| Literature DB >> 34948437 |
Ramesh Kumar Saini1, Parchuri Prasad2, Xiaomin Shang3, Young-Soo Keum1.
Abstract
Extraction of lipids from biological tissues is a crucial step in lipid analysis. The selection of appropriate solvent is the most critical factor in the efficient extraction of lipids. A mixture of polar (to disrupt the protein-lipid complexes) and nonpolar (to dissolve the neutral lipids) solvents are precisely selected to extract lipids efficiently. In addition, the disintegration of complex and rigid cell-wall of plants, fungi, and microalgal cells by various mechanical, chemical, and enzymatic treatments facilitate the solvent penetration and extraction of lipids. This review discusses the chloroform/methanol-based classical lipid extraction methods and modern modifications of these methods in terms of using healthy and environmentally safe solvents and rapid single-step extraction. At the same time, some adaptations were made to recover the specific lipids. In addition, the high throughput lipid extraction methodologies used for liquid chromatography-mass spectrometry (LC-MS)-based plant and animal lipidomics were discussed. The advantages and disadvantages of various pretreatments and extraction methods were also illustrated. Moreover, the emerging green solvents-based lipid extraction method, including supercritical CO2 extraction (SCE), is also discussed.Entities:
Keywords: Bligh and Dyer method; Folch method; Soxhlet extraction; green solvents; lipidomics; pre-treatments; supercritical CO2 extraction
Mesh:
Substances:
Year: 2021 PMID: 34948437 PMCID: PMC8704327 DOI: 10.3390/ijms222413643
Source DB: PubMed Journal: Int J Mol Sci ISSN: 1422-0067 Impact factor: 5.923
The advantages and disadvantages of major pretreatment methods applied to the efficient extraction of lipids.
| Pretreatment Methods | Mode of Action | Advantages | Disadvantages | References |
|---|---|---|---|---|
| Acid-catalyzed hot-water | Release of bound lipids by uncoupling the lipid-protein and lipid-starch and intermolecular forces |
Cost-effective Can be applied for wet biomass High yield of bound lipids |
Degradation of thermolabile and acid-sensitive compounds | [ |
| 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 |
High energy demand Low recovery of lipids from cells with rigid cell wall | [ |
| Enzyme | Specific enzyme-substrateinteraction |
Simple Mild temprtaure conditions No sophisticated instrument required low energy requirements Selective extraction |
Long processing time and High cost of enzymes Extraction efficiency depends on the cell wall characteristics | [ |
| 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 |
High energy demand Not effective for samples of high moisture content Low recovery of lipids | [ |
| 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 | [ |
| High-speed shearing homogenization | Cavitation and shear forces |
Suitable for wet and dry biomass Efficient extraction Rapid |
Extensive heat generation High energy consumption | [ |
| Hydrodynamic cavitation | Shear forces, creation, and extinction of cavities |
High extraction efficiency from microalgae |
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.) | [ |
| Microwave Irradiation | Temperature increase, molecular energy increase |
Makes membranes porous which facilitates the effective extraction of lipid Short operating time More efficient than conventional heating |
High energy demand Not suitable for commercial scale High extraction temperature Generation of free radicals | [ |
| Osmotic shock | osmotic pressure-induced cell disruption and the release of the intracellular lipids |
Lower energy consumption Easier scale-up High yield |
Generation of waste saltwater Time-consuming | [ |
| Pulsed Electric Field (PEF) | Transient permeabilization of cell membranes |
High energetic efficiency Rapid Nonthermal method |
High initial capital investment-temperature extraction | [ |
| Ultrasonication | Cavitation, acoustic streaming, and liquid shear stress |
Extensively used pretreatment method Rapid High yield Energy-efficient process for optimum cell disintegration |
Generation of free radicals after prolonged treatment Not investigated for large scale applications | [ |
The list of solvents tested for the efficient extraction of lipids plants, animals, and microbes.
