Food mixing : principles and applications / edited by P.J. Cullen.

"The mixing of liquids, solids and gases is one of the most common unit operations in the food industry. Mixing increases the homogeneity of a system by reducing non-uniformity or gradients in composition, properties or temperature. Secondary objectives of mixing include control of rates of hea...

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Bibliographic Details
Other Authors: Cullen, P. J. (Patrick J.) (Editor)
Format: Book
Language:English
Published: Chichester, U.K. ; Ames, Iowa : Wiley-Blackwell, 2009.
Subjects:
Table of Contents:
  • 1. Mixing in the food industry: trends and challenges / P.J. Cullen and Colm P. O'Donnell
  • 1.1. Role of mixing
  • 1.2. Design criteria for mixing
  • 1.3. Specific challenges in food mixing
  • 1.3.1. Quality assurance compliance through mixing
  • 1.3.2. Engineering texture through mixing
  • 1.4. Advances in the science of mixing
  • 1.5. Book objectives
  • 2. Mixing fundamentals / Kasiviswanathan Muthukumarappan
  • 2.1. Introduction
  • 2.2. Defining mixing
  • 2.2.1. Macromixing
  • 2.2.2. Mesomixing
  • 2.2.3. Micromixing
  • 2.3. Scale of scrutiny
  • 2.4. Quantifying mixedness
  • 2.4.1. Inference of mixing indices
  • 2.5. Determining the end point of mixing
  • 2.5.1. Solids mixing
  • 2.5.2. Fluid mixing
  • 2.5.3. Multi-phase mixing
  • 2.5.4. Alternative measures of mixedness in industrial practice
  • 2.6. Residence time distributions
  • 2.6.1. Modelling of residence time distributions
  • 3. Kinematics of flow and mixing mechanisms / Brijesh Tiwari and P.J. Cullen
  • 3.1. Introduction
  • 3.2. Fluid mixing
  • 3.2.1. Kinematics of fluid flow
  • 3.2.2. Quantification of flow regimes
  • 3.2.3. Chaotic advection
  • 3.2.4. Fluid mixing mechanisms
  • 3.3. Solids mixing
  • 3.3.1. Mixing flow in solids
  • 3.3.2. Solids mixing mechanism
  • 3.4. Identification of mixing mechanisms
  • 3.4.1. Solids
  • 3.4.2. Fluids
  • 4. Rheology and mixing / P.J. Cullen and Robin K. Connelly
  • 4.1. Introduction
  • 4.2. Dispersion rheology
  • 4.2.1. Forces acting on dispersed particles
  • 4.2.2. Parameters affecting suspension rheology
  • 4.3. Fluid rheology and mixing
  • 4.3.1. Shear flow
  • 4.3.2. Elongational flow
  • 4.4. Effects of mixing on fluid rheology
  • 4.5. Mixer rheometry
  • 4.5.1. Theory
  • 4.5.2. Mixer rheometry applications
  • 4.6. Conclusion
  • 5. Equipment design / David S. Dickey
  • 5.1. Introduction
  • 5.2. Liquid mixing equipment
  • 5.2.1. Portable mixers
  • 5.2.2. General purpose liquid mixers
  • 5.2.3. Mixer shafts design
  • 5.2.4. Other mechanical design considerations
  • 5.2.5. Special purpose liquid mixing equipment
  • 5.2.6. Food specific mixing equipment
  • 5.3. Powder mixing equipment
  • 5.3.1. Ribbon blenders
  • 5.3.2. Paddle blenders
  • 5.3.3. Combination blenders
  • 5.3.4. Tumble blenders
  • 5.3.5. Loading and emptying blenders
  • 5.3.6. Liquid addition to powders
  • 5.3.7. Sampling
  • 5.3.8. Safety
  • 5.3.9. Blending systems
  • 5.4. Equipment components
  • 5.4.1. Electric motors
  • 5.4.2. Speed reducers
  • 5.4.3. Seals
  • 6. Mixing scale-up / David S. Dickey
  • 6.1. Introduction
  • 6.2. Scale-up for fluid mixing
  • 6.2.1. Dimensional analysis
  • 6.2.2. Scale-up with geometric similarity
  • 6.2.3. Scale-up without geometric similarity
  • 6.3. Scale-up for powder mixing
