| Literature DB >> 36236142 |
Giovani Leone Zabot1, Fabiele Schaefer Rodrigues1, Lissara Polano Ody1, Marcus Vinícius Tres1, Esteban Herrera2, Heidy Palacin2, Javier S Córdova-Ramos2, Ivan Best3, Luis Olivera-Montenegro2,3.
Abstract
This review presents an updated scenario of findings and evolutions of encapsulation of bioactive compounds for food and agricultural applications. Many polymers have been reported as encapsulated agents, such as sodium alginate, gum Arabic, chitosan, cellulose and carboxymethylcellulose, pectin, Shellac, xanthan gum, zein, pullulan, maltodextrin, whey protein, galactomannan, modified starch, polycaprolactone, and sodium caseinate. The main encapsulation methods investigated in the study include both physical and chemical ones, such as freeze-drying, spray-drying, extrusion, coacervation, complexation, and supercritical anti-solvent drying. Consequently, in the food area, bioactive peptides, vitamins, essential oils, caffeine, plant extracts, fatty acids, flavonoids, carotenoids, and terpenes are the main compounds encapsulated. In the agricultural area, essential oils, lipids, phytotoxins, medicines, vaccines, hemoglobin, and microbial metabolites are the main compounds encapsulated. Most scientific investigations have one or more objectives, such as to improve the stability of formulated systems, increase the release time, retain and protect active properties, reduce lipid oxidation, maintain organoleptic properties, and present bioactivities even in extreme thermal, radiation, and pH conditions. Considering the increasing worldwide interest for biomolecules in modern and sustainable agriculture, encapsulation can be efficient for the formulation of biofungicides, biopesticides, bioherbicides, and biofertilizers. With this review, it is inferred that the current scenario indicates evolutions in the production methods by increasing the scales and the techno-economic feasibilities. The Technology Readiness Level (TRL) for most of the encapsulation methods is going beyond TRL 6, in which the knowledge gathered allows for having a functional prototype or a representative model of the encapsulation technologies presented in this review.Entities:
Keywords: bioactive compounds; chitosan; coating material; encapsulation efficiency; gum Arabic; polymers
Year: 2022 PMID: 36236142 PMCID: PMC9571964 DOI: 10.3390/polym14194194
Source DB: PubMed Journal: Polymers (Basel) ISSN: 2073-4360 Impact factor: 4.967
Polymers used for encapsulation of bioactive compounds and the main objectives of the studies.
| Polymer | Material | Encapsulated Bioactive Compound | Objective | References |
|---|---|---|---|---|
| Alginate | Ca alginate hydrogel granules | Reishi medicinal mushroom extract; Probiotic | Mask the bitter taste of extract and protect bioactive substances in oral administration to prolong cell viability under simulated gastrointestinal conditions and to protect the bioactive ingredients of Reishi mushroom along the storage | [ |
| Alginate | Macrospheres | Effective protection against diseases caused by | [ | |
| Alginate | Hydrogel | Jujube extract ( | Effect of encapsulation on antioxidant activity and protection of bioactive compounds | [ |
| Gum Arabic | Adhesive membrane | Cinnamon extract | Present an active food packaging material with more control over its pungent smell and quick release | [ |
| Gum Arabic | Nanocapsule | Savory essential oil | Alternative control method to the pre-emergence herbicide Metribuzin (Sencor®) | [ |
| Gum Arabic + Chitosan | Nanocapsule | Saffron ( | Increase bioavailability and protection of bioactive compounds through nanoencapsulation | [ |
| Cellulose | Powder particles | Vitamin A | Evaluate the emulsifying properties of cellulose particles and the ability to encapsulate with vitamin A | [ |
| Cellulose | Edible films | Probiotic bacteria ( | Search for new applications of coatings and films based on edible cellulose as carriers of various probiotics | [ |
| Celulose | Cryogels | Tebuconazole fungicide | Controlled release of Tebuconazole fungicide | [ |
| Chitosan + Cellulose | Nanoformulations | Citronella essential oil ( | Control of | [ |
| Chitosan | Nanoparticles | Peppermint oil ( | A nanoinsecticide to control | [ |
| Chitosan | Nanoliposomes | Caffeine | Retention and release of caffeine in the digestive system | [ |
| Pectin | Hydrogels | Lactase | Lactase encapsulated in pectin-based hydrogels | [ |
| Pectin | Film | Beetroot extract encapsulated in pectin from watermelon peel | Monitor the freshness of packaged chilled beef by developing a pH indicator film | [ |
| Pectin | Edible coating | Carvacrol/2-hydroxypropyl-β-cyclodextrin (CAR/HPβCD-IC) | Fungal inhibition against | [ |
| Shellac | Gels | Riboflavin | Form shellac-based gels and oat protein at neutral pH as a carrier to entrap and deliver active substances | [ |
| Shellac + Chitin | Composite microspheres | Yeast alcohol dehydrogenase (YADH) | Enzymatic immobilization by adsorption | [ |
| Shellac + Zein | Composite capsules | Curcumin | Controlled release of curcumin | [ |
| Xanthan gum + sodium alginate | Gels | Debranched pea starch | Improve the performance of debranched pea starch gels | [ |
| Xanthan gum | Edible films | Xanthan Gum solutions with glycerol acid | Increase lotus root storage stability | [ |
Figure 1Encapsulation and morphology of microcapsule.
