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LLE 3: Solvents

LLE 3: Solvents
     Part 1: Introduction
         1 SOLVENTS
     Part 2: Phase Equilibriumin Liquid-Liquid Extraction
         1. INTRODUCTION
             1.1 The Process
             1.2 Phase Equilibria
         2. FUNDAMENTALS
             2.1 Basic Concepts
                 2.1.1 Free Energy and the Chemical Potential
                 2.1.2 Activities and the Gibbs-Duhem Equation
             2.2 Liquid Phase Stability
                 2.2.1 Binary Systems
                 2.2.2 Ternary and Multi-component Systems
             2.3 The Critical Point
                 2.3.1 Binary Systems
                 2.3.2 Ternary Systems
         3. DATA REPRESENTATION
             3.1 Binary Systems
             3.2 Ternary Systems
                 3.2.1 Triangular diagrams
                 3.2.2 Distribution Coefficients
             3.3 Solvent Free Basis
             3.4 Selectivity
             3.5 Multi-component Systems
             3.6 System Types
                 3.6.1 Type 1 Systems
                 3.6.2 Type 2 Systems
                 3.6.3 Effect of Temperature
             3.7 Graphical Tie-line Correlations.
                 3.7.1 Binary Systems
                 3.7.2 Ternary Systems
         4. DATA MEASUREMENT
             4.1 Binary Systems
                 4.1.1 Direct Analytical Method
                 4.1.2 Turbidimetry
                 4.1.3 The Volumetric Method
                 4.1.4 Critical Point Determination
             4.2 Ternary Systems
                 4.2.1 Binodal Curve
                 4.2.2 Tie-line Determination
                 4.2.3 The AKUFVE Apparatus
             4.3 Liquid-liquid-vapour Equilibria
                 4.3.1 Circulation Stills
                 4.3.2 Flow Stills
                 4.3.3 Conclusions
             4.4 Gas-liquid Chromatography
                 4.4.1. Introduction
                 4.4.2 Elution Chromatography
                 4.4.3 Frontal Chromatography
                 4.4.4 Direct Chromatographic Method
                 4.4.5 Conclusions
             4.5 Calculation from Other Physical Properties
                 4.5.1 Vapour Pressure Osmometry
                 4.5.2 Viscosity
                 4.5.3 Heat of Mixing
                 4.5.4 Conformal Solution Theory
         5. CORRELATING EQUATIONS
             5.1 Algebraic Methods
                 5.1.1 Correlation of the Binodal Curve
                 5.1.2 Tie-line Correlations
             5.2 Thermodynamically Based Equations
                 5.2.1 Classical Equations
                 5.2.2 Local Composition Equations
                 5.2.3 Modifications of Local Composition Equations
                 5.2.4 Equations Based on Quasichemical Theory
                 5.2.5 Temperature Dependence of Parameters
             5.3 Equations of State
                 5.3.1 Pure Component Equations
                 5.3.2 Mixtures
         6. CORRELATION AND PREDICTION
             6.1 Correlation
                 6.1.1 Calculation of Parameters
                 6.1.2 Treatment of error
                 6.1.3 Comparison of Equations
             6.2 Prediction from Binary Data
                 6.2.1 Calculation of parameters
                 6.2.2 Comparison of Equations
             6.3 General Comments
         7. PREDICTION FROM PURE COMPONENT DATA
             7.1 Solubility Parameter Methods
                 7.1.1 Basic Theory
                 7.1.2 Effect of Temperature Using the approximate form
                 7.1.3 The Multi-component Solubility Parameter
                 7.1.4 Apparent Solubility Parameters
                 7.1.5 Polymer Solutions
                 7.1.6 Estimation of Solubility Parameters
                 7.1.7 Conclusions
             7.2 Group Contribution Methods
                 7.2.1 The ASOG Method
                 7.2.2 The UNIFAC Equation
                 7.2.3 The Modified UNIFAC Models
                 7.2.4 Developments from UNIFAC
                 7.2.5 The DISQUAC Model
                 7.2.6 Group Re-Definition
         8. THE USE OF PHASE EQUILIBRIUM DATA
             8.1 The Single Stage
                 8.1.1 The Flash Method
                 8.1.2 Free Energy Minimisation
                 8.1.3 The Direct Method
                 8.1.4 Test for Phase Splitting
                 8.1.5 Initial Guesses
             8.2 The Complete Plant
                 8.2.1 Stage-to-Stage Methods
                 8.2.2 Solution by Component.
                 8.2.3 The Newton-Raphson Method
                 8.2.4 Method of False Transients
                 8.2.5 Continuation Methods
         9. REVIEW OF COMPUTER PROGRAMS.
             9.1 Program for a Single Stage
