THINK FLUID DYNAMIX CFD Simulation of Clarifiers. THINK Fluid Dynamix

Similar documents
THINK Fluid Dynamix THINK FLUID DYNAMIX. CFD for Aeration Applications

THINK FLUID DYNAMIX Mixing, Homogenization & Blend Time. THINK Fluid Dynamix

Sedimentation. Several factors affect the separation of settleable solids from water. Some of the more common types of factors to consider are:

Chapter 6: Solid-Liquid Separation in WWTPs. Raúl Muñoz Pedro García Encina

SEDIMENTATION INTRODUCTION

L-10 SEDIMENTATION PART-I

Module 15 : Grit Chamber. Lecture 19 : Grit Chamber

15. GRIT CHAMBER 15.1 Horizontal Velocity in Flow Though Grit Chamber

Module 15 : Grit Chamber. Lecture 19 : Grit Chamber

Alonso G Griborio, PhD, PE 1 Randal W Samstag, MS, PE, BCEE 2. Hazen and Sawyer, Hollywood, FL, US

PRIMARY TREATMENT NATURE

A novel methodology for the calibration of discrete settling behaviour of activated sludge

6 SETTLING TESTS 6.1 INTRODUCTION. Authors: Elena Torfs Ingmar Nopens Mari K.H. Winkler Peter A. Vanrolleghem Sophie Balemans Ilse Y.

Separation Processes: Sedimentation Separations

Discrete particle settling. Flocculent settling. Compression

SETTLING VELOCITY OF PARTICLES

ABSTRACT INTRODUCTION

THEORY: SETTLING PROCESSES

Effect of Particle Drag on Performance of a Conical Base Classifier

Sedimentation of Activated Sludge in Secondary Clarifiers

What do I need to know to pass an Advanced Industrial Wastewater License Test?

Modelling hindered batch settling Part I: A model for linking zone settling velocity and stirred sludge volume index

Development of a Laboratory Clarifier Test to Predict Full Scale Primary Clarifier Performance

Treatment Processes. Coagulation. Coagulation. Coagulation. Coagulation. Coagulation and Flocculation

Water Pollution Control: Physical Methods. AWPPCE RPI Fall 2013

INTRODUCTION AND OVERVIEW

Introduction of Equivalent shape factors for investigating settling Velocity in thickeners

Water & Wastewater Mixing: Lighting Up A Dark Art (or cramming a quart into a pint pot!)

L-17 Coagulation and Flocculation Part-I. Environmental Engineering-I

AWT & Conventional Mixed Liquor Settling Velocities. Richard O. Mines, Jr. Mercer University Jeffrey L. Vilagos City of Tampa

Chapter XII. Special Topics Report Centrifuge Settling & Filtration Theory

FINITE ELEMENT SIMULATION OF UNSTEADY FLOWS IN SECONDARY SETTLING TANKS

Calculation of Sand Losses During Hopper Loading Process in Trailers

Water & Wastewater Mixing (WWM)

Modelling and Advanced Control of a Biological Wastewater Treatment Plant

Secondary Clarifier Modeling: A Multi-Process Approach

Introduction to Mechanical Process Engineering WS 2013/2014

Delvin DeBoer, Ph.D., PE. MN/ND/SD SWTW April 29, 2014 OUTLINE

WEF Residuals and Biosolids Conference 2017

CFD for Wastewater Case Studies: Sedimentation, Mixing and Disinfection

Simplified Model of WWER-440 Fuel Assembly for ThermoHydraulic Analysis

D.R. Rector, M.L. Stewart and A.P. Poloski Pacific Northwest National Laboratory P.O. Box 999, Richland, WA

MODELING FLOCCULATION IN SEDIMENTATION TANK WITH DEPTH-AVERAGED METHOD

industrial wastewater applications of coagulants and flocculants

Research Article Rheology Measurements for Online Monitoring of Solids in Activated Sludge Reactors of Municipal Wastewater Treatment Plant

Investigation into Sand Deposition and Transportation in Multiphase Pipelines Phase 2

Modeling the Transition from Zone Settling to Compression of a Bulking Activated Sludge

