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WorksheetsSection 4.2.5. Separation of Dissolved Liquids PART 3
Total questions: 47
Worksheet time: 24mins
Which separation technique is particularly effective for dilute aqueous solutions of biomolecules?
Chromatography
Leaching
Distillation
Spray drying
In solvent extraction, the rate of mass transfer is primarily governed by:
Solvent viscosity
Interfacial area and concentration gradient
Solvent boiling point
Phase density difference
Which operating condition reduces entrainment losses in liquid–liquid extraction?
Very high agitation speed
Controlled agitation with proper settling time
Increasing solvent polarity
Operating at supercritical pressure
The “distribution coefficient” in solvent extraction represents:
Ratio of solvent viscosity to density
Ratio of solute concentration in solvent phase to that in feed phase
Fraction of solute lost
Solvent-to-feed ratio
The minimum number of extraction stages required for a target separation is estimated using:
McCabe–Thiele method
Perry–Greenwood chart
Antoine equation
Rayleigh equation
For systems with close-boiling solvents, solvent extraction is favored over distillation because:
Distillation is more energy intensive
Distillation produces impure raffinate
Distillation requires less equipment
Extraction is always cheaper
The effectiveness of leaching nuts and seeds depends on:
Particle porosity and solvent diffusivity
Color of the extract
Operating at low pH
Shape of the particles only
Which parameter is most critical in adsorption processes?
Particle color
Surface area of the adsorbent
Solvent miscibility
Molecular weight of the solvent
Ion exchange resins are generally classified into:
Strong acid, weak acid, strong base, weak base
Cationic and anionic only
Porous and nonporous
Polar and nonpolar
A common adsorbent used in removing organic impurities from aqueous solutions is:
Bentonite
Activated carbon
Silica sand
Resin
Chromatography is especially advantageous in biochemical product recovery because:
It operates at low temperatures, avoiding denaturation
It requires no solvents
It is faster than filtration
It does not require equilibrium stages
In counter-current leaching, solvent economy is maximized by:
Recycling solvent through multiple stages
Using single-pass solvent flow
Eliminating decanters
Operating at high temperature only
The main disadvantage of mixer-settlers in solvent extraction is:
Limited throughput due to large settling area requirements
High solvent consumption
Continuous operation is impossible
Lack of agitation control
Which parameter best describes solvent selectivity in liquid–liquid extraction?
Solvent density difference
Separation factor
Solvent refractive index
Extraction pressure
A system where uranium is extracted from nitric acid solution is an example of:
Solvent extraction with immiscible organic solvent
Adsorption
Ion exchange
Distillation
In chromatography, separation is achieved because components:
Have equal distribution between phases
Partition differently between stationary and mobile phases
Dissolve only in solvents
Migrate at the same velocity
Which of the following makes solvent extraction attractive for heat-sensitive materials?
It operates at ambient temperatures
It requires less solvent
It uses high vacuum
It eliminates raffinate recovery
Leaching of oil from soybean flakes typically uses which solvent?
Acetone
Hexane
Methanol
Carbon tetrachloride
In ion exchange, the exhaustion of resin means:
Resin loses color
Active sites are fully occupied by counter-ions
Resin becomes insoluble
Resin dissolves in water
Which regeneration agent is used for cation exchange resins in water softening?
Sodium chloride solution
Sulfuric acid
Ethanol
Calcium hydroxide
In adsorption, breakthrough curves are used to determine:
Resin pore size
Bed exhaustion time
Solvent density
Settling rate
Which chromatography type is most widely used for protein purification?
Thin layer chromatography
Ion-exchange chromatography
Gas chromatography
Paper chromatography
The primary advantage of column chromatography over batch methods is:
Higher resolution and continuous separation
No need for solvents
Faster drying of solids
Ability to separate immiscible liquids
In solvent extraction, emulsion formation can be minimized by:
Using low interfacial tension solvents
Optimizing agitation intensity
Adding large amounts of surfactants
Decreasing settling time drastically
The driving force for ion exchange processes is:
Pressure difference
Electrostatic affinity of ions to functional groups on resin
Solvent evaporation
Osmotic pressure
A key difference between leaching and solvent extraction is that:
Leaching operates on solid–liquid systems
Leaching produces raffinate
Solvent extraction requires drying
Leaching always uses organic solvents
A countercurrent washing system in leaching helps to:
Reduce solvent recovery
Minimize residual solute in solids
Increase particle size
Prevent diffusion
Which factor primarily affects the separation speed in adsorption columns?
Bed height and particle size
Solvent polarity
Temperature of the extract
Density of the raffinate
Chromatography provides high separation efficiency because:
Multiple equilibria are established during migration
It requires large volumes of solvent
Components remain immiscible
Mobile phase remains stagnant
Which method is often used for scale-up of solvent extraction equipment?
Sigma (Σ) theory
Antoine equation
Reynold’s analogy
Stokes’ law
In adsorption, desorption of solute is usually achieved by:
Heating or solvent washing
Crushing the adsorbent
Increasing pressure
Freezing the column
In ion exchange water softening, hardness is mainly caused by:
Sodium and potassium ions
Calcium and magnesium ions
Iron and copper ions
Chloride and sulfate ions
Leaching efficiency improves with:
Smaller particle size and higher solvent penetration
Larger particle size
Higher solvent viscosity
Lack of agitation
In chromatography, the retention factor (Rf) measures:
Ratio of distance traveled by solute to solvent front
Solvent density difference
Diffusivity of solute in solvent
Interfacial tension
Which industrial process uses adsorption extensively?
Decolorization of sugar solutions
Distillation of crude oil
Extraction of palm oil
Ion exchange in water treatment
Solvent recovery is critical in extraction processes because:
Solvent cost and environmental concerns
Raffinate has no value
Extraction is irreversible
Solvent is always consumed
Which is a typical case where adsorption is preferred over solvent extraction?
Trace organic removal from water
Recovery of oil from seeds
Extraction of metals from acid solutions
Large-scale distillation
The selectivity of ion exchange resins depends on:
Type of functional groups present
Color of the solution
Solvent boiling point
Flow rate
Chromatography columns often require:
A stationary phase packed with solid or coated liquid
Two immiscible solvents
Continuous agitation
Vacuum operation
The equilibrium distribution of solute in extraction is influenced by:
Solvent-to-feed ratio
Particle size of solid feed
Bed porosity
Crystallization rate
In continuous countercurrent leaching, performance is measured by:
Solvent viscosity
Solute recovery efficiency per stage
Raffinate density
Bed height
A refinery wants to remove trace sulfur compounds from a hydrocarbon stream without high energy costs. The best method is:
Solvent extraction
Adsorption using activated carbon
Ion exchange
Leaching
Which solvent property most strongly determines phase disengagement in extraction?
Polarity difference with feed solvent
Refractive index
Color
pH
Leaching kinetics are controlled mainly by:
Diffusion through solid pores
Solvent density
Heat of vaporization
Adsorption equilibria
In water softening by ion exchange, regeneration with NaCl restores:
Na⁺ ions on the resin
Ca²⁺ and Mg²⁺ ions
K⁺ ions
Sulfate groups
Which chromatography method separates based on molecular size?
Gel filtration chromatography
Ion exchange chromatography
Affinity chromatography
Partition chromatography
Which factor reduces solvent requirements in extraction?
High distribution coefficient of solute
High solvent miscibility
Low solute diffusivity
Smaller interfacial area