                 9.1.1 Equilibrium Compositions
                 9.1.2 Binodal Curve Construction
             9.2 Programs for Multi-stage Extraction
                 9.2.1 EXTRAC
                 9.2.2 LIQEXT
                 9.2.3 LILISP
                 9.2.4 Use of a Spreadsheet Program
                 9.2.5 Use of Dynamic Simulation
             9.3 Metals Extraction
                 9.3.1 Computer-aided Structure Synthesis
                 9.3.2 SEPHIS-MOD4
                 9.3.3 SXLSQA
             9.4 Miscellaneous
                 9.4.1 Water Solubility Data
         10 CONCLUSIONS
         11 NOMENCLATURE
         12 REFERENCES
     Part 3: Selection of Solvents for Liquid-Liquid Extraction Processes
         1. INTRODUCTION.
         2. PROCEDURES FOR SOLVENT SELECTION.
             2.1. Selection Procedures Reported in Recent Years.
                 2.1.1. The Hildebrand solubility parameter and Rohrschneider polarity scale.
                 2.1.2 Group combinatorial methods; the UNIFAC scheme.
                 2.1.3 Molecular modelling.
                 2.1.4 Optimisation algorithms.
                 1 2.1.5 Expert systems.
                 2.1.6 Conclusions
             2.2. Recommended Selection Procedure.
         3. STAGE 1 OF SELECTION - THE LONG LIST.
             3.1. The Miscibility Gap.
             3.2. Equilibrium Extraction.
                 3.2.1. Conventional partitioning solvents.
                 3.2.2. Supercritical fluid extraction.
             3.3. Reactive Extraction.
                 3.3.1. Reactive extraction of metals.
                 3.3.2. Reactive extraction in biotechnology and fine chemicals processing.
                 3.3.3. Extraction of bulk organics and contaminants from natural raw feedstocks.
             3.4. Micellar Extraction.
             3.5. Aqueous Biphasic Systems.
         4. STAGE 2 OF SELECTION - DEVELOPMENT OF THE ?#147;SHORT LIST?#148;; PRACTICAL AND ENGINEERING ISSUES.
             4.1. Solvent, Extract and Feed Miscibility.
             4.2. Phase Physical Properties, Drop Size and Preliminary Extractor Selection.
             4.3. Process and Chemical Safety.
             4.4. Environmental Considerations.
             4.5. Product and Solvent Recovery.
         5. STAGE 3 OF SELECTION - FULL PERFORMANCE ASSESSMENT OF SHORT- LISTED ALTERNATIVES.
             5.1. Equilibrium Extractions.
             5.2. Reactive Extraction.
             5.3. Micellar and Aqueous Biphasic Systems.
         6. OUTLINE PROCESS DESIGN.
         7. EXAMPLES OF APPLICATION.
             7.1. Separation of Lipids and Fatty Acids from Edible Oils.
                 7.1.1. Purification of triglycerides.
                 7.1.2. Separation and isolation of monoglycerides.
             7.2. Separation and Isolation of Penicillins.
             7.3. Extraction and Separation of Zirconium and Hafnium.
         8. REFERENCES.
     Part 4: Selection of Solvents for Organic Systems
         1 INTRODUCTION
         2 DESIGN GUIDE
         3 SOLVENT PROPERTIES
             3.1 Environmental Considerations
             3.2 Chemical Reactivity
             3.3 Density
             3.4 Interfacial Tension
             3.5 Vapour Pressure
             3.6 Flammability
             3.7 Freezing Point
             3.8 Cost and Availability
             3.9 Viscosity
         4 SOLVENT SEPARATION
             4.1 Separation Factor
                 4.1.1 Introduction
                 4.1.2 Solvent Capacity
                 4.1.3 Solvent Solubility
                 4.1.4 Effect of temperature
                 4.1.5 Comparison of separation factors in extractive distillation and liquid extraction
                 4.1.6 The Distribution Coefficient
             4.2 The Infinite Dilution Form of the Separation Factor
                 4.2.1 Pierotti correlations
                 4.2.2 The UNIFAC method
             4.3 Solubility
                 4.3.1 The UNIFAC Equation
         5 GENERATION AND REPRESENTATION OF EQUILIBRIUM DATA
             5.1 Experimental Methods
                 5.1.1 Solubility Determinations
                 5.1.2 Tie Line Determination
                 5.1.3 The AKUFVE Apparatus
             5.2 Correlation and Prediction
                 5.2.1 Graphical Representation
                 5.2.2 Correlating Equations
             5.3 Correlation of Experimental Data
                 5.3.1 Calculation method
             5.4 Generation of Equilibrium Compositions
             5.5 Fitted Data Example
         6 PROCESS CALCULATIONS - EXTRACTOR
             6.1 Classical Methods
                 6.1.1 Number of Stages
                 6.1.2 Amount of Solvent
                 6.1.3 Minimum Solvent
             6.2 Analytical Method
