Nanoemulsion Encapsulation of Fat-Soluble Vitamins: Advances in Technology, Bioaccessibility and Applications
Abstract
1. Introduction
| Conventional Emulsion | Nanoemulsion | |
|---|---|---|
| Droplet diameter | >500 nm | 10–500 nm |
| Thermodynamic stability | unstable | approaching thermodynamic stability |
| Kinetic stability | unstable | stability |
| Appearance | turbid to opaque | transparent or translucent or milky liquid |
| shape | spherical | spherical |
| polydispersity | often high (>40%) | typically low (<10–20%) |
| rheological properties | pseudoplastic/plastic flow | general Newtonian flow |
| emulsifiers | surfactants | surfactants plus co-surfactants |
2. Fat-Soluble Vitamins
2.1. Vitamin A
2.2. Vitamin D
2.3. Vitamin E
2.4. Vitamin K
3. Preparation of Nanoemulsions
3.1. High-Energy Methods
3.1.1. High-Pressure Homogenization (HPH)
3.1.2. Ultrasonic Homogenization (USH)
3.1.3. Microfluidic Homogenization (MFH)
3.2. Low-Energy Methods
3.2.1. Spontaneous Emulsification (SE)
3.2.2. Phase Inversion Temperature (PIT)
3.2.3. Phase Inversion Composition (PIC)
4. Impact of Nanoemulsion Encapsulation on FSVs
4.1. Factors Affecting the Stability of FSVs Encapsulated in Nanoemulsions
4.2. Effect on Bioavailability of FSVs Encapsulated in Nanoemulsions
4.2.1. Carrier Oil Type
4.2.2. Oil Phase Composition and Concentration
4.2.3. Emulsifier Type
4.2.4. Droplet Size
5. Safety
6. Applications in the Food Industry
6.1. Nutritional Fortification
6.2. Dairy Product Fortification
6.3. Functional Beverage Fortification
6.4. Edible Packaging Materials
7. Conclusions
Author Contributions
Funding
Institutional Review Board Statement
Informed Consent Statement
Data Availability Statement
Conflicts of Interest
References
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| Methods | Surfactant(s) (w/w%) | Oil (w/w%) | Vitamin Concentration (w/w%) | Emulsification Process | DZ (nm)/PDI | ZP (mV) | References |
|---|---|---|---|---|---|---|---|
| HSH | Lecithin (2 a) and Q-Naturale (0.5 a) | 10 a (VE:orange oil = 1:1) | 0.5 a | High-speed blending followed by high pressure homogenization (12,000 psi, 3 passes) | <200/- | −60 | [58] |
| Pea Protein (2 a) | 10 a (99 a flaxseed oil/corn oil/fish oil + 1 a vitamin D3) | 0.1 a | High-speed blending followed by high pressure homogenization (12,000 psi, 5 passes) | 200~550/- | - | [57] | |
| Pea Protein (1 a) and Soy Lecithin (1 a) | 0.5~5 a canola oil | 0.5 a | High-speed blending followed by high pressure homogenization (20 kpsi, 2 cycles) | <350/<0.3 | −25 | [11] | |
| USH | Tween 80 and soya lecithin (2.64–9.36%) | olive oil (10%) | 5.48–10.52% | Mixing with magnetic stirrer (8000 rpm, 7 min) followed by Sonication (20 kHz, 2.98–8.02 min) | 119.33 nm/- | - | [59] |
| KolliphorRH-40 (600 μL) + Ethylene Glycol (400 μL) | MCT Oil (100 μL) | - | Mixing with magnetic stirrer (1500 rpm, 10 min) followed by ultrasonication (50 kHz, 30 s) | 169/0.288 | −22.6 | [60] | |
| MFH | Quillaja Saponins (1 a) and Whey Protein Isolate (1 a) | 10 a corn oil | 0.1 a | Dual-channel microfluidizer (13 kpsi, 1 pass) | <150/- | −22.6 | [61] |
| Tween 80 (0.30 a) + Span 60 (0.19 a) | 1.29 a α-TOC | 1.29 a | Spontaneous emulsification followed by microfluidization (70 MPa, 3 cycles) | <200/- | - | [62] | |
| SE | TWEENÒ 80 (10 a) | 10 a (8 a VE + 2 a MCT oil) | 0.8 a | Magnetic stirring (500 rpm, 25 °C) | <200/<0.3 | - | [63] |
