Absorption and Stripping
Adsorption
Distillation and Flash
Liquid-Liquid Extraction
Efficiency
100

Absorption processes are more effective when pressure is modified in this manner

What is increased (or when pressure is increased)?

100

This variable (mathematically) is responsible for the change of required mass of adsorbent between batch and fixed-bed adsorption

What is weight fraction?

100

Total reflux provides this critical information

What is the minimal number of stages needed for distillation to be possible at the given xD and xB?

100

Liquid-liquid extraction multistage assessments are most similar to this mass transfer operation

What is absorption or stripping?

100

This curve allows us to graphically calculate the number of stages for a non-ideal system

What is the pseudo-equilibrium curve?

200

liquid streams leave a stripping process more purified when the gas flow rate is modified in this manner

What is increased

200

This is the key characteristic of an adsorptive chemica1

What is porosity?

200

This property is exploited when using flash or distillation as a separation technique

What is volatility (or boiling points)?

200

The solvent and diluent (or carrier) should ideally be this

What is immiscible?

200

DAILY DOUBLE:
a. This property determines how alike Murphree tray efficiency and Murphree point efficiency will be
b. FOLLOW-UP: These columns have effectively the same Murphree tray efficiency and Murphree point efficiency

DAILY DOUBLE:
a. What is the width of the column?
b. FOLLOW-UP: What are thin columns?

300

Corrosive systems are best used with this kind of column

What are packed columns?

300

The process of chemisorption forms these kinds of layers

What are monolayers (since there is a “chemical-like” bond, only direct adhesion occurs in chemisorption whereas physisorption can more multilayers given it is more about intermolecular bonds and adhesion can occurs with other adsorbate molecules on the adsorbent)

300

This is used as a preliminary assessment of the effectiveness of a flash or distillation technique as a separation process

What is relative volatility?

300

The preliminary effectiveness of a liquid-liquid extraction technique can be described using this
parameter

What is the extraction factor?

300

This describes the state of exiting streams when stages are 100% efficient

What is equilibrium?

400

These equations represent mathematical estimations for number of stages or outgoing contaminant concentration in absorption/stripping systems

What are kremser equations?

400

Generally, the relationship between physisorption effectiveness and temperature can be described like this

What is inversely proportional (when temperature increases, physisorption is less effective)?

400

Mathematically, this value represents the difference between the liquid flow rates in the stripping and rectification zones divided by the feed rate

What is q (or quality of the feed)?

400

The immiscibility of two fluids can be estimated using this parameter

What is the solubility parameter?

400

The following can be said about the Murphree vapor and Murphree liquid efficiencies (with deference to equivalence)

What is not equivalent?

500

These variables must be dilute for Henry’s law to apply

What are liquid mole fractions?

500

For reasonable adsorptive systems (read dilute), Freundlich isotherms with this curvature are considered favorable

What is downward curvature (or, in other words, n<1)?

500

This assumption is used to justify the McCabe-Thiele method in distillation

What is constant molar overflow?

500

Dilute fractional extraction is used when this is true of the contaminants


What describes multiple contaminants being desirable?

500

With deference to distillation, this stage is not counted in the overall efficiency equation

What is the reboiler?

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