The Operator s Guide to Monitoring Secondary Clarifier Performance

Real Time Control to increase Hydraulic Capacity of Wastewater Treatment Plants during rain

Published in: International Association for Hydraulic Research, XXIV Congress, Madrid, Sep 1991

Critical analysis of constitutive functions for hindered settling velocity in 1-D settler models

BAE 820 Physical Principles of Environmental Systems

Week 7 Assignment 7. The due date for submitting this assignment has passed NPTEL - Privacy & Terms - Honor Code - FAQs - Funded by

Fundamental Concepts: Sedimentation

SUMMARY OF KEY WASTEWATER COLLECTION MATH FORMULAS. 1. Mass, Lbs/Day = (Vol, MGD) x ( Conc., mg/l) x ( 8.34 lbs/gal)

Principles of Convection

A UNIQUE METHOD TO CONTROL SETTLING OF FIRST CARBONATION JUICE

The Islamic University of Gaza- Civil Engineering Department Sanitary Engineering- ECIV 4325 L7. Physical Wastewater Treatment

TPDES: Soil, Erosion and Sedimentation Methods

THE RESEARCH OF ACTIVATED SLUDGE DEWATERING PROCESSES.

CEE 370 Environmental Engineering Principles

Proppant Transport & Screenout Behavior. R.D. Barree

Sedimentation. Treatment Processes. Sedimentation. Sedimentation. Sedimentation. Sedimentation. CIVL 1112 Water Treatment - Sedimentation 1/7

These subclasses are to be used according to the following general rules:

1. The Properties of Fluids

CEE 370 Environmental Engineering Principles

Technology offer: Wastewater treatment by electrocoagulation (EC)

Poly Prep N Floc. Part No Instruction Manual. Updated 6/2/2009 Ver. 2.0

Development of a dynamic process model for the mechanical fluid separation in decanter centrifuges

10 TH EUROPEAN WASTE WATER CONFERENCE DEVELOPMENT OF FLOCCULATION MODELS FOR IMPROVING WATER TREATMENT

Centrifugation. Tubular Bowl Centrifuge. Disc Bowl Centrifuge

DYNAMIC MODELING OF FILAMENTOUS BULKING IN LAB-SCALE ACTIVATED SLUDGE PROCESSES

ADVANCED SEPARATION TECHNOLOGY APPLICATION FOR NOM REMOVAL FROM A FRESHWATER SUPPLY

Pharmaceutics I. Unit 6 Rheology of suspensions

Lecture 3: Coagulation and Flocculation

An introduction to particle size characterisation by DCS:

LIQUID/SOLID SEPARATIONS Filtration, Sedimentation, Centrifuges Ron Zevenhoven ÅA Thermal and Flow Engineering

Experiments at the University of Minnesota (draft 2)

Centrifugation. There are several process functions using centrifuges in biotech separation. These are listed below.

ENVE 411 Water Engineering Design

MRI Flocculation. MRI Flocculation Systems. Mix & Match for Maximum Pretreatment Control

Modeling of Sedimentation Process in Water

1 Turbidity = NTU 2pH = 3 Alkalinity = mg/l as CaCO 3 4 Temperature = 5 Fe mg/l 6 Mn mg/l 7 Total Hardness mg/l as CaCO 3

Solutions for Tutorial 3 Modelling of Dynamic Systems

MEANDER CURVE (MODIFIED FOR ADEED)

Optimization of a Flocculation-Sedimentation Treatment Plant with Computational Fluid Dynamics

CREAM SEPARATION. Centrifugation. Chapter 8

The Art of Mixing, Anaerobic Digesters

sedimentation Experimental design analysis applied to factors related to migration of sediment out of a stormwater catchbasin sump

Numerical Analysis of Type I Settling

5 BATCH MLSS SETTLING EVALUATION

Floc Strength Scale-Up: A Practical Approach

Title: Centrifuge Optimization. Decanter Centrifuges for Municipal Sludge Dewatering

INDBOND 3000 Dry Strength Resin for Paper

15. Physics of Sediment Transport William Wilcock

Effect of solution physical chemistry on the rheological properties of activated sludge