| Tween 80 (10 a) | 10 a MCT oil | 2.5 a | Magnetic stirring (500 rpm, 25 °C) | <200/<0.3 | - | [64] | |
| Tween 80 (3 b) + Pea Protein (3 b) | 3 b canola oil | 1 c | Magnetic stirring (800 rpm, 25 °C) | 207.7/0.31 | 3.7 | [65] | |
| PIT | Kolliphor®HS15 (10–40 b) + CCTG (10–25 b) | 10–30 b Leciva S70 | 0.2 b | Magnetic stirring (five temperature cycles, 85 °C–65 °C–85 °C–65 °C–85 °C–65 °C–85 °C–65 °C–85 °C–65 °C–85 °C) | <100/- | <20 | [66] |
| PIC | Tween 80 (5 a) | 3 a Mustard oil | 2 a | Magnetic stirring (400 rpm, 25 °C) | 86.45 ± 3.61/0.391 + 0.43 | - | [67] |
| Bioactive Compound | Fabrication Method | Surfactant(s) (w/w%) | Oil (w/w%) | Vitamin Dispersion Method and Concentration (w/w%) | Emulsification Process | DZ (nm)/PDI | Result | Reference |
|---|---|---|---|---|---|---|---|---|
| β-carotene | MSH and HPH | OSA/Tween 20/WPI/TW, DML (10 a) | Medium chain triglyceride (MCT) oil (10 d) | β-carotene was dissolved in MCT (140 °C, several seconds)/1 d | High speed blender (5000 rpm), HPH (100 MPa, 3 passes)/MSH (100 MPa, 3 passes) | <300 nm/(0.12 < PDI < 0.26) | Small molecule emulsifiers produce smaller droplets in nanoemulsions than large molecule ones, but macromolecular emulsifiers have better stability for β-carotene. | [80] |
| β-carotene | HPH | TPC (2.0 d)/WPI (1.0 d)/Tween 80 (1.0 d) | Corn oil (8 d) | β-carotene was dissolved in corn oil (sonicating 10 min, 50 °C, 30 min)/0.1 a | High-speed shearer (25,000 rpm, 3 min), HPH (75 MPa, 3 passes) | <140 nm/- | The stability in TPC stabilized nanoemulsions significantly higher than Tween 80 and WPI. | [81] |
| β-carotene | USH | Tween 80 and soya lecithin (2.64–9.36 a) | Olive oil (10 a) | β-carotene was dissolved in olive oil (−)/5.48–10.52 a | Magnetic stirrer (8000 rpm, 7 min), USH (20 kHz, 2.98–8.02 min) | 119.33 nm/- | As the surfactant concentration rises, the rate of β-carotene degradation diminishes. | [68] |
| β-carotene | MSH | Tween 20/lecithin/sodium caseinate/sucrose palmitate (2–8%) | Corn oil (4 a) | β-carotene was dissolved in corn oil (−)/0.5 a | High-speed shearer (9500 rpm, 2 min), MSH (30,000 psi, 5 times) | -/- | The stability and particle size behavior of β-carotene nanoemulsions during in vitro digestion are significantly influenced by the type and concentration of emulsifiers used. | [82] |
| β-carotene | MSH | SBL (0.25 a/0.75 a)/WPI (0.25 a/0.75 a) | Corn oil (10 a/30 a) | β-carotene was mixed with corn oil (65 °C, 3000 rpm for 1 min; 17,500 for rpm 2 min, sonication bath for 5 min repeated twice; 9000 rpm for 15 min)/20 d | Homogenizer (11,000 rpm, 2 min), MSH (130 MPa, 5 passes) | <500 nm/- | WPI (Cmax685 ng/mL) enhances retinol bioavailability more than SBL (Cmax394 ng/mL) due to better gut absorption. | [10] |
| VD3 | HPH | Pea protein (1 b, 5 b and 10 b) | Canola oil (0.5, 1, 2.5, 5 b) | Vitamin D3 was dissolved in canola oil/(11.7 e) | High-speed mixer (30,000 rpm, 2 min), HPH (10, 20 and 30 kpsi, 1–5 cycles) | 170–350 nm/(PDI < 0.3) | Pea protein nanoemulsions (P 230) exhibited approximately 5.3-fold higher transport efficiency across Caco-2 cells (Cancer coli-2) compared to free vitamin D suspension; The cellular uptake efficiency was also about 2.5 times higher than that of pea protein nanoemulsions (P 350) | [11] |
