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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| Format: | eBook |
| Language: | English |
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Amsterdam, Netherlands ; Oxford, United Kingdom ; Cambridge MA :
Elsevier,
[2023]
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| 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.