). Simple counting gives the internal energy of the mixture 2 2 U = Nd(xAεAA + 2xAxBεAB + xBεBB) = Nd{εAA(1 − xB) + εBBxB + [εAB − (εAA + εBB)/2]2xB(1 − xB)} The first two terms in the second expression are just the internal energy of the unmixed A and B, and so the second term, depending on εmix = εAB − (εAA + εBB)/2 can be though of as the energy of mixing. -
Grade 6 Science Mechanical Mixtures Suspensions
Grade 6 Science Week of November 16 – November 20 Heterogeneous Mixtures Mechanical Mixtures Mechanical mixtures have two or more particle types that are not mixed evenly and can be seen as different kinds of matter in the mixture. Obvious examples of mechanical mixtures are chocolate chip cookies, granola and pepperoni pizza. Less obvious examples might be beach sand (various minerals, shells, bacteria, plankton, seaweed and much more) or concrete (sand gravel, cement, water). Mechanical mixtures are all around you all the time. Can you identify any more right now? Suspensions Suspensions are mixtures that have solid or liquid particles scattered around in a liquid or gas. Common examples of suspensions are raw milk, salad dressing, fresh squeezed orange juice and muddy water. If left undisturbed the solids or liquids that are in the suspension may settle out and form layers. You may have seen this layering in salad dressing that you need to shake up before using them. After a rain fall the more dense particles in a mud puddle may settle to the bottom. Milk that is fresh from the cow will naturally separate with the cream rising to the top. Homogenization breaks up the fat molecules of the cream into particles small enough to stay suspended and this stable mixture is now a colloid. We will look at colloids next. Solution, Suspension, and Colloid: https://youtu.be/XEAiLm2zuvc Colloids Colloids: https://youtu.be/MPortFIqgbo Colloids are two phase mixtures. Having two phases means colloids have particles of a solid, liquid or gas dispersed in a continuous phase of another solid, liquid, or gas. -
Introduction to Phase Diagrams*
ASM Handbook, Volume 3, Alloy Phase Diagrams Copyright # 2016 ASM InternationalW H. Okamoto, M.E. Schlesinger and E.M. Mueller, editors All rights reserved asminternational.org Introduction to Phase Diagrams* IN MATERIALS SCIENCE, a phase is a a system with varying composition of two com- Nevertheless, phase diagrams are instrumental physically homogeneous state of matter with a ponents. While other extensive and intensive in predicting phase transformations and their given chemical composition and arrangement properties influence the phase structure, materi- resulting microstructures. True equilibrium is, of atoms. The simplest examples are the three als scientists typically hold these properties con- of course, rarely attained by metals and alloys states of matter (solid, liquid, or gas) of a pure stant for practical ease of use and interpretation. in the course of ordinary manufacture and appli- element. The solid, liquid, and gas states of a Phase diagrams are usually constructed with a cation. Rates of heating and cooling are usually pure element obviously have the same chemical constant pressure of one atmosphere. too fast, times of heat treatment too short, and composition, but each phase is obviously distinct Phase diagrams are useful graphical representa- phase changes too sluggish for the ultimate equi- physically due to differences in the bonding and tions that show the phases in equilibrium present librium state to be reached. However, any change arrangement of atoms. in the system at various specified compositions, that does occur must constitute an adjustment Some pure elements (such as iron and tita- temperatures, and pressures. It should be recog- toward equilibrium. Hence, the direction of nium) are also allotropic, which means that the nized that phase diagrams represent equilibrium change can be ascertained from the phase dia- crystal structure of the solid phase changes with conditions for an alloy, which means that very gram, and a wealth of experience is available to temperature and pressure. -
Settling Velocities of Particulate Systems†
Settling Velocities of Particulate Systems† F. Concha Department of Metallurgical Engineering University of Concepción.1 Abstract This paper presents a review of the process of sedimentation of individual particles and suspensions of particles. Using the solutions of the Navier-Stokes equation with boundary layer approximation, explicit functions for the drag coefficient and settling velocities of spheres, isometric particles and arbitrary particles are developed. Keywords: sedimentation, particulate systems, fluid dynamics Discrete sedimentation has been successful to 1. Introduction establish constitutive equations in processes using Sedimentation is the settling of a particle, or sus- sedimentation. It establishes the sedimentation prop- pension of particles, in a fluid due to the effect of an erties of a certain particulate material in a given fluid. external force such as gravity, centrifugal force or Nevertheless, to analyze a sedimentation process and any other body force. For many years, workers in to obtain behavioral pattern permitting the prediction the field of Particle Technology have been looking of capacities and equipment design procedures, an- for a simple equation relating the settling velocity of other approach is required, the so-called continuum particles to their size, shape and concentration. Such approach. a simple objective has required a formidable effort The physics underlying sedimentation, that is, the and it has been solved only in part through the work settling of a particle in a fluid is known since a long of Newton (1687) and Stokes (1844) of flow around time. Stokes presented the equation describing the a particle, and the more recent research of Lapple sedimentation of a sphere in 1851 and that can be (1940), Heywood (1962), Brenner (1964), Batchelor considered as the starting point of all discussions of (1967), Zenz (1966), Barnea and Mitzrahi (1973) the sedimentation process. -