| β-carotene | MSH | Tween 20 (1.5 a) | Corn oil/MCT/orange oil (4 a) | Crystalline β-carotene was dissolved in oil phase (50 °C, <5 min, 1 h)/0.5 a | High-speed blender (2 min), MSH (9000 psi, 3 times) | 140–170 nm/- | The bioaccessibility was much higher for LCT (68%) nanoemulsions than for MCT (2%) nanoemulsions. | [83] |
| β-carotene | MSH | Tween 20 (0.5 a) | Olive or flaxseed oil (4 a) | β-carotene was dissolved in olive or flaxseed oil (−)/0.04 b | High-shear mixer (3 min), MSH (9000 psi, 3 times. | <200 nm/- | β-carotene bioaccessibility was greater for olive oil (65.2%) than for flaxseed oil (47.8%). | [84] |
| β-carotene | MSH | Tween 20 (1.5 a) | MCT or LCT (1 a/4 a) | β-carotene was dissolved in MCT or LCT (sonicating 1 min, 50 °C, 5 min)/0.5 a | High-shear mixer (10,000 rpm, 2 min), MSH (9000 psi, 3 times) | <500 nm/- | When the oil concentration was 4% (w/w), the bioaccessibility of the nanoemulsions first decreased and then increased with the increase in LCT content. When the oil concentration was 1% (w/w), the bioaccessibility increased from about 14% to 86% with the increase of LCT content. | [50] |
| β-carotene | HPH | Sodium caseinate (1 a) | MCT:LCT = 1:1 (10 a) | β-carotene was dissolved in oil phase (−)/0.6 a | High-shear blender (10,000 rpm, 2 min), HPH (12,000 psi, five times) | <180 nm/(PDI < 0.2) | The bioavailability increased with increasing lipid content. | [85] |
| β-carotene | MSH | Tween 20 (2 d) | Corn oil (20 d) | β-carotene was dissolved in corn oil (sonication 40 kHz, 1 min, 50 °C, 5 min)/0.1 d | High-shear blender (10,000 rpm, 2 min), MSH (12,000 psi, 3 passes) | <200 nm/- | The bioavailability of β-carotene shows a trend of first increasing and then decreasing with oil concentration | [86] |
| β-carotene | MSH | Tween 20 (1.5 a) | Corn oil (4 a) | β-carotene was dissolved in corn oil (sonicating 1 min, <50 °C, 5 min)/0.5 a | High-speed blender (10,000 rpm, 2 min), MSH (4 kpsi/9 kpsi, 5 times) | <400 nm/- | β-carotene bioaccessibility was found to decline progressively with a reduction in droplet size, with values dropping from approximately 59% (small emulsion) to 34% (large emulsion). | [87] |
| VD3 | HPH | Quillaja saponin (2 a) | Corn oil (10 a) | VD3 was dissolved in corn oil (−)/0.1 a | High-speed blender (2 min), HPH (12,000 psi, 3 cycles) | <400 nm/- | In vitro studies showed that the VD3 concentration of nanoemulsion was 3.94 times higher than traditional crude emulsion group. In vivo studies have shown that crude emulsion increases serum 25 (OH) VD levels by 36.04%, while supplementing VD with nanoemulsion increases VD levels by 73.10% | [88] |
| VD3 | MSH | Whey protein isolate (1 d) | Corn or mineral oil (10 a) | Vitamin D3 was dissolved in either corn oil (digestible oil) or mineral oil (indigestible oil) (−)/0.2 d | High-speed mixer (10,000 rpm, 2 min), MSH (12,000 psi, 5 times) | <170 nm/- | The extent of bioaccessibility was markedly greater in the nanoemulsions samples containing solely digestible oil (75.2%) compared to those with only indigestible oil (20.7%). | [89] |
| VD | HPH | Tween 20 (1 b) | STG or MCT/LCT (10 a) | Vitamin D was dissolved in STG or MCT/LCT (−)/0.1 a | High-speed ultra-Turrax blender (19.2 bar, 2 min), HPH (600 MPa, 5 cycles) | <200 nm/- | In comparison to MCT/LCT (45.40 ± 2.85%), STG (61.31 ± 2.90%) demonstrated a significantly greater VD bioaccessibility. | [90] |