  • 7. Monitoring and control of mixing operations / Colette C. Fagan, P.J. Cullen and Colm P. O'Donnell
  • 7.1. Introduction
  • 7.2. Torque and power measurement
  • 7.3. Flow measurement
  • 7.3.1. Hot-wire anemometry
  • 7.3.2. Laser Doppler anemometry
  • 7.3.3. Phase Doppler anemometry
  • 7.3.4. Flow visualization using computer vision
  • 7.3.5. Particle image velocimetry
  • 7.3.6. Planar laser-induced fluorescence
  • 7.3.7. Tomography
  • 7.4. Quantification of mixing time
  • 7.4.1. NIR spectroscopy
  • 7.4.2. Chemical imaging
  • 8. Computational fluid mixing / Chris D. Rielly and Jolius Gimbun
  • 8.1. Introduction
  • 8.1.1. History of CFD
  • 8.1.2. Steps towards CFD simulation of mixing processes
  • 8.2. Conservation equations
  • 8.2.1. Mass conservation
  • 8.2.2. Momentum conservation
  • 8.2.3. Turbulence
  • 8.2.4. Energy conservation
  • 8.2.5. Species transport
  • 8.2.6. Turbulent species and energy transport
  • 8.2.7. Boundary conditions
  • 8.3. Numerical methods
  • 8.3.1. Discretised solution of the flow variables
  • 8.3.2. Grid generation
  • 8.3.3. Discretisation
  • 8.3.4. Finite-volume discretisation methods
  • 8.3.5. Solver methods
  • 8.4. Application of CFD to stirred tank modelling
  • 8.4.1. Mixing operations
  • 8.4.2. Representation of the impeller
  • 8.4.3. Prediction of mixer performance characteristics
  • 8.4.4. Simulation of unbaffled or partially baffled stirred tanks
  • 8.4.5. Simulation of single-phase flow in baffled stirred tanks
  • 8.4.6. Mixing and blending simulations
  • 8.4.7. Multi-phase simulations
  • 8.5. Application to food mixing operations
  • 8.5.1. Challenges for simulation of food processes
  • 8.5.2. Examples of food applications
  • 8.6. Closing remarks
  • 9. Immiscible liquid - liquid mixing / Fotis Spyropoulos, P.W. Cox and Ian T. Norton
  • 9.1. Introduction
  • 9.2. Emulsion types and properties
  • 9.2.1. Kinetically trapped nano-emulsions
  • 9.2.2. Pickering emulsions
  • 9.2.3. Double emulsions
  • 9.2.4. Air-filled emulsions
  • 9.2.5. Water-in-water emulsions
  • 9.3. Future challenges
  • 9.3.1. Better mechanistic understanding of the emulsification process / es
  • 9.3.2. Improved emulsification processes
  • 9.3.3. Designed emulsions for improved nutrition and health
  • 9.3.4. Reduced use of surfactants for environmental reasons
  • 10. Solid - liquid mixing / Mostafa Barigou
  • 10.1. Introduction
  • 10.2. Regimes of solids suspension and distribution
  • 10.2.1. State of nearly complete suspension with filleting
  • 10.2.2. State of complete particle motion
  • 10.2.3. State of complete off-bottom suspension
  • 10.2.4. State of homogeneous or uniform suspension
  • 10.3. Prediction of minimum speed for complete suspension
  • 10.3.1. Influence of physical properties
  • 10.3.2. Influence of solids concentration
  • 10.3.3. Influence of geometric parameters
  • 10.4. Hydrodynamics of particle suspension and distribution
  • 10.4.1. Particle slip velocity
  • 10.4.2. Particle settling and drag
  • 10.5. Scale-up of solid - liquid mixing
  • 10.6. Damage to food particles in suspension
  • 10.7. Fine particle slurries
  • 11. Gas - liquid mixing / J.K. Sahu and Keshavan Niranjan
  • 11.1. Introduction
  • 11.2. Gas - liquid dispersion operations
  • 11.2.1. Characteristics of dispersed phase - mean diameter
  • 11.2.2. Gas dispersion - bubble behaviour
  • 11.2.3. Gas dispersion in agitated vessels
  • 11.3. Power input to turbine dispersers