Figure 2Schematic illustration of the emulsions.
Recent studies on encapsulation of bioactive peptides, fatty acids from vegetable oils, and vitamins (tocopherols).
| Bioactive Compounds | Sources | Encapsulation Material | Encapsulation Method | Process Conditions | Objective | Results | References |
|---|---|---|---|---|---|---|---|
| Bioactive peptides | Milk casein hydrolysate | Pullulan | Electrospinning (encapsulation of various bioactive compounds in the form of nanosized fibers) | Pullulan at 100, 120, and 140 g kg−1 | Improve the stability, and low bioavailability, masking the bitter taste | Production of clean bead-free peptides-loaded pullulan nanofibres at 120 and 140 g kg−1 with an encapsulation efficiency of 72–86% and a mean diameter of 60–133 nm | [ |
| Antioxidant peptides | Fish hydrolyzed collagen | Liposome | Freeze-dried | The highest encapsulation efficiency was found in SPC-CHO-0.5% HC ( | Improve stability and bioactivities | Lyophilized SPC-CHO-0.5% HC presented higher stability than lyophilized SPC-GLY-0.25% HC during storage for 28 days at 25 °C | [ |
| Antioxidant peptides | Fish protein hydrolysate | Not described | Spray dried | Enzymatic hydrolysis and chemical methods; spray dried at 180 °C inlet temperature to obtain powder; stored at −18 °C | Retention of antioxidant properties and microstructure | Visceral protein hydrolysate prepared with pepsin had better quality regarding antioxidant characteristics and papain in nutritional aspect | [ |
| Antihypertensive peptide | Whey protein hydrolysate <3 kDa | Alginate-collagen, alginate-gum Arabic, and alginate–gelatin | Extrusion method | Sonication for 15 min | Released antihypertensive peptides during gastrointestinal digestion | The highest efficiency was obtained in capsules of alginate—gum Arabic (95%); the released peptides incremented their ACE activity (85%) | [ |
| Antioxidant peptides | Flaxseed protein | Maltodextrin | Spray drying | Hydrolysate to maltodextrin (MD) to ratios (1:1, 1:2 and 1:3, | Retention of antioxidant properties and microstructure | Samples powders obtained by 1:3 ratio presented the highest radical scavenging activity for and ABTS+ (86%) and DPPH (69%); analysis of chemical structure indicated that hydrolysates were coated and dispersed within maltodextrin | [ |
| Antioxidant peptides | Milk Casein hydrolysate | Maltodextrin | Spray drying | Spraying was carried out by a pressure nozzle, compressed air flow rate of 0.54 m3 h−1, flow rate of 5 mL min−1, and inlet air temperature and outlet air temperature of 130 ± 1 °C and 70.0 ± 0.5 °C | Reduction of hygroscopicity and retention of antioxidant properties | Antioxidant activities were 90–99%, 77–92%, 77–93%, 95–99%, and 77–98% after the spray-drying process; hygroscopicity was reduced by microencapsulation ( | [ |
| Antioxidant peptides | Pink peach meat protein hydrolysate | Gum Arabic and maltodextrin | Emulsions-spray drying | Inlet air at 160 °C, outlet at 80 °C, nozzle diameter of 0.5 mm, air at 0.4 MPa, and spray flow feed rate of 15–20 mL min−1 | Retention of antioxidant properties; improvement of sensory properties | Antioxidant activity was improved; sensory properties were improved in a concentration of up to 3% | [ |
| Bioactive peptides | Azocasein | Not applicable | Double emulsions water-in-oil-in-water | Enzymatic hydrolysis | Improved bioavailability | Encapsulation efficiency of casein peptides was 93% | [ |
| Antioxidant peptides | Casein hydrolysate | Gum Arabic and maltodextrin | Freeze-dried | Enzymatic hydrolysis, coating material (10:0, 8:2, 6:4); ultrasonication at 40 kHz, 750 W, 12 mm diameter tip and with 50% pulse for 20 min | Improve the antioxidant and sensorial properties | Reduced bitterness if compared to the casein hydrolysate; maintenance of antioxidant activity (93%) | [ |