| VD3 | HPH | Pea protein (2 a) | Flaxseed oil, corn oil, or fish oil (10 a) | Vitamin D3 was dissolved in oil phase (−)/1 a | High-shear blender (2 min), HPH (12,000 psi, 5 passes) | 200~550 nm/- | Vitamin bioaccessibility was notably superior in MUFA-emulsions (78%) compared with PUFA-emulsions (43%). | [57] |
| VD | USH | Tween 80 (20 c of buffer) | Corn oil20 a | Vitamin D was dissolved in corn oil (magnetic stirrer 30 min)/0.5 c of oil | High speed blender (10,000 rpm, 2 min), MSH (6000 psi, 15,000 psi, 3 times) | <600 nm/- | In vitro studies have demonstrated that the bioaccessibility of vitamin D is inversely related to droplet size. In vivo studies have indicated that emulsions with the largest droplet size have higher vitamin D absorption. | [91] |
| VE | MSH | Saponins (0.1 d) | Sunflower oil (10 d) | vitamin E was dissolved in sunflower oil (−)/2 d | High-speed homogenizer (15,500 rpm, 5 min), MSH (12,000 psi, four cycles) | 277 nm/- | The bioavailability of nanoemulsions is three times higher than that of traditional emulsions. | [92] |
| VE | MSH | Q-Natural® (1 d) | Corn oil (LCT) or MCT (10 d) | Vitamin E was dissolved in either corn oil (LCT) or MCT oil (−)/2.5 d | High-speed mixer (2 min), MSH (9000 psi, 4 cycles) | 228–270 nm/- | The bioaccessibility and conversion of a-tocopherol acetate to a-tocopherol was markedly greater in LCT (39% and 29%)-emulsions than in MCT (17% and 17%)-emulsions. | [51] |
| VE | MSH | Q-Naturale (0.5 d) | Corn oil (LCT) or MCT (10 a) | Vitamin E was dissolved in either corn oil (LCT) or MCT oil (−)/25 d | High-speed mixer (2 min), MSH (9000 psi, 5 cycles) | - | The bioaccessibility of LCT-emulsions (46%) than MCT-emulsions (19%) The conversion of α-tocopherol acetate to α-tocopherol was more pronounced in LCT (90%) than MCT (75%). | [93] |
| VE | MSH | Gum arabic or quillaja saponin or whey protein isolate (1.5 a) | Corn oil (10 a) | Vitamin E was dissolved in corn oil (−)/2 a | (−)/MSH (12,000 psi, 3 times) | - | The bioaccessibility of WPI-emulsions (85%) was higher for other two emulsions (65%). | [94] |
| VK1 | SE | Tween 80 (5–20%) | α-TOC | VK1 was dissolved in α-TOC (−)/5.48–10.52% | Organic phase slowly added into an aqueous phase under magnetic stirring at 700 rpm, stirred for 5 min at 1400 rpm. | <300 nm/(PDI < 0.2) | With the increases in the concentration of surfactant, there is a corresponding decline in droplets size. | [95] |
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Zeng, T.; Song, F.; Yang, Z.; Yan, X.; Jiang, L.; Li, D.; Huang, Z. Nanoemulsion Encapsulation of Fat-Soluble Vitamins: Advances in Technology, Bioaccessibility and Applications. Foods 2026, 15, 156. https://doi.org/10.3390/foods15010156
Zeng T, Song F, Yang Z, Yan X, Jiang L, Li D, Huang Z. Nanoemulsion Encapsulation of Fat-Soluble Vitamins: Advances in Technology, Bioaccessibility and Applications. Foods. 2026; 15(1):156. https://doi.org/10.3390/foods15010156
Chicago/Turabian StyleZeng, Ting, Fei Song, Zhen Yang, Xianghui Yan, Lianzhou Jiang, Dongze Li, and Zhaoxian Huang. 2026. "Nanoemulsion Encapsulation of Fat-Soluble Vitamins: Advances in Technology, Bioaccessibility and Applications" Foods 15, no. 1: 156. https://doi.org/10.3390/foods15010156
APA StyleZeng, T., Song, F., Yang, Z., Yan, X., Jiang, L., Li, D., & Huang, Z. (2026). Nanoemulsion Encapsulation of Fat-Soluble Vitamins: Advances in Technology, Bioaccessibility and Applications. Foods, 15(1), 156. https://doi.org/10.3390/foods15010156
