Principles of multiple-liquid separation systems : interaction, application and advancement /

"Principles of Multiple-Liquid Separation Systems: Interaction, Application and Advancement describes the basic principles and advancements of multiple-liquid separation systems in downstream processing. Several important elements are included, such as the fundamental process and mechanisms of...

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Bibliographic Details
Corporate Author: ScienceDirect (Online service)
Other Authors: Chew, Kit Wayne (Editor), Chia, Shir Reen (Editor), Show, Pau Loke (Editor)
Format: eBook
Language:English
Published: Amsterdam, Netherlands ; Oxford, United Kingdom ; Cambridge MA : Elsevier, [2023]
Subjects:
Online Access:Connect to the full text of this electronic book
Table of Contents:
  • Front cover
  • Half title
  • Title
  • Copyright
  • Contents
  • Contributors
  • Chapter 1 Polymer-polymer interaction
  • 1.1 Introduction
  • 1.2 Phase diagram
  • 1.3 Parameters influencing phase diagram
  • 1.3.1 Molecular weight
  • 1.3.2 Polymer concentration
  • 1.3.3 Temperature
  • 1.3.4 pH
  • 1.3.5 Tie line length
  • 1.4 Application of aqueous two-phase system
  • 1.4.1 Proteins
  • 1.4.2 Pharmaceutical products
  • 1.4.3 Low molecular weight compounds
  • 1.5 Genetic materials
  • 1.6 Future perspective
  • 1.7 Conclusion
  • References
  • Chapter 2 Polymer-salt interaction
  • 2.1 Introduction
  • 2.2 Mechanism and working principles
  • 2.2.1 Binodal curve
  • 2.3 Key process parameters
  • 2.3.1 Effect of polymer molecular weight (MW)
  • 2.3.2 Effect of concentration of polymer
  • 2.3.3 Effect of system pH
  • 2.3.4 Effect of temperature
  • 2.3.5 Effect of hydrophobicity and addition of salt
  • 2.4 Applications
  • 2.4.1 Protein purification
  • 2.4.2 DNA and nucleic acids
  • 2.4.3 Virus, virus-like particles (VLPs)
  • 2.4.4 Drug residues in food and water
  • 2.5 Limitation and future challenges
  • Conclusion
  • References
  • Chapter 3 Alcohol-salt interaction
  • 3.1 Introduction
  • 3.2 Background and basic principle of alcohol/salt-based liquid biphasic system
  • 3.3 Influence of key parameters
  • 3.3.1 Effect of temperature
  • 3.3.2 Effect of anion salt type
  • 3.3.3 Effect of type of alcohol
  • 3.4 Applications of alcohol/salt-based LBS
  • 3.4.1 Enzymes
  • 3.4.2 Proteins
  • 3.4.3 Medicinal plants
  • 3.4.4 Other applications
  • 3.5 Limitations and advancements to the alcohol/salt-based liquid biphasic system
  • 3.6 Conclusions
  • References
  • Chapter 4 Sugar-based deep eutectic solvent-aqueous two-phase system
  • 4.1 Introduction
  • 4.2 Sugar-based deep eutectic solvent
  • 4.2.1 Synthesis of deep eutectic solvent.
  • 4.2.2 Characterization of deep eutectic solvent
  • 4.3 Sugar-based deep eutectic solvent-aqueous two-phase system
  • 4.4 Effect of parameters
  • 4.4.1 Mass fraction of deep eutectic solvent
  • 4.4.2 Type of hydrogen bond acceptor and hydrogen bond donor
  • 4.4.3 Hydrogen bond acceptor to hydrogen bond donor mass/molar ratio
  • 4.4.4 Temperature
  • 4.4.5 Type of phase forming component
  • 4.5 Application of sugar-based deep eutectic solvent-aqueous two-phase system
  • 4.6 Advancement of sugar-based deep eutectic solvent-aqueous two-phase system over the last 5 years
  • 4.7 Recycling of sugar-based deep eutectic solvent
  • 4.8 Conclusions
  • References
  • Chapter 5 Ionic liquid-salt interaction
  • 5.1 Introduction
  • 5.1.1 Types of ATPS
  • 5.2 Fundamentals of ionic liquid-salt: thermodynamic and properties
  • 5.3 Determination of solution concentration in both phases
  • 5.4 Factors that influence the two-phase separation in ionic liquid/salt ATPS
  • 5.4.1 Effect of type of inorganic salt
  • 5.4.2 Effect of inorganic salt concentration
  • 5.4.3 Effect of temperature
  • 5.5 Applications of Ionic liquid/salt ATPS
  • 5.5.1 Separation and concentration of chloramphenicol using Ionic liquid/salt two-phase flotation system (IL-ATPF )
  • 5.5.2 Extraction of protein using Ionic liquid
  • 5.5.3 Purification of roxithromycin using IL-salt ATPS
  • 5.5.4 Extraction of anthraquinones using ILATPS
  • 5.6 Conclusion
  • References
  • Chapter 6 T-butanol-salt three-phase interaction
  • 6.1 Introduction
  • 6.2 Process description
  • 6.2.1 Process overview
  • 6.2.2 About tert-butanol and ammonium sulfate
  • 6.3 Principle of three-phase partitioning
  • 6.4 Application of three-phase systems
  • 6.4.1 Extraction of proteins
  • 6.4.2 Oil extraction
  • 6.4.3 Multimolecule separation
  • 6.4.4 Other molecules
  • 6.5 Future perspectives and challenges
  • 6.6 Conclusion.
