The Art of Mixing, Anaerobic Digesters

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

Floc Strength Scale-Up: A Practical Approach

Water & Wastewater Mixing (WWM)

ENGG 199 Reacting Flows Spring Lecture 2b Blending of Viscous, Non-Newtonian Fluids

WEF Residuals and Biosolids Conference 2017

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

Nirma University Institute of Technology Chemical Engineering Department, Handouts -RRP- CRE-II. Handouts

Slurry Pump Mixing Effectiveness in Tank 50H

1. Starting of a project and entering of basic initial data.

Chemical Reaction Engineering

Effect of radius ratio on pressure drop across a 90 bend for high concentration coal ash slurries

Effect of Shape and Flow Control Devices on the Fluid Flow Characteristics in Three Different Industrial Six Strand Billet Caster Tundish

Assessing Mixing Sensitivities for Scale-up. Matthew Jörgensen Atlanta, 10/20/2014

Rheological Characterisation of blends of Primary and Secondary Sludge

INTRODUCTION TO MULTIPHASE FLOW. Mekanika Fluida II -Haryo Tomo-

L-10 SEDIMENTATION PART-I

THINK FLUID DYNAMIX CFD Simulation of Clarifiers. THINK Fluid Dynamix

mixing of fluids MIXING AND AGITATION OF FLUIDS

Proppant Transport & Screenout Behavior. R.D. Barree

CFD for Wastewater Case Studies: Sedimentation, Mixing and Disinfection

IMPROVING MIXING PROCESSES FOR INDUSTRIAL APPLICATIONS

APPLICATION OF MODELS WITH DIFFERENT COMPLEXITY FOR A STIRRED TANK REACTOR

Study on residence time distribution of CSTR using CFD

Optimum Configuration of a Double Jet Mixer Using DOE

Improving the Accuracy of Computational Fluid Dynamics Simulations of Nuclear Waste Mixing using Direct Numerical Simulations

PLO MIXING AND RTD IN TANKS: RADIOTRACER EXPERIMENTS AND CFD SIMULATIONS

Direct numerical simulation (DNS) investigation of turbulent open channel flow of a Herschel Bulkley fluid

EFFECT OF DISTRIBUTION OF VOLUMETRIC HEAT GENERATION ON MODERATOR TEMPERATURE DISTRIBUTION

Separationsteknik / Separation technology

Turbulent Compressible Flow in a Slender Tube

AGITATION AND AERATION

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

Module 15 : Grit Chamber. Lecture 19 : Grit Chamber

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

Heat Transfer Coefficient Solver for a Triple Concentric-tube Heat Exchanger in Transition Regime

A First Course on Kinetics and Reaction Engineering Example 11.5

Design advances and operational studies for the True Pipe Sampler: A symmetry based unit for reliable sampling of pressurised particulate

Initial and Boundary Conditions

On the Rheological Parameters Governing Oilwell Cement Slurry Stability

The need for increased accuracy of sampling in a mining

STRUCTURAL ANALYSIS OF A WESTFALL 2800 MIXER, BETA = 0.8 GFS R1. By Kimbal A. Hall, PE. Submitted to: WESTFALL MANUFACTURING COMPANY

Particles Removal from a Moving Tube by Blowing Systems: A CFD Analysis

Modelling of dispersed, multicomponent, multiphase flows in resource industries Section 4: Non-Newtonian fluids and rheometry (PART 1)

SETTLING VELOCITY OF PARTICLES

EVALUATION OF SLUDGE REMOVAL CAPABILITIES FOR ADMP MIXER IN TANK 18

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

Investigation of cake deposition on various parts of the surface of microfiltration membrane due to fouling

by Wensheng Zhang, Fuping Hao, Yoko Pranolo, Chu Yong Cheng, and Dave Robinson Presented by Wensheng Zhang 8 July 2011

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

BASIC DESIGN EQUATIONS FOR MULTIPHASE REACTORS

Introduction to Turbulence AEEM Why study turbulent flows?