             6.3 Rigorous Solution
             6.4 Process Variables
                 6.4.1 Tie lines
                 6.4.2 Solvent/Feed Ratio Limits
                 6.4.3 Extraction Factor
             6.5 Reflux
             6.6 Economics
             6.7 Equipment size
         7 SOLVENT RECOVERY
             7.1 Recovery Methods
                 7.1.1 Lube Oil Manufacture
                 7.1.2 BTX Recovery
             7.2 Distillation
                 7.2.1 Equilibrium Data
                 7.2.2 Stage Requirements
                 7.2.3 Sizing
                 7.2.4 Costing
                 7.2.5 Summary
         8 PROCESS MODIFICATIONS
             8.1 Modified Solvents
                 8.1.1 Temperature Gradients
                 8.1.2 Pro/Anti Solvents
                 8.1.3 Control of pH
             8.2 Mixed solvents
             8.3 Dual-Solvents
             8.4 Impurities
         9 CONCLUSIONS
         10 NOMENCLATURE
         11 REFERENCES
         12 APPENDIX I EXAMPLE: THE SELECTION OF A SOLVENT FOR THE EXTRACTION OF ETHANOL FROM WATER
     Part 5: Selection of Solvents for Inorganic Systems
         1. INTRODUCTION
         2. DESIGN GUIDE
         3. PRELIMINARY FLOWSHEET SELECTION
             3.1 Introduction
             3.2 Aqueous Chemistry
             3.3 Compatibility between Solvent Extraction and Other Unit Processes
                 3.3.1 Leaching
                 3.3.2 Solids-liquid Separation
                 3.3.3 Stripping and Other Extraction Processes
                 3.3.4 Solute Recovery Processes
                 3.3.5 Effluents
                 3.3.6 Environmental Effects
             3.4 Materials Balance
                 3.4.1 Bleed of Impurity from Circuit
                 3.4.2 Water Balance
                 3.4.3 Solvent Balance
         4. Classification and Performance of Reagents: A Basis for Selection
             4.1 Reagent Classification
             4.2 Extractant Behaviour
                 4.2.1 Extraction by Compound Formation
                 4.2.2 Extraction by Ion Pair Formation
                 4.2.3 Extraction by Solvation
             4.3 Diluents and Modifiers
             4.4 Degradation of Reagents
                 4.4.1 Acid and Acid Chelating Extractants
                 4.4.2 Amines
                 4.4.3 Solvating Extractants
             4.5 Solvent Prices
             4.6 Solubility of Solvents in Aqueous Solutions
                 4.6.1 Acid Extractants
                 4.6.2 Acid Chelating Extractants and Amines
                 4.6.3 Solvating Extractants
                 4.6.4 Diluents
                 4.6.5 Modifiers
             4.7 Solvent Viscosity
                 4.7.1 Acid Extractants
                 4.7.2 Acid Chelating Extractants
                 4.7.3 Amines and Quaternary Ammonium Compounds
                 4.7.4 Solvating Extractants
             4.8 Interfacial Properties
             4.9 Hazards
                 4.9.1 Fire
                 4.9.2 Toxic Hazards
             4.10 Construction materials
         5. EXPERIMENTAL METHODS: BENCH-SCALE TESTS
             5.1 Shake-out Screen Tests
             5.2 Isotherm Development
                 5.2.1 Isotherms
                 5.2.2 Choice of Dispersed Phase
                 5.2.3 Equipment
                 5.2.4 Scrubbing
                 5.2.5 Treatment of Isotherm Data
             5.3 Counter-current Simulation
             5.4 Separation in Complex Systems
             5.5 Modelling
             5.6 Problems in Analysis of Solutes
         6. EXPERIMENTAL METHODS: SYSTEMS DEVELOPMENT
             6.1 Introduction
             6.2 Determination of Extraction and Stripping Rates
                 6.2.1 Batch Mixing Measurements
             6.3 Equipment Selection and Design
             6.4 Phase Separation Rates
                 6.4.1 Batch Measurements
                 6.4.2 Continuous Measurements
             6.5 Continuous Process Operation
                 6.5.1 Mixer-settlers
                 6.5.2 Other Contactors
                 6.5.3 Pilot Plant Operation
             6.6 Solvent Loss
                 6.6.1 Solubility
                 6.6.2 Entrainment
                 6.6.3 Crud Formation
                 6.6.4 Evaporation
                 6.6.5 Degradation
             6.7 Solvent Recovery
         7. ECONOMIC EVALUATION
             7.1 Introduction
             7.2 Capital Costs
                 7.2.1 General
                 7.2.2 Plant
                 7.2.3 Solvent Inventory
             7.3 Operating Costs
             7.4 Cost Comparisons
         8. CONCLUSIONS
         9. REFERENCES
         10. NOTATION
         11. APPENDIX - SOLVENT SELECTION: AN EXAMPLE
     Terms and Conditions of Use

