Acid-catalyzed hot-water |
Release of bound lipids by uncoupling the lipid-protein and lipid-starch and intermolecular forces |
|
|
[34] |
Bead beating |
Mechanical compaction and shear stress |
Cost-effective
Continuous module of operation
High disruption efficiency
Mild operating temperature
Suitable for lab-scale to industrial scale
|
|
[35,36] |
Enzyme |
Specific enzyme-substrateinteraction |
|
|
[18,28,29,30,31,32,37] |
Expeller press |
Mechanical compaction and shear stress |
Cost-effective and simple process
Solvent-free extraction possible
Microwave heating before expeller press can improve the lipid yield
|
|
[38,39,40,41] |
High-pressure homogenization (HPH) |
Cavitation and shear stress |
Simple continuous operating system
Can be applied for wet biomass
Low solvent requirement
Low-temperature extraction
Applicable to large-scale
|
High capital and maintenance cost
Less efficient for filamentous microorganisms
Undesirable for heat-liable compounds
Induced the formation of free fatty acids
|
[42,43] |
High-speed shearing homogenization |
Cavitation and shear forces |
|
|
[18,44] |
Hydrodynamic cavitation |
Shear forces, creation, and extinction of cavities |
|
High energy consumption
Excess heat generation
Cavitation reactor designs are at an initial stage
Need optimization of critical parameters (orifice plate, inlet pressure, flow rate, cavitation number etc.)
|
[23,45] |
Microwave Irradiation |
Temperature increase, molecular energy increase |
|
High energy demand
Not suitable for commercial scale
High extraction temperature
Generation of free radicals
|
[39,41,46] |
Osmotic shock |
osmotic pressure-induced cell disruption and the release of the intracellular lipids |
Lower energy consumption
Easier scale-up
High yield
|
|
[25,47] |
Pulsed Electric Field (PEF) |
Transient permeabilization of cell membranes |
|
|
[48,49,50,51] |
Ultrasonication |
Cavitation, acoustic streaming, and liquid shear stress |
|
|
[52,53,54,55,56] |