  • 10.5.2 Key factors
  • 10.5.3 Advantages and limitations
  • 10.6 Electricity-assisted liquid biphasic system
  • 10.6.1 Mechanism
  • 10.6.2 Key factors
  • 10.6.3 Advantages and limitations
  • 10.7 Microwave-assisted liquid biphasic system
  • 10.7.1 Mechanism
  • 10.7.2 Key factors
  • 10.8 Future prospects
  • References
  • Chapter 11 Economical sustainability of multiphase systems
  • 11.1 Economic sustainability
  • 11.1.1 Economic feasibility
  • 11.1.2 Cost-benefit analysis
  • 11.2 Advantages of liquid-liquid separation over conventional method
  • 11.2.1 Water content
  • 11.2.2 Interfacial tension
  • 11.2.3 Energy consumption
  • 11.2.4 Equipment requirement
  • 11.2.5 Solvents
  • 11.3 Three-phase interactions
  • 11.4 Costing in liquid separation system
  • 11.4.1 Technology for liquid separation system
  • 11.4.2 Equipment cost for ATPS liquid separation system
  • 11.4.3 Operating cost
  • 11.4.4 Variable cost
  • 11.4.5 Fixed cost
  • 11.4.6 Plant overhead cost
  • 11.5 Value of end product from biochemical engineering separation
  • 11.6 Cost-benefit analysis of ATPS and conventional separation method
  • 11.7 ATPS process cost/benefits evaluation-polymer-salt interaction
  • 11.7.1 Capital/operating cost for ATPS process
  • 11.7.2 Total revenue for ATPS process
  • 11.7.3 Time value of money
  • 11.7.4 Net present value
  • 11.7.5 Internal rate of return
  • 11.7.6 Break-even analysis
  • 11.8 Conventional protein A affinity chromatography cost/benefits analysis
  • 11.8.1 Capital/operating costs for protein A affinity chromatography
  • 11.8.2 Operating costs for protein A capture process
  • 11.8.3 Total revenue
  • 11.8.4 Net present value
  • 11.8.5 Internal rate of return
  • 11.8.6 Break-even analysis
  • 11.8.7 Comparison of ATPS and protein A chromatography
  • 11.9 Conclusion
  • References
  • Chapter 12 Environmental sustainability of multiphase systems.
  • 12.1 Introduction
  • 12.2 Environmental impact caused by conventional extraction method
  • 12.2.1 Air pollution
  • 12.2.2 Water pollution
  • 12.2.3 Soil pollution
  • 12.3 Nonconventional extraction method
  • 12.3.1 Microwave-assisted extraction
  • 12.3.2 Pressurized liquid extraction
  • 12.3.3 Gravity separation
  • 12.3.4 Coalescing separation
  • 12.4 Comparison between alternative extraction methods
  • 12.5 Environmental sustainability-related industrial applications
  • 12.5.1 Purification of natural dye carmine
  • 12.5.2 Ionic liquid as green extraction solvent
  • 12.6 Conclusion
  • References
  • Chapter 13 Potential upscaling of multiphase systems
  • 13.1 Introduction
  • 13.2 Chromatography
  • 13.2.1 Introduction to chromatography
  • 13.2.2 Limitation and challenges with chromatography
  • 13.2.3 Cleaning and regeneration
  • 13.2.4 Development and advancement in chromatography
  • 13.2.5 Concluding remarks and future prospects
  • 13.3 Membrane
  • 13.3.1 Introduction to membrane
  • 13.3.2 Issues with membrane
  • 13.3.3 Methods to reduce membrane fouling
  • 13.3.4 Advancement in membrane cleaning
  • 13.3.5 Concluding remarks and future prospects
  • 13.4 Aqueous two-phase system
  • 13.4.1 Introduction to aqueous two-phase system
  • 13.4.2 Limitation and challenges
  • 13.4.3 Factor affecting ATPS
  • 13.4.4 Development and advancement
  • 13.4.5 Concluding remarks and future prospects
  • 13.5 Precipitation
  • 13.5.1 Introduction to precipitation
  • 13.5.2 Limitation and challenges
  • 13.5.3 Factors affecting protein solubility
  • 13.5.4 Development and advancement
  • 13.5.5 Concluding remarks and future prospects
  • 13.6 Conclusion
  • References
  • Chapter 14 Integrated systems for multiphase development
  • 14.1 Introduction
  • 14.2 Ultrasonic-assisted extraction
  • 14.2.1 Mechanism/working principle
  • 14.2.2 Key factors/influencing parameters.