| Polyunsaturated fatty acids | Tea oil | Maltodextrin/Xanthan gum/Lysozyme nanoparticles | Pickering emulsion | Tea oil plus composite solutions at oil-water volume ratio of 1:5; homogenization for 3 min at 18,000 rpm to obtain the tea oil Pickering emulsion | Reduce lipid oxidation on tea oil powder | Encapsulation efficiency of 66% when 50% maltodextrin and 4% Xanthan gum/Xanthan gum/lysozyme nanoparticles was used; the surface of tea oil powder presented a relatively smooth porous microstructure | [ |
| Omega-3 fatty acid | Flaxseed oil | Maltodextrin | Coacervation | - | Maintaining stability | - | [ |
| Omega-3 and omega-6 fatty acids |
| Gum Arabic/whey protein/modified starch/sodium caseinate | Drying (spray drying, freeze drying)/supercritical emulsification/emulsion/coacervation | - | Prevents the oxidation of fatty acids | Microcapsules prepared with spray- and freeze-drying ranged between 10–400 and 20–5000 µm | [ |
| Unsaturated fatty acids | Drumstick oil ( | Maltodextrin/gum Arabic (25:75); (oil to wall ratio 1:4) | Spray drying | Inlet air at 180 °C, outlet at 85 °C, air pressure of 0.06 MPa and air flow rate of 73 m3 h−1 | To evaluate the protection of the encapsulating compound in drumstick oil | The range of emulsion droplet mean diameters was 1.94 to 4.92 µm; encapsulation efficiency of 91.05% with lower water activity; good oxidative stability; peroxide value was 7.63 to 8.07 meq of peroxide/kg of oil after 30 days of storage at 45 °C; particles size was 22.56 ± 0.63 µm;showed larger smooth-surfaced particles, which may indicate that viscosity of the emulsions and emulsifying capacity are higher. | [ |
| Omega-3 fatty acid | Chia seed oil | Soy protein microparticles | Supercritical CO2-assisted impregnation | 16 MPa impregnation pressure with ethanol as cosolvent (0.1-ethanol:oil ratio, | Protect bioactive compounds through microencapsulation and increase bioavailability | Encapsulation efficiency of 95% and a retention efficiency of 35%, showing excellent oxidative stability; microcapsules ranged between 1 and 10 μm, having a spherical form with occasional depressions but no pores or fissures; 95.69 ± 4.28% of the encapsulated oil is released upon exposure to gastrointestinal conditions and becomes available for absorption. | [ |
| Omega-3 fatty acid | Chia, camelina and echium oilseeds and wet microalgal lipids | Sodium caseinate and lactose (oil to wall ratio 1:4 ( | Spray drying | Inlet air at 170 °C, compressed air pressure of 0.5 MPa, air flow of 700 L min−1 and aspiration 70% | Produce microencapsulated lipid extracts from sources of omega-3 | Particles size ranged between 1.5 and 30 μm and they presented a spherical shape and a smooth surface without cracks; the chia fatty acid ethyl esters microcapsules had the best microencapsulation efficiency of 76.9%, while the echium microcapsules had the highest payload of 142 mg/g. | [ |
| Omega-3 fatty acid | Flaxseed oil | 4% gum Arabic and 16% soy protein isolate | Spray drying | Inlet air at 150 °C, outlet at 80–85 °C and flow rate of 4 mL min−1 | Evaluate the effect of flaxseed oil nano-encapsulation on stability, physical, color, rheological, textural, and organoleptic properties in egg-free cake | Nanoencapsulated flaxseed oil used as an egg replacer in cakes; had the greatest percentage of omega-3 fatty acids (30%); particle size less than 100 nm; encapsulation efficiency of 72%; moisture content of 4% and peroxide value of 1.1 meq/kg. | [ |