US ARMY INTELLIGENCE CENTER CIRCUITS

ENVIRONMENTAL ENGINEERING. Chemical Engineering department

1 Turbidity = NTU 2 ph = Alkalinity = 34 mg/l as CaCO 3 4 Temperature = 5 Fe = 2 mg/l 6 Mn = mg/l 7 Total Hardness = 50mg/l as CaCO 3

Table of Contents. Preface... xiii

Transcription:

THINK FLUID DYNAMIX CFD Simulation of Clarifiers

Provided by: THINK Fluid Dynamix Am Pestalozziring 21 D-91058 Erlangen (Germany) Tel. +49 (0)9131 69098-00 http://www.think-fd.com CFD ENGINEERING & CONSULTING THINK Fluid Dynamix is the CFD based engineering and consulting business unit of INVENT Umwelt- und Verfahrenstechnik AG.

Definitions & Concepts - What is a clarifier? - Which is its principle of operation? Clarifiers are settling tanks built with mechanical means for continuous removal of solids being deposited by sedimentation. Gravity separation of solids from liquid, producing a clarified overflow and a thickened solids underflow, has long been used in the wastewater treatment industry. The shape of the clarifier determines whether the actual flow pattern approaches radial or plug-flow. Circular and rectangular clarifiers are the most popular. Circular clarifiers show a more reliable sludge-collecting performance while rectangular clarifiers can help to save surface area in the plant. - Which are the most common shapes? Example of rectangular clarifier Copyright: 3

PRIMARY SEDIMENTATION Definitions & concepts - Types of clarifiers The objective of treatment by sedimentation is to remove readily settleable solids and floating material found in wastewater and thus reduce the suspended solids content. Efficiently designed and operated primary sedimentation tanks, can remove 50 to 70 percent of the suspended solids and from 25 to 40 percent of the BOD. SECONDARY SEDIMENTATION For activated sludge sedimentation tanks, the primary function is the removal of biological floc from the liquid stream. By means of gravity settling it is possible to remove over 99.5 percent of the mixed liquor TSS from the treated effluent. A secondary function is the thickening of the settled activated sludge to reduce the volume before returning it to the process for mixing and treatment with the influent wastewater. Copyright: 4

SEDIMENTATION PROCESS Settling theory - Types of settling based on solids concentration and flocculation tendency Settling basins handling wastewater must separate a variety of materials in the clarification zone. Depending on the concentration of the suspended solids and the tendency of the particles to flocculate, four distinct types of settling processes are typically recognized in wastewater treatment plant design: TYPE I: DISCRETE NONFLOCCULENT SETTLING The settling of discrete, nonflocculating particles can be analyzed by means of the classic laws of sedimentation formed by Newton and Stokes. These particles settle independently at their terminal velocity. Newton s law yields the terminal particle velocity be equating the gravitational force of the particle to the frictional resistance, or drag. TYPE II: FLOCCULENT SETTLING Particles in relatively dilute solutions will not act as discrete particles but will coalesce during sedimentation. As coalescence or flocculation occurs, the mass of the particle increases, and it settles faster. As the settling velocities of the aggregates formed change with time and a strict mathematical solution is not possible, laboratory testing is required to characterize the settling behavior. Copyright: 5

TYPE III: HINDERED SETTLING OR ZONE SETTLING Settling theory - Types of settling based on solids concentration and flocculation tendency - Sludge Rheology Type III settling is the predominant mechanism in secondary clarifiers. The solid concentration is much higher than in discrete or flocculent processes. As a result, the contacting particles tend to settle as a zone or blanket and maintain the same position relative to each other. TYPE IV: COMPRESSION SETTLING Particles have reached such a concentration that a structure is formed and further settling can only occur by compression. This type of settling typically occurs in the lower layers of a deep sludge mass such as near to bottom of secondary clarifiers and sludge thickeners. SLUDGE RHEOLOGY Wastewater sludges behave as non-newtonian fluids at high solids concentration such as those often found at the bottom of the sludge blanket. This has an important implication in collection and removal of thickened sludge. Geinopolos and Katz (1964) showed that primary, secondary, and also digested sludges behave as visco-plastic materials. Copyright: 6