Numerical investigation of solid-liquid two phase flow in a non-clogging centrifugal pump at offdesign

Liquid Feed Injection in a High Density Riser

MODA. Modelling data documenting one simulation. NewSOL energy storage tank

VISIMIX LAMINAR. MODELING OF A STAGNANT ZONE FORMATION AS A RESULT OF INEFFICIENT MIXING.

A First Course on Kinetics and Reaction Engineering Unit 33. Axial Dispersion Model

Numerical Modeling of Sampling Airborne Radioactive Particles Methods from the Stacks of Nuclear Facilities in Compliance with ISO 2889

(Refer Slide Time: 4:41)

ScienceDirect Abstract

Numerical Study of Pressure and Velocity Distribution Analysis of Centrifugal Pump

DYNAMIC STRESS MEASUREMENT OF CENTRIFUGAL COMPRESSOR IMPELLER AND STUDY FOR STRENGTH CRITERIA BASED ON CORRELATION BY UNSTEADY CFD

Technical Paper. Spray Granulation Gives Solid Materials Customized. The properties of spray-granulated products can be as varied as their appearance

Chapter (4) Motion of Fluid Particles and Streams

Applied CFD Project 1. Christopher Light MAE 598

Innovation in. Motionless Mixers

Control Loop Investigations

BAE 820 Physical Principles of Environmental Systems

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

Phone: , For Educational Use. SOFTbank E-Book Center, Tehran. Fundamentals of Heat Transfer. René Reyes Mazzoco

FLUID MECHANICS D203 SAE SOLUTIONS TUTORIAL 2 APPLICATIONS OF BERNOULLI SELF ASSESSMENT EXERCISE 1

RHEOLOGY AND MIXING OF SUSPENSION AND PASTES. Pr Ange NZIHOU, EMAC France

Design of Monoblock Centrifugal Pump Impeller

1) Batching Methods (Add Weigh or Loss In Weight) based on batch dispensing time, time between batches, head room, floor space, accuracy and budget.

Effect of Particle Drag on Performance of a Conical Base Classifier

WASTEWATER SLUDGE PIPELINE PREDICTIONS USING CONVENTIONAL VISCOMETRY AND ULTRASOUND BASED RHEOMETRY

AGITATION/GAS-LIQUID DISPERSION. CHEM-E Fluid Flow in Process Units

ENVIRONMENTAL FLUID MECHANICS

ABSTRACT I. INTRODUCTION

INTERNAL FLOW IN A Y-JET ATOMISER ---NUMERICAL MODELLING---

Shear stress and shear rates for µ-slides y-shaped based on Computational Fluid Dynamics (CFD)

Flow Field Investigation in a Rectangular Shallow Reservoir using UVP, LSPIV and numerical model

Prediction of Axial Compressor Blade Vibration by Modelling Fluid-Structure Interaction

MIXING IN WATER SUPPLY SERVICE TANKS AND RESERVOIRS

Effect of additives on suspension pipe flow

CFD Analysis and Experimental Evaluation of the Effective Parameters on Paint Homogeneity in Mixing Tanks

An Overview of Impellers, Velocity Profile and Reactor Design

3 Energy Exchange in Turbomachines

A new jet-stirred reactor for chemical kinetics investigations Abbasali A. Davani 1*, Paul D. Ronney 1 1 University of Southern California

Mass Balance MATHEMATICAL MODEL FOR THERMAL CRACKING OF HYDROCARBONS ETHANE CRACKING

Applied chemical process

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

CFD Simulation in Helical Coiled Tubing

MASS, MOMENTUM, AND ENERGY EQUATIONS

Respect the Rheology!

Effect of a Continuous Feed on the Fluid-Dynamics of a Mechanically Stirred Tank

Determining of the Residence Time Distribution in CPC reactor type

Numerical Simulation: Effects of Gas Flow and Rf Current Direction on Plasma Uniformity in an ICP Dry Etcher

Polymer Applications Understanding Polymer Activation. Presented by Rich Hopkins February 15, 2011

Engineering Theory of Leaching

Numerical Comparison of Rushton Turbine and CD-6 Impeller in Non-Newtonian Fluid Stirred Tank Akhilesh Khapre, Basudeb Munshi

Transcription:

