Engineering adsorption is a surface-based separation process in which molecules (adsorbate) from a fluid phase adhere to the surface of a solid material (adsorbent) via physical or chemical interactions, enabling removal or recovery of target species from gases or liquids. It is used industrially for air purification, solvent recovery, water treatment, and chromatographic separation. The process is characterized by equilibrium isotherms and mass transfer kinetics, with the adsorbent regenerated by temperature or pressure changes to allow repeated cycles.
qe = (qm × KL × Ce) / (1 + KL × Ce)
LaTeX: q_e = \frac{q_m K_L C_e}{1 + K_L C_e}
| Symbol | Meaning | Unit |
|---|---|---|
| qe | Amount adsorbed per unit mass of adsorbent at equilibrium | mg/g |
| qm | Maximum monolayer adsorption capacity | mg/g |
| KL | Langmuir adsorption constant | L/mg |
| Ce | Equilibrium concentration of adsorbate in solution | mg/L |
Problem
Activated carbon adsorbs methylene blue dye. The Langmuir constants are qm = 200 mg/g and KL = 0.05 L/mg. Calculate the equilibrium adsorption capacity when the equilibrium dye concentration Ce = 40 mg/L.
Solution
Step 1: Substitute into the Langmuir isotherm: qe = (200 × 0.05 × 40) / (1 + 0.05 × 40). Step 2: Numerator = 200 × 0.05 × 40 = 400. Step 3: Denominator = 1 + 2 = 3. Step 4: qe = 400 / 3 = 133.3 mg/g.
Answer
qe = 133.3 mg/g — the activated carbon adsorbs 133.3 mg of dye per gram at this concentration.
| Adsorbent | Surface Area | Primary Use | Regeneration Method |
|---|---|---|---|
| Activated carbon | 500–1500 m²/g | VOC removal, water purification | Thermal (steam) |
| Zeolite (molecular sieve) | 300–700 m²/g | Gas drying, N₂/O₂ separation | Pressure swing (PSA) |
| Silica gel | 200–800 m²/g | Moisture adsorption, chromatography | Thermal drying |
| Alumina (activated) | 150–350 m²/g | Fluoride removal, desiccation | Thermal regeneration |
| Ion exchange resin | Varies | Heavy metal and ion removal | Chemical regeneration |
Wikimedia Commons, CC BY-SA
Membrane separation is a process in which a semi-permeable membrane selectively allows certain molecules or ions to pass through while retaining others, driven by a concentration, pressure, or electrical potential gradient. Common forms include reverse osmosis, nanofiltration, ultrafiltration, microfiltration, and pervaporation, each distinguished by the size range of species separated. Membrane processes are highly energy-efficient alternatives to thermal separation methods and are critical in water purification, food processing, and pharmaceutical applications.
Ion exchange is a reversible chemical process in which ions of the same charge are exchanged between a solution and an insoluble solid ion-exchange resin, allowing selective removal, concentration, or substitution of specific ions. Cation exchange resins remove positively charged ions (e.g., Ca²⁺, Mg²⁺, heavy metals) while anion exchange resins target negatively charged species (e.g., NO₃⁻, SO₄²⁻). Ion exchange is fundamental to water softening, demineralization, pharmaceutical purification, and nuclear waste treatment.
Industrial filtration is a mechanical separation process that removes solid particles from a liquid or gas stream by passing the mixture through a porous medium that retains the solids (filter cake) while allowing the fluid (filtrate) to pass through. It is fundamental to chemical processing, wastewater treatment, food and beverage production, and pharmaceutical manufacturing. The efficiency of filtration depends on particle size, filter medium properties, applied pressure, and the characteristics of the slurry.
From Latin "ad-" (to) + "sorbere" (to suck in), meaning to attract onto a surface. Distinguished from "absorption" (into the bulk). The term was introduced by Heinrich Kayser in 1881 to describe the phenomenon of gases condensing onto solid surfaces.