Agitator Design for Gas-Liquid Fermenters and Bioreactors

Agitator Design for Gas-Liquid Fermenters and Bioreactors
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This book is concise reference to designing mechanically sound agitation systems that will perform the process function efficiently and economically. Currently, all the books on bioreactor and fermenter design do not focus specifically on agitation. Sections cover agitator fundamentals, impeller systems, optimum power and air flow at peak mass transfer calculations, optimizing operation for minimum energy per batch, heat transfer surfaces and calculations, shaft seal considerations, mounting method, mechanical design, and vendor evaluation.

Оглавление

Gregory T. Benz. Agitator Design for Gas-Liquid Fermenters and Bioreactors

Table of Contents

List of Tables

List of Illustrations

Guide

Pages

Agitator Design for Gas–Liquid Fermenters and Bioreactors

Preface

Foreword

Foreword for Greg Benz

1 Purpose of Agitator Design

References

2 Major Steps in Successful Agitator Design

Define Process Results

Define Process Conditions

Choose Tank Geometry

Calculate Equivalent Power/Airflow Combinations for Equal Mass Transfer Rate

Choose Minimum Combined Power

Choose Shaft Speed; Size Impeller System to Draw Required Gassed Power

Decision Point: D/T and Gassing Factors OK?

Mechanical Design

Decision Point: Is the Mechanical Design Feasible?

Repeat to Find Lowest Cost

Repeat for Different Aspect Ratios

Repeat for Different Process Conditions

Finish

Summary of Chapter

List of Symbols

References

3 Agitator Fundamentals

Agitated Tank Terminology

Prime Mover

Reducer

Shaft Seal

Wetted Parts

Tank Dimensions

How Agitation Parameters Are Calculated

Reynolds Number

Power Number

Pumping Number

Dimensionless Blend Time

Aeration Number

Gassing Factor

Nusselt Number

Froude Number

Prandtl Number

Geometric Ratios

Baffle Number

Dimensionless Hydraulic Force

Thrust Number

Typical Dimensionless Number Curves

Example 1: Power Draw Calculation

Answer

Example 2: Pumping Calculation

Answer

Example 3: Blend Time Calculation

Answer

A Primer on Rheology

Newtonian Model

Pseudoplastic or Shear Thinning, Model (Aka Power Law Fluid)

Bingham Plastic

Herschel–Bulkley

Impeller Apparent Viscosity

A Bit of Impeller Physics

Summary of Chapter

List of Symbols

Greek letters

References

4 Agitator Behavior under Gassed Conditions

Flooding

kla Method

Power Draw Method

Visual Flow Pattern Method

Effect on Power Draw

Holdup

Example of Holdup Calculation

Holdup “War Story”

Variable Gas Flow Operation

Mechanical Effects

Summary of Chapter

List of Symbols

References

5 Impeller Types Used in Fermenters

Impeller Flow Patterns

Axial Flow

Radial Flow

Mixed Flow

Chaos Flow

Examples of Axial Flow Impellers. Low Solidity

High Solidity

Example

Up‐pumping vs. Down Pumping

Examples of Radial Flow Impellers

Straight Blade Impeller

Disc, aka Rushton, Turbines

Example

Smith Turbines

CD‐6 Turbine by Chemineer; aka Smith Turbine by Many Manufacturers

Example

Deeply Concave Turbines

Deep Asymmetric Concave Turbine with Overhang (BT‐6)

Examples of Mixed Flow Impellers

Examples of Chaos Impellers

Shear Effects

Specialty Impellers

Summary of Chapter

List of Symbols

References

6 Impeller Systems

Why Do We Need a System?