Part 1  Introduction
Part 2  Phase equilibrium in liquid-liquid extraction
Part 3  Selection of solvents for liquid-liquid extraction processes -methodology
Part 4  Selection of solvents for liquid-liquid extraction processes  (i) organic systems
Part 5  Selection of solvents for liquid-liquid extraction processes  (ii) metals and inorganic systems

 

Volume SE III   Part 1 Introduction.

This part gives an overview of the volume and how to use it to best effect.


Volume SE III   Part 2 Phase equilibrium in liquid-liquid extraction.

Liquid-liquid extraction involves the treatment of a liquid mixture of two or more components with a solvent which is immiscible with the mixture but has a greater extractive power for one of the components than the others. The successful application of extraction depends on the mixture reaching or tending to reach equilibrium. This part sets out and discusses the various ways of representing equilibrium data for binary, ternary and multicomponent systems. The various methods used for determining phase equilibrium data and measuring physical properties are described and areas of research reviewed. The equations for correlating equilibrium data and the ways in which they can be used for prediction and for calculating the number of stages for a separation process are discussed. The final chapter reviews computer programs which can be used for evaluating phase equilibrium data.


Volume SE III   Part 3 Selection of solvents for liquid-liquid extraction processes - methodology.

This manual part was written to supplement and update Parts 4 and 5 and to provide a general methodology for solvent selection applicable to most extraction processes. Parts 4 and 5 deal respectively with the selection of solvents for organic and inorganic (especially metals) systems: they contain material which remains both valid and valuable, and are retained.

Between the publication of Parts 4 and 5 and the preparation of Part 3 a significant diversification was apparent in liquid-liquid extraction technology. Much of the new literature focused not upon equilibrium systems but reactive extractions, and the growth of biotechnology led to novel techniques such as aqueous/aqueous and micellar extraction. During the same period there was also a significant growth in (mainly computer-aided) techniques for equilibrium calculation and solvent selection.

These developments, where not already covered in Part 2, are reviewed in the context of a comprehensive method for solvent selection presented as a series of decision trees. The user is encouraged to develop an initial 'long-list' of feasible solvents which is then cut down to provide a shortlist for final selection. Shortlisting involves many practical aspects of selection, such as the existence of suitable equipment as well as product and solvent recovery strategies.

The selection scheme is designed to be punctuated by laboratory and pilot plant experimental work; but it may also be used, in conjunction with other manual parts, for a rapid 'paper' study or evaluation of options.


Volume SE III   Part 4 Selection of solvents for liquid-liquid extraction processes (i) organic systems.

In this report a procedure is described for the selection of an appropriate solvent for the extraction and purification of mixtures of organic materials. The procedure describes the steps which need to be followed in selecting a solvent for a particular separation. The types of ternary system usually encountered in liquid-liquid extraction are described, together with the principles of selectivity. The effects of temperature, solvent capacity and solubility on solvent selectivity are described and a brief discussion of partition coefficients is given. Experimental methods for determining equilibrium data needed for design calculations are included. Methods of solvent recovery are briefly reviewed and their influence on overall process costs is discussed. A worked example is given to demonstrate the solvent selection procedure.


Volume SE III   Part 5 Selection of solvents for liquid-liquid extraction processes (ii) metals and inorganic systems.

This report describes a procedure for the selection of solvents for the extraction and purification of metals and inorganic materials. It is concerned primarily with hydrometallurgical processes but the procedures described can be applied equally well to other inorganic materials such as wet process phosphoric acid production and the recovery of salts from brine. The procedure sets out the steps which have to be followed to select a solvent, including the need for a cost evaluation. Reagents are classified into groups based on their mode and action. A brief discussion of the extraction chemistry of these groupings is given. The uses and properties of diluents and ways in which their properties can be modified by small additions of "modifiers" are described. The chemical stability of the extraction and the effect on plant performance of other properties, for example solubility, viscosity and interfacial tension are discussed. The steps which are used to derive a procedure for solvent selection are used in a worked example.