  • 11.4. Gas handling capacity and loading of turbine impeller
  • 11.5. Bubbles in foods
  • 11.6. Methods for mixing gas in liquid
  • 11.6.1. Mixing by mechanical agitation under positive pressure
  • 11.6.2. Mixing by mechanical agitation under vacuum
  • 11.6.3. Steam-induced mixing
  • 11.6.4. Other gas - liquid mixing methods
  • 11.7. Characterization of bubble-containing structures
  • 11.7.1. Gas hold-up
  • 11.7.2. Bubble size distribution
  • 11.7.3. Rheological characterization
  • 11.8. Role of gases and specific ingredients in characterizing interfacial and rheological properties
  • 11.9. Stability of foams and solidification of bubbly dispersions
  • 11.10. Ultrasound in gas mixing and applications in food aeration
  • 12. Evaluation of mixing and air bubble dispersion in viscous liquids using numerical simulations / Kiran Vyakaranam, Maureen Evans, Bharani Ashokan and Jozef L. Kokini
  • 12.1. Introduction
  • 12.2. Measures of mixing and evaluation of flow
  • 12.2.1. Efficiency of stretching
  • 12.2.2. Dispersive mixing efficiency
  • 12.2.3. Distributive mixing efficiency
  • 12.3. Governing equations for calculation of flow
  • 12.4. CFD approaches for simulation of mixing flows
  • 12.4.1. Finite element method
  • 12.4.2. Techniques to handle moving parts
  • 12.5. FEM numerical simulation of batch mixer geometries
  • 12.5.1. 3D numerical simulation of flow in a Brabender Farinograph®
  • 12.5.2. Analysis of mixing in 2D single-screw and twin-screw geometries
  • 12.6. 3D Numerical simulation of twin-screw continuous mixer geometries
  • 12.6.1. Distributive mixing efficiency in a 3D mixing geometry
  • 12.6.2. Evaluation of dispersive mixing in 3D continuous mixer geometry
  • 12.7. Prediction of bubble and drop dispersion in a continuous mixer
  • 12.8. Summary
  • 13. Particulate and powder mixing / John J. Fitzpatrick
  • 13.1. Introduction
  • 13.2. Characterisation of particulate mixtures
  • 13.2.1. Types of mixtures
  • 13.2.2. Mixture quality
  • 13.3. Assessment of mixture quality
  • 13.3.1. Sampling
  • 13.3.2. Sample variance and standard deviation
  • 13.3.3. Lacey and Poole indices of mixture quality
  • 13.3.4. Relative standard deviation
  • 13.3.5. Estimating the true variance (s2) from the random sample variance (S2)
  • 13.3.6. Assessing if satisfactory mixture quality is achieved
  • 13.3.7. 'Baking a cake' method of assessing mixture quality
  • 13.3.8. Influence of particle size and powder cohesiveness on mixture quality
  • 13.4. Mixing mechanisms
  • 13.4.1. Convection or macromixing
  • 13.4.2. Diffusion or micromixing
  • 13.4.3. Shearing
  • 13.5. Segregation or demixing
  • 13.5.1. Segregation
  • 13.5.2. Reducing segregation
  • 13.6. Powder mixing equipment
  • 13.6.1. Tumbling mixers
  • 13.6.2. Convective mixers
  • 13.6.3. High shear mixers
  • 13.6.4. Sigma blade mixers
  • 13.6.5. Continuous mixers
  • 13.7. Mixer selection and process design
  • 13.7.1. Specification of mixture quality requirement
  • 13.7.2. Mixer selection
  • 13.7.3. Process design
  • 13.8. Other factors affecting mixing process design in dry food processing
  • 13.8.1. Hygiene and cleaning
  • 13.8.2. Addition of multiple ingredients with large variation in properties
  • 13.8.3. Addition of ingredients in liquid form
  • 13.8.4. Dust prevention and control.
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  • Call Number:
    664.024 FOO
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