The Art of Mixing, Anaerobic Digesters Dr Hara Papachristou Process Engineer hpapachristou@bhrgroup.co.uk 25th October 2011 BHR Group 2011 BHR Group is a trading name of VirtualPiE Limited www.bhrgroup.com

Aims Highlight the importance of getting digester mixing right Provide an overview of the current state of the art in digester mixing BHR Group 2011 2

Contents Importance of digester mixing Mixing objectives and design criteria Measuring and modelling mixing performance Digester mixing state of the art Digester and Sludge Mixing Software BHR Group 2011 3

Background Increasing number of digesters, mixing and holding tanks are in use Wide range of mixer types/sizes Few mixing criteria established or applied Reliance on mixer suppliers, no independent design information No link between rheology and mixer sizing Variable success of installed mixers BHR Group 2011 4

Industry Needs Why is mixing so increasingly important? Thicker feed sludges to improve throughput, leading to thicker digestate Smooth out variability in feed physical properties Maximise gas production Maintain uniform digester temperature Avoid built-up deposits on digester floor Dilute inhibitory substances entering digester Avoid short circuiting to maximise pathogen kill BHR Group 2011 5

Mixing Objectives What should the mixer achieve? Blending feed sludge into the bulk Generate the desired flow pattern Minimise dead or stagnant zones Avoid solids accumulation Scum drawdown Enable tank emptying BHR Group 2011 6

Defining Mixing Criteria Feed Slurry Blending Blend Time: time taken to achieve a predetermined degree of concentration homogeneity 90% blend time: the time taken for concentration fluctuation to be within +/- 10% of the mean concentration Typically, 90% or 95% blend times of 1 to 2 hours are specified for digesters Active volume The non stagnant volume Typically, 90% or 95% specified Extend of short circuiting BHR Group 2011 7

Modelling Performance Published Design Information Digester mixer design Chemical process mixer design Physical Modelling Clear simulants for slurry & feed Velocity and blend time measurements Wash out curves Computational Fluid Dynamics Flow patterns, velocities and blending BHR Group 2011 8

Digester Mixer Design Consideration Digester shape (base & aspect ratio) Feed & digestate rheology Location of inlets & outlets Digester feed rate & cycle Digester flow pattern & residence time Mixer type and size BHR Group 2011 9

State of the Art Feed location BHR Group 2011 10

State of the Art Impellers BHR Group 2011 11

State of the Art Jets BHR Group 2011 12

State of the Art (a) Sparger A Unconfined Gas Continuous or sequential gas addition through the nozzles No difference for low viscosity digestate Sequential superior for high viscosity digestate x x Inlet position (b) Sparger B 6 7 5 11 12 x 9 8 4 10 1 Inlet position x 3 2 BHR Group 2011 13

WWM Scope for Digester Mixing CR8239 Sludge Tank & Digester Mixing Research Report CR8237 Digester & Sludge Tank Mixing Design Guide Mixer design, rating, and selection guide Linked to performance criteria Sludge rheology dependent Based on physical modelling and CFD BHR Group 2011 14

Digester & Sludge Tank Mixing Software Aims: Enable easier and practical application of the paper design guidelines Allow range of mixing scenarios based on combinations of different tank geometries, sludge properties, mixer type Allow rating of digester mixing performance BHR Group 2011 15

Digester & Sludge Tank Mixer Software Excel based software Non newtonian fluids (Power Law and Herschel Bulkley) Transitional and turbulent regimes Jet and submersible mixers Impeller mixers (focus on axial impellers) Unconfined gas mixers Two primary criteria Blend time Active or cavern volume calculations BHR Group 2011 16

Digester & Sludge Tank Mixer Software BHR Group 2011 17

Digester & Sludge Tank Mixer Software BHR Group 2011 18

Digester & Sludge Tank Mixer Software BHR Group 2011 19

Thank you Hara Papachristou email: hpapachristouh@bhrgroup.co.uk Water, Environment & Power (WEP) Fluid Systems Academy Process Enquiries: contactus@bhrgroup.co.uk BHR Group 2011 BHR Group is a trading name of VirtualPiE Limited www.bhrgroup.com