| Sample | Solvent Tested | Most Efficient | Reference |
|---|---|---|---|
| Argan ( | n-Hexane, ethyl acetate, acetone, n-hexane/acetone (1:1, | n-Hexane/acetone (1:1, | [ |
| Fresh egg yolk, boiled yolk, and yolk powder | Ethyl acetate/ethanol (in different ratios) and chloroform/methanol (2:1, | Ethyl acetate/ethanol at 2:1 and 1:1 ratios ( | [ |
| Human plasma | 1-Butanol/methanol (1:1 and 3:1, | 1-Butanol/methanol (1:1, | [ |
| Krill meal | Acetone, ethanol, isopropanol, ethyl acetate, isohexane, n-hexane, and subcritical butane | Ethanol and isopropanol | [ |
| Legumes | Chloroform/methanol (Folch method), n-hexane/isopropanol and n-hexane/acetone | Chloroform/methanol | [ |
| Milk | Butanol/methanol (3:1 and 1:1, | Butanol/methanol/chloroform (3:5:4, | [ |
| Microalga | Chloroform/methanol (1:2, | Dichloromethane/methanol (2:1, | [ |
| Spent coffee grounds | Ethyl acetate, ethanol, isopropanol, and n-propanol | Ethanol | [ |
| Thraustochytrids | Chloroform, diethyl ether, ethanol, heptane, n-hexane, isopropanol, methylene chloride, methanol, toluene, and in two solvent combinations at ratios of 1:1, 1:2, and 2:1 ( | Chloroform/methanol (2:1, | [ |
* In terms of extraction yield and health and environmental impact.
Figure 1Comparison of Bligh and Dyer method [8] and Folch method [7] of lipid extraction. * Assumption of 100% or 80% water in the sample. # For quantitative analysis, re-extraction of residues with 100 mL chloroform and rinsing with 50 mL chloroform is recommended.
The optimized parameters of supercritical CO2 extraction of lipids.
| Sample | Optimized Parameters | Reference |
|---|---|---|
| Argan seeds | The pressure of 297.71 bar and a temperature of 44.63 °C | [ |
| Argan seeds | The pressure of 400 bar and temperature 45 °C | [ |
| Grape seeds | The pressure of 500 bar and a temperature of 50 °C, and solvent flow of 8 g/min | [ |
| Microalage (20% water) | The pressure of 30 MPa, the temperature of 60 °C, with 0.4 kg/h of CO2 and 5% of co-solvent (ethanol) | [ |
| Microalga | Initial soaking period of 12 h (150 bar, 40 °C), flushing cycle (5 mL/min Flow rate, 30 min) | [ |
| Oats ( | The pressure of 550 bar, the temperature of 47.7 °C, and large particle size (>250 μm) | [ |
| Soybean seeds | Extraction with CO2/dimethyl ether (DME; 14:1, | [ |
Figure 2Illustrations showing the Matyash [12] method of lipid extraction.
Figure 3Illustrations showing the phase separation in chloroform-based (Folch method and Bligh and Dyer methods) [7,8] and methyl-tert-butyl ether (MTBE; Matyash Method) [12] based extraction methods. Compared to the lipid-rich chloroform layer below the aqueous phase (in chloroform-based extraction). Moreover, the nonextractable matrix, including proteins (forms at the bottom of the tube), can be removed by centrifugation easily.
Solid-phase extraction (SFE) of lipid classes.
| Sample | Desired Lipid Class | Sorbent | Separation Principle | Reference |
|---|---|---|---|---|
| Clam ( | Phospholipids | Titania-coated fibrous silica (TiO2/KCC-1) | Hydrophilic interaction | [ |
| Extra virgin olive oil | Phospholipids | Weak anionic exchange phase containing charged piperazine units, or graphitized carbon black | Ionic and lipophilic interactions | [ |
| French fries | Monounsaturated fatty acid methyl esters | Silver (Ag) nanoparticles-coated monolithic | Ag+-like affinity interaction | [ |
| Human breast milk | Phospholipids and glycerolipids | Mixture of C18 and zirconia-coated silica gel | Hydrophobic and Lewis acid/base interaction | [ |
|
| Phospholipids | Sulfobetaine (3-(trimethylammonio)propane-1-sulfonate) | Zwitterionic hydrophilic interaction | [ |
| Milk powder-based products | Oxysterols | C18 silica | Hydrophilic interaction | [ |
Advantages and disadvantages of various lipid extraction methods.
| Extraction Method | Advantages | Disadvantages | References |
|---|---|---|---|
| Accelerated solvent extraction (ASE) |
Automated and rapid (≈ 1 min) extraction method Low consumption of solvents commercially available technique |
High extraction temperature Special ASE Instrument required | [ |
| Green solvent assisted extraction |
Environment-friendly, non-toxic Food quality grade product |
Required an additional demulsification step | [ |
| Maceration and solvent extraction |
Standard methods for extraction High yield of lipids |
Laborious multistep process Use of toxic solvents Solvent residues in the product | [ |
| Soxhlet extraction |
Standard method of lipid extraction High yield of lipids |
Time-consuming Use of toxic solvents High extraction temperature | [ |
| Supercritical CO2 |
Environment-friendly, non-toxic, and non-flammable (CO2) Solvent-free extraction Food quality grade product Minimum/zero post-extraction processing |
High instrumentation cost High energy requirements Low yield of polar lipids | [ |