Reaction Engineering

Fermenter History

Steps to Impeller System Design

Choose Number of Impellers

Choose Placement of Impellers

Choose Type(s) of Impellers

Choose Power Split or Distribution Among Impellers

Choose D/T and/or Shaft Speed

D/T Effects with Variable Gas Flowrates

Example 6.1

Example 6.2

Conclusions on D/T Ratio

Design to Minimize Shear Damage

Sparger Design

Ring Sparger

Pre‐dispersion

Fine Bubble Diffuser

Summary of Chapter

List of Symbols

References

7 Piloting for Mass Transfer

Why Pilot for Mass Transfer

Methods for Determining kla

Sulfite Method

Dynamic Method; aka Dynamic Gassing/Degassing Method

Steady‐State Method; aka Mass Balance Method

Combined Dynamic and Steady‐State Method

Equipment Needed for Scalable Data

Data Gathering Needs

Experimental Protocol

Example Problem: Experimental Protocol for Steady‐State Analysis

Summary of Chapter

List of Symbols

References

8 Power and Gas Flow Design and Optimization. What This Chapter Is about

Where We Are in Terms of Design

Design with no Data

Example of Procedure

Design with Limited Pilot Data

Design with Full Data

Choose Minimum Combined Power

Example Problem

State of Design Completion

Additional Considerations

Summary of Chapter

List of Symbols

References

9 Optimizing Operation for Minimum Energy Consumption per Batch. Purpose of This Chapter

Prerequisite

Conceptual Overview

Detailed Procedure

Example Problem

Minimizing Total Energy Usage

Practical Design

Additional Considerations

Summary of Chapter

List of Symbols

References

10 Heat Transfer Surfaces and Calculations. Purpose of This Chapter

Design Philosophy

Overview of the Problem

Heat Sources

Cooling Sources

Heat Exchange Surface Overview

Principle of Heat Transfer Calculation

Calculations By Type of Surface. Vessel Jacket, Agitated Side

Simple Unbaffled Jacket, Jacket Side

Dimple Jacket, Jacket Side

Half‐Pipe Coil, Jacket Side

Helical Coil, Inside

Helical Coil, Process Side

Vertical Tube Bundle, Inside

Vertical Tube Bundle, Process Side

Plate Coil, Inside

Plate Coil, Process Side

Example Problem: Vertical Tube Bundle. Problem Statement

Problem Solution

Additional Consideration: Effect on Power Draw

Additional Consideration: Forces on Heat Exchange Surfaces Used as Baffles

Additional Consideration: Wall Viscosity

Additional Consideration: Effect of Gas

External Heat Exchange Loops

Summary of Chapter

List of Symbols

References

Further Readings

11 Gasses Other Than Air and Liquids Other Than Water

General Principle

Comments on Some Specific Gasses. Ammonia

Carbon Dioxide

Carbon Monoxide

Hydrogen

Methane

Oxygen

Economic Factors

Disposal Factors

Effects of Different Gasses on kla

Effects of Different Gasses on Driving Force

Operating Condition Effects

Constraints on Outlet Concentration

Safety

Liquids Other Than Water

Summary of Chapter

List of Symbols

References

12 Viscous Fermentation. General Background

Sources of Viscosity

Viscosity Models for Broths

Effect of Viscosity on Power Draw

Example Problem

Example Problem Answer

Effect of Viscosity on kla

Effect of Viscosity on Holdup

Effect of Viscosity on Blend Time

Effect of Viscosity on Flooding

Caverns

Estimating Cavern Size

Xanthan and Gellan Gums

Viscosity Models for Gums

Installation Survey

Effect of D/T and No. and Type of Impellers on Results in Xanthan Gum

Production Curve

Heat Transfer

All‐Axial Impeller Design

Invisible Draft Tube vs. Axial/Radial Combination

Mycelial Broths

Typical Viscosity Model

Morphology Effects

Recommendations

Summary of Chapter

List of Symbols

References

13 Three Phase Fermentation

General Problem

Effect on Mass Transfer

Effect on Foam

Emulsion vs. Suspension

Complexity: How to Optimize Operation

Summary of Chapter

List of Symbols

References

14 Use of CFD in Fermenter Design. Purpose of This Chapter

Basic Theory

Methods of Presenting Data

Velocity Distribution

Cavern Formation

Blending Progress

Flow Around Coils

Bubble Size, kla, Holdup

DO Distribution

Summary of Chapter

List of Symbols

References

15 Agitator Seal Design Considerations. Introduction

Terminology

Main Functions of Fermenter Shaft Seals

Common Types of Shaft Seals

Material Considerations

Methods of Lubricating Seals

Seal Environmental Control and Seal Support System

Seal Life Expectations

Special Process Considerations

Summary of Chapter

Reference

16 Fermenter Agitator Mounting Methods. Introduction

Top Entering Methods

Direct Nozzle Mount

Beam Gear Drive Mount with Auxiliary Packing or Lip Seal; Beams Tied into Vessel Sidewall

Beam Gear Drive Mount with Auxiliary Mechanical Seal; Beams Tied into Vessel Sidewall

Beam Gear Drive Mount with Auxiliary Mechanical Seal; Beams Tied into Building Structure

Complete Drive and Seal Mount to Beams Tied into Vessel Sidewall, with Bellows Connector

Complete Drive and Seal Mount to Beams Tied into Building Structure, with Bellows Connector

Bottom Entering Methods

Direct Nozzle Mount

Floor Gear Drive Mount with Auxiliary Packing or Lip Seal

Floor Gear Drive Mount with Auxiliary Mechanical Seal

Floor Integrated Drive and Seal Mount with Bellows Connector

Summary of Chapter

References

17 Mechanical Design of Fermenter Agitators. Introduction

Impeller Design Philosophy

Discussion on Hydraulic Force

Shaft Design Philosophy

Shaft Design Based on Stress

Simple Example Problem

Sample Problem with Steady Bearing

Shaft Design Based On Critical Speed

Cantilevered Designs

Example Problem

Units with Steady Bearings

Solid Shaft vs. Hollow Shaft

Role of FEA in Overall Shaft Design‐Simplified Discussion

Agitator Gear Drive Selection Concepts

Early History

Loads Imposed

Handle or Isolate Loads?

