Liquid-liquid extraction (LLE), also called solvent extraction, is a separation process that transfers a target solute (or solutes) from one liquid phase (the feed or raffinate) into a second immiscible liquid phase (the solvent or extract). The two phases are mixed to allow mass transfer, then separated by gravity or centrifugal force. LLE is widely used when distillation is impractical due to close boiling points, azeotropes, heat sensitivity, or when high selectivity is needed. Common industries include petrochemicals, pharmaceuticals, hydrometallurgy, food processing, wastewater treatment, and fine chemicals.
LLE relies on the difference in solubility of the target solute between two immiscible liquids (usually an aqueous phase and an organic solvent). The distribution coefficient (K or D) defines how favorably the solute partitions into the solvent phase:
Key factors affecting performance: solvent selection, pH, temperature, phase ratio, mixing intensity, and contact time.
| Type | Description | Typical Use |
|---|---|---|
| Mixer-Settler | Separate mixing tank + settling tank per stage; gravity separation | Large-scale, high flow, multi-stage extraction |
| Centrifugal Extractor (Podbielniak, Luwesta, etc.) | High-speed rotating disc or bowl for rapid mixing & separation | High throughput, short residence time, space-limited sites |
| Packed or Plate Column (Karr, Scheibel, Pulsed) | Counter-current flow in vertical column with packing or plates | High number of theoretical stages, continuous operation |
| Rotating Disc Contactor (RDC) | Rotating discs enhance mixing in a column | Moderate to high throughput, good for viscous phases |
| Agitated Column (Kühni, Oldshue-Rushton) | Impellers on shaft provide mixing | High dispersion, good for difficult phase separation |
| Feature | Mixer-Settler | Centrifugal Extractor | Packed/Plate Column |
|---|---|---|---|
| Throughput | High | Very high | Moderate to high |
| Number of Stages | Flexible (multiple units) | Limited per machine | High (column height) |
| Footprint | Large | Very compact | Compact (vertical) |
| Residence Time | Long (settling) | Very short | Moderate |
| Best For | Large scale, slow kinetics | Heat-sensitive, high-value, space-limited | High stage efficiency, continuous |
| Parameter | Typical Range | Notes |
|---|---|---|
| Phase Ratio (O/A or A/O) | 1:1 to 10:1 | Depends on distribution coefficient & economics |
| Operating Temperature | 20–80 °C | Higher temp often increases solubility & kinetics |
| Residence Time | 1–30 minutes per stage | Shorter in centrifugal, longer in mixer-settler |
| Number of Stages | 2–20 theoretical stages | Determined by extraction factor & required recovery |
| Solvent Recovery | 99%+ typical | Via distillation, stripping, or back-extraction |
| Industry / Application | Typical Separation | Primary Goal |
|---|---|---|
| Petrochemical | Aromatics (benzene/toluene/xylene) from aliphatics | High-purity product recovery |
| Pharmaceuticals | Antibiotics, vitamins, APIs from fermentation broth | Selective solute extraction, product concentration |
| Hydrometallurgy | Copper, uranium, rare earths, cobalt/nickel from leach solutions | Metal recovery & concentration |
| Food & Beverage | Caffeine from coffee/tea, essential oils, decaffeination | Natural product extraction |
| Wastewater / Environmental | Phenols, organic acids, heavy metals from aqueous waste | Pollutant removal, solvent recovery |

Also check out, "Oil Extraction System"