| Polyunsaturated fatty acids | Walnut oil | Fructooligosaccharide/soybean protein isolate (20% | Freeze drying | Temperature − 46 °C, pressure 4.1 Pa for 48 h | Evaluate the fructooligosaccharide/soy isolate protein | Microcapsules ranged between 121.51 and 162.02 µm; fructooligosaccharide reduces particle size and increases viscosity; microencapsulated walnut oil had a peroxide value of 26.84 meq/kg after 8 days of storage, compared to the walnut oil which reached a peroxide value of 74.56 meq/kg. | [ |
| Alpha-linolenic acid | Perilla oil; ( | γ-cyclodextrin | Inclusion complex | The formation of pseudorotaxane complexes that precipitate in aqueous media | Evaluate the thermal stability and bioavailability α-linolenic acid from perilla oil | The complexes may serve as an effective supply of α-linolenic acid to raise plasma omega-3 fatty acid levels | [ |
| Cinnamaldehy | Cinnamon essential oil | Carboxymethyl cellulose and polyvinyl alcohol | Pickering emulsions by in situ hydrophobization | Use oleic acid as a hydrophobic compound | Increase the shelf life of the bread | No fungal growth at 25 °C for 15 days; controlled release of cinnamon essential oil; fungal inhibition against | [ |
| Flavonoid karanjin | Polyuria | Interfacial polymerization | 400–500 rpm slow mixing | Evaluate the insecticidal activity of microencapsulated | High encapsulation efficiency of 87.41%; release kinetics was y = −0.0042 x + 6.4205; effective protection against | [ | |
| Monoterpene α-pinene | Juniper berry essential oil | Gum Arabic/maltodextrin (1:1); (oil to wall ratio 1:4, | Spray drying | Inlet air at 120 °C, outlet at 80 °C and 3.2 cm3 min−1 of feed flow rate | Evaluate properties of microcapsules | Particle size was 10.83 µm ± 1.86; encapsulation efficiency of 70.07% and a retention efficiency of 82.66%; powder has the following characteristics: 4.92% moisture, 10.18% hygroscopicity, 63.80% solubility, 72.83% porosity, and 3.23 min of dissolving time; depending on the kind of wall material, it took between 15 and 45 min for the oil to completely discharge; presents antimicrobial and antifungal activity; it can be used as a food preservative. | [ |
| Eugenol | Clove essential oil | Chitosan nanoparticles (oil to wall ratio 0.5:1) | Emulsification ( | Homogenize at 13,000 rpm for 10 min in ice bath conditions; for ionic gelation of the chitosan, sodium tripolyphosphate was added and agitated for 40 min | Improved antioxidant and antimicrobial activity by nanoencapsulation of clove essential oil | Particle size of 295.8 ± 45.6 nm; high retention rate (73.4%); high in vitro antimicrobial activity against | [ |
| Alpha-tocopherol | Wheat germ oil | 1.5% Sodium alginate and 2% pectin | Air atomization | O/W emulsion dropped; 5% ( | Increase antioxidant activity and thus shelf life and nutritional value of cookies | Encapsulation efficiency of 55.97%; maximum antioxidant activity of 41.1%; improved storage stability and shelf life of cookies; microencapsulated α-tocopherol can serve as an antioxidant to avoid autoxidation in fat-based bakery products. | [ |
| Alpha-tocopherol | Palm oil | Maltodextrin and sodium caseinate; (Core to wall ratio 1) | Spray drying | 1.5 mm nozzle diameter, 10 mL min−1 of feed flow rate, 55 kgf cm2 air pressure, 20,000–25,000 rpm atomization speed, inlet air at 110 °C and outlet at 90 °C | Demonstrate the encapsulating and protective capacity of the wall material for the microencapsulation of vitamin E | Encapsulation efficiency of 59.9 ± 0.017 to 71.5 ± 0.027%; particle size from 13 to 29 µm; moisture content from 4.5 to 4.98%, microcapsule considered soluble due to the short solubility time of 178 to 251 s. | [ |