Treatment and Biosolids Technologies
Treatment and Biosolids Technologies City of Morro Bay New Water Reclamation Facility Engineering Component of Siting Study • Project engineering team will look at the following parameters related to each site: – Range of cost for conveyance, treatment, and distribution to potential users – Land availability for range of treatment and biosolids management options • A range of treatment technologies can reach City objectives – Keep options open during preliminary planning Public Workshop Results Top‐Ranked Issues from Dot Exercise • Environmental – Avoid Visual Impacts • Cost Issues – Keep Costs Low (highest score) • Engineering and Design – Recharge Morro Aquifer Overview • Environmental – Effluent reuse goals – Quality and Quantity – Conveyance methods for recycled water • Cost Issues / Engineering and Design – Liquid treatment technologies – Biosolids processing technologies / products – Procurement Treatment Processes • Preliminary – Screening of large solids • Primary –Flotation & settling • Secondary – Biological Treatment Source of • Tertiary – Filtration Biosolids • Disinfection • Advanced – Salts – Contaminants of Emerging Concern Treatment Process Selection Driven by End Goals 1. Start with effluent reuse goals 2. Identify treatment technologies to meet those goals 3. Develop plan for handling biosolids from range of liquid treatment options Effluent Reuse Goals ‐ Quantity • “How much” varies seasonally • Evapotranspiration rates determine potential use for irrigation • Wet weather or production of “off‐spec” water often require -
Gp-Cpc-01 Units – Composition – Basic Ideas
GP-CPC-01 UNITS – BASIC IDEAS – COMPOSITION 11-06-2020 Prof.G.Prabhakar Chem Engg, SVU GP-CPC-01 UNITS – CONVERSION (1) ➢ A two term system is followed. A base unit is chosen and the number of base units that represent the quantity is added ahead of the base unit. Number Base unit Eg : 2 kg, 4 meters , 60 seconds ➢ Manipulations Possible : • If the nature & base unit are the same, direct addition / subtraction is permitted 2 m + 4 m = 6m ; 5 kg – 2.5 kg = 2.5 kg • If the nature is the same but the base unit is different , say, 1 m + 10 c m both m and the cm are length units but do not represent identical quantity, Equivalence considered 2 options are available. 1 m is equivalent to 100 cm So, 100 cm + 10 cm = 110 cm 0.01 m is equivalent to 1 cm 1 m + 10 (0.01) m = 1. 1 m • If the nature of the quantity is different, addition / subtraction is NOT possible. Factors used to check equivalence are known as Conversion Factors. GP-CPC-01 UNITS – CONVERSION (2) • For multiplication / division, there are no such restrictions. They give rise to a set called derived units Even if there is divergence in the nature, multiplication / division can be carried out. Eg : Velocity ( length divided by time ) Mass flow rate (Mass divided by time) Mass Flux ( Mass divided by area (Length 2) – time). Force (Mass * Acceleration = Mass * Length / time 2) In derived units, each unit is to be individually converted to suit the requirement Density = 500 kg / m3 . -
Partition Coefficients in Mixed Surfactant Systems
Partition coefficients in mixed surfactant systems Application of multicomponent surfactant solutions in separation processes Vom Promotionsausschuss der Technischen Universität Hamburg-Harburg zur Erlangung des akademischen Grades Doktor-Ingenieur genehmigte Dissertation von Tanja Mehling aus Lohr am Main 2013 Gutachter 1. Gutachterin: Prof. Dr.-Ing. Irina Smirnova 2. Gutachterin: Prof. Dr. Gabriele Sadowski Prüfungsausschussvorsitzender Prof. Dr. Raimund Horn Tag der mündlichen Prüfung 20. Dezember 2013 ISBN 978-3-86247-433-2 URN urn:nbn:de:gbv:830-tubdok-12592 Danksagung Diese Arbeit entstand im Rahmen meiner Tätigkeit als wissenschaftliche Mitarbeiterin am Institut für Thermische Verfahrenstechnik an der TU Hamburg-Harburg. Diese Zeit wird mir immer in guter Erinnerung bleiben. Deshalb möchte ich ganz besonders Frau Professor Dr. Irina Smirnova für die unermüdliche Unterstützung danken. Vielen Dank für das entgegengebrachte Vertrauen, die stets offene Tür, die gute Atmosphäre und die angenehme Zusammenarbeit in Erlangen und in Hamburg. Frau Professor Dr. Gabriele Sadowski danke ich für das Interesse an der Arbeit und die Begutachtung der Dissertation, Herrn Professor Horn für die freundliche Übernahme des Prüfungsvorsitzes. Weiterhin geht mein Dank an das Nestlé Research Center, Lausanne, im Besonderen an Herrn Dr. Ulrich Bobe für die ausgezeichnete Zusammenarbeit und der Bereitstellung von LPC. Den Studenten, die im Rahmen ihrer Abschlussarbeit einen wertvollen Beitrag zu dieser Arbeit geleistet haben, möchte ich herzlichst danken. Für den außergewöhnlichen Einsatz und die angenehme Zusammenarbeit bedanke ich mich besonders bei Linda Kloß, Annette Zewuhn, Dierk Claus, Pierre Bräuer, Heike Mushardt, Zaineb Doggaz und Vanya Omaynikova. Für die freundliche Arbeitsatmosphäre, erfrischenden Kaffeepausen und hilfreichen Gespräche am Institut danke ich meinen Kollegen Carlos, Carsten, Christian, Mohammad, Krishan, Pavel, Raman, René und Sucre.