Measurement of Sludge Settleability - Sludge Volume Index Sludge settleability is central to the health of the biological system. Poor settling sludge causes lower underflow (RAS) solids concentration because of poor compaction. As fewer solids are removed from the tank than applied to it, the sludge blanket can propagate to the surface of the clarifier, resulting in loss of solids in the effluent. Consequently, measuring sludge settleability is fundamental to the operation and control of the biological system. Sludge Volume Index Historically, the SVI has been used most commonly as a measurement of sludge settleability. It is the volume in milliliters occupied by 1gramm of a suspension after 30 minutes of settling. Standard methods specifies gently stirring the sample during settling to eliminate or minimize wall effects. Dick and Vesilind (1969) noted that, for the same samples, slow stirring yielded consistently lower SVI values than the unstirred tests. Copyright: 7

Numerical Modeling - What is CFD? Computational Fluid Dynamics (CFD) is an advanced computer-based technique which uses numerical procedures to solve and analyze problems that involve fluid flow. Numerical simulations are the perfect environment to identify problems, to perform parameter studies and to optimize existing designs. Copyright: 8

Computational Fluid Dynamics - How to model settling tanks? An accurate CFD simulation of a settling tank requires the following models: 3 Dimensional domain Time-dependent analysis Motion of mechanical parts Multiphase modeling Settling model (which takes into account flocculation and rheology effects) Copyright: 9

Numerical Modeling - Settling behavior - Sludge Volume Index CFD animation in YouTube The results obtained by settling test (such as the SVI) carried out in a laboratory can be also numerically reproduced by means of a Multiphase Simulation. By proper setup of the numerical parameters a correct agreement between numerical and physical test can be achieved. The accurate modeling of the settling characteristics of solid matter in the clarifier is essential in order to produce reliable results and been able to simulate the process operation correctly. Copyright: 10

Simulation of Reactor Operation Correct set of parameters based on experimental data For any clarifier, the sludge settling characteristics can be numerically modeled based on experimental data such as the SVI and the average Total Suspended Solids at the inlet. After all process parameters are correctly defined an accurate simulation of the reactor operation is possible. Copyright: 11

Real Time Simulation An unparalleled way of studying and understanding process operation CFD animation in YouTube High resolution real time simulations open up completely new ways to study and to understand process operation: the evolution of the TSS profile can be analyzed over time for the complete system and the solid concentration can be tracked for all outlets. Time fluctuations of the flow velocity field can be studied as well as the the motion of the mechanical scrappers and their influence on the system. Copyright: 12

Simulation of Rectangular Clarifiers Study of velocity and solid concentration field in real time. CFD animation in YouTube In many plants around the world, rectangular clarifiers can be found. They offer many advantages such as the need for less land and construction costs in multiple unit design, and there are less chance for short-circuiting. On the other hand they have the disadvantage of longer detention time for settled sludge. With real-time CFD simulation the operation of the basin and the degree of solids removal can be studied, issues can be identified and non-optimal designs can be optimized. Copyright: 13

Modeling of Clarifiers A new way of studying process operation A new way of design and optimization Numerical simulations are the perfect environment for identification of problems, parameter studies and optimization work Accurate modeling of sludge and their settling characteristics based on experimental data Real time simulation of the process Simulation and analysis of the motion of mechanical parts (scrappers) and their effects on the reactor behavior Full description of velocity and concentration field over entire reactor space and physical time Copyright: 14

Technical Competence Company Video in YouTube THINK Fluid Dynamix offers support and assistance with the design, optimization, and modernization of hydraulic structures in water and wastewater treatment plants. More than 25 years of experience innovating and developing revolutionary solutions allow us to provide unique and in-depth analysis and solutions. We have a comprehensive functional and industrial expertise, and are passionate about taking on challenges that matter to our clients and to the environment. The design of optimized process applications and hydraulic structures for the water and wastewater treatment industry requires a high level of multidisciplinary scientific and engineering skills. An optimal solution should show energy efficiency while maintaining a robust and reliable system approach Copyright: 15

Sources: Metcalf & Eddy (2014), Wastewater Engineering, 5 th ed. T. E. Wilson (2005), Clarifier Design, 2 nd Edition THINK Fluid Dynamix Am Pestalozziring 21 D-91058 Erlangen (Germany) Tel. +49 (0)9131 69098-00 www.think-fd.com