Handle Loads Option 1: Oversized Commercial Gear Drive

Handle Loads Option 2: Purpose‐Built Agitator Drive

Isolate Loads Option 1: Hollow Quill Integrated Drive with Flexibly Coupled Extension Shaft

Isolate Loads Option 2: Outboard Support Bearing Module

Bearing Life Considerations

Noise Considerations

Torsional Natural Frequency

Important or Useful Mechanical Design Features

Summary of Chapter

List of Symbols

Greek Letters

References

18 Sanitary Design. Introduction

Definitions

Construction Principles

Wetted Parts Construction Methods. Welded Construction

In‐Tank Couplings

Mounting Flange Area

Axial Impellers

Radial Impellers

Bolts and Nuts

Steady Bearings

Use of Castings, 3‐D Printing

Polishing Methods and Measures1: Polishing vs. Burnishing

Polishing Methods and Measures2: Lay

Polishing Methods and Measures3: Roughness Average

Electropolish

Passivating

Effect on Mechanical Design

Summary of Chapter

Additional Sources of Information

List of Symbols

References

19 Aspect Ratio

Acknowledgment

Definition and Illustration of Aspect Ratio

What Is the Optimum Aspect Ratio?

Effects of Z/T on Cost and Performance at a Given Working Volume. Vessel Cost

Agitator Shaft Design Difficulty

Power Required for Mass Transfer

Agitator Cost

Airflow Requirements

Compressor Power

DO Uniformity

Heat Transfer Capability

Real Estate/Land Usage Issues

Building Codes; Noise

Illustrative Problem Number 1

Vessel Dimensions

Airflow and Power

Heat Transfer Data and Assumptions

Heat Transfer Results

Blend Time, DO Uniformity

Capital Cost (Agitator Plus Vessel Only)

Other Operating Costs

So What Is the Optimum Aspect Ratio for This Problem?

Illustrative Problem Number 2

Illustrative Problem Number 3

Summary of Chapter

List of Symbols

References

20 Vendor Evaluation

Product Considerations

Gear Drive Ruggedness

Design Technology

Impeller Selection

Shaft Design

Company Considerations

Reputation with Customers

Company Size

Years in Business

Years Under New Ownership

Employee Turnover

Vertical Integration

R&D Program and Publications

Depth of Application Engineering

Testing Laboratory

ISO Certification (Necessary vs Sufficient)

Quality Control Program (Not Lot Sample; 100%)

Rep vs Direct Sales (a Good Rep Annoys the Manufacturer)

Service Capability

Typical Delivery Times and Performance

Parts Availability

Price (Least Important)

Willingness to Work with Consultants

Vendor Audit Checklist

Use of an Outside Consultant

Summary of Chapter

List of Symbols

References

A.Appendix to Chapter 20

21 International Practices. Introduction

North America. Vendors

Design Practices

Selling/Buying Practices

Degree of Vertical Integration

Role of Design Firms

R&D

Culture

EU. Vendors

Design Practices

Selling/Buying Practices

Degree of Vertical Integration

Role of Design Firms

R&D

Culture

Japan

Vendors

Design Practices

Selling/Buying Practices

Degree of Vertical Integration

Role of Design Firms

R&D

Culture

China

Vendors

Design Practices

Selling/Buying Practices

Degree of Vertical Integration

Role of Design Firms

R&D

Culture

Summary of Chapter

Cultural Resources

Afterword

Index. a

b

c

d

e

f

g

h

i

j

l

m

n

o

p

r

s

t

u

v

w

x

y

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Отрывок из книги

Gregory T. Benz

.....

Examining this curve, we can observe several things. One is that the power number becomes constant for a given D/T under turbulent conditions, i.e. at high Reynolds numbers (typically, above 20 000). When a manufacturer of an impeller states it power number, it is normally the turbulent power number at a D/T of 1/3 and a C/T of 1/3. Axial impellers will tend to have a decreasing power number at increasing D/T.

Also note that the curve becomes a 45° angle at laminar flow conditions (typically, NRe <10). That means the product of Reynolds number and Power number is constant in that range. A simple derivation reveals that in the laminar range,

.....

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