Environmental Engineering Reference
In-Depth Information
Table 2.1 Exploitable properties used in separation processes.
Equilibrium properties
Rate properties
Vapor pressure
Diffusivity
Partitioning between phases
Ionic mobility
solubility of a gas in a liquid
Molecular size and shape
sorption of a solute in a fluid onto a sorbent
Chemical reaction equilibrium
Electric charge
Phase change
solid/liquid
liquid/gas
Table 2.2 Examples of separating mechanisms and separating agents.
Separation process
Separation mechanism
Separating agent
Distillation
Vapor pressure
Heat
Extraction
Partitioning between phases
Immiscible liquid
Adsorption
Partitioning between phases
Solid sorbent
Absorption
Partitioning between phases
Non-volatile liquid
Filtration
Molecular size and shape
Membrane
Ion exchange
Chemical reaction equilibrium
Solid ion-exchanger
Gas separation
Diffusivity and phase partitioning
Membrane
Electrodialysis
Electric charge and ionic mobility
Charged membrane/electric field
(c) The magnitude of the property difference. Obviously, the larger the difference be-
tween the components to be separated, the easier the separation. How large is good
enough? This answer is based on experience and the value of the components to be
separated. Preliminary calculations for various separation processes (using various
property differences) can be very useful.
(d) Chemical behavior under process conditions. Will the process fluids chemically attack
the separation equipment (corrosion, morphological changes such as swelling, etc.)
and/or react themselves (polymerize, oxidize, etc.)? This is a very important consid-
eration as it affects the lifetime and reliability of the process.
(e) Quantities and phases which need to be processed. This is an economic consideration
as the cost of implementing various property differences (energy input as heat, for
example) is a function of the scale of the process. The phases (gas vs liquid, for
example) also affect the equipment size and material handling considerations.
(f) Separation criteria. What are the concentrations of the various components in the feed
stream? What purity and recovery are needed? How many components in the feed
need to be separated?
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