| Alpha-tocopherol | Palm fatty acid distillate | Galactomannan and gum acacia | Spray drying | Inlet air at 180–200 °C and outlet at 90 °C | Evaluate emulsion and oxidative stability | Encapsulation efficiency between 60.68 and 70.01%; microcapsules ranged between 16 µm and 11 µm; a yield between 53.15 and 64.09%; moisture content from 3.40 to 3.08%; microencapsulation improved oxidative stability and absorption of vitamin E. | [ |
| Alpha-tocopherol | Vitamin E | Whey protein isolate; (Core to wall ratio 1:3) | (1) Spray drying; (2) Freeze-drying; (3) Spray freeze-drying | (1) Inlet temperature 100 °C, outlet temperature 80 °C and 4 mL min−1 feed flow rate; | Evaluate the effect of the three techniques of vitamin E microencapsulation | Encapsulation efficiencies and particle size of 90% and 195.8 µm for spray dried microcapsules, 86% and 279 µm for freeze-dried microcapsules, 89% and 145.3 µm for spray freeze-dried microcapsules, respectively; the rats showed plasma vitamin E concentrations of 7.35 at 4 h, 7.69 at 4 h, 9.45 µg/mL at 3 h; area | [ |
| (3) The temperature was kept between −25 °C and −10 °C with a vacuum of 0.8 torr, and then brought to 10 °C with a vacuum of 0.3 torr | under the curve were 109.84, 104.38 and 124.46 µg/(mL × h); spray freeze-drying microencapsulation improved the oral bioavailability by 1.13 and 1.19-fold compared to other techniques. | ||||||
| Vitamin E | Palm oil | Maltodextrin/Sodium caseinate (3:2:1) | Freeze drying | Temperature −41 °C and pressure 4 × 10−4 mbar | Effect on vitamin E encapsulation with selenomethionine | Encapsulated vitamin E with 5.6 mg selenomethionine improves solubility and bioavailability; particle size was 3.00 µm ± 0.55; release rates of vitamin E after 30 min in simulated gastric fluid solution and simulated intestinal fluid solution were 87% and 42%, respectively. | [ |
| Alpha-tocopherol | Vitamin E | Polycaprolactone | Supercritical fluid extraction of emulsions | Pressure 8 MPa and temperature 40 °C; CO2 flow rate of 7.2 kg h−1 kg−1 emulsion and acetone as solvent | Demonstrate the feasibility of supercritical fluid technique in the nano-encapsulation of liquid lipophilic compounds | High encapsulation efficiency of 90%; particle size was from 8 and 276 nm; spherical, core-shell, and non-aggregated nanocapsules were formed, according to morphological analyses; higher storage stability between 6 and 12 months. | [ |
| Alpha-tocopherol | Vitamin E | Polycaprolactone | Nanoprecipitation | At 30 °C in an ultrasonic bath, PCL was dissolved in acetone, lecithin, acetone-methanol mixture (60 to 40%, | Improve the carboxymethylcellulose film in the production of active packaging with α-tocopherol nanocapsules | High encapsulation efficiency of 88.43–99.66%; particle size ranged between 201.6 and 230.2 nm; alpha-tocopherol nanocapsules’ release behavior from CMC films might be best described by the Higuchi kinetic model; the maximum radical scavenging activity (68.85%) was found in films with 70% nanocapsules. | [ |
| Alpha-tocoferol | Vitamin E | Acid hydrolysis-carboxymethyl starch (H-CMS) and xanthan gum (XG) | Spray-drying | Inlet air temperature 190 ± 5 °C and outlet air temperature 80 ± 5 °C | Improved bioavailability | Microcapsules produced with substitution grades of 0.44 and a ratio of 1:20 (H-CMS/XG) demonstrated higher specific delivery in the small intestine, releasing 38.32% and 61.68% of vitamin E into simulated gastric and intestinal fluids, respectively | [ |
| Alpha-tocoferol | Vitamin E | Gelatin and gum Arabic | Complex coacervation | Adjust the pH with acetic acid (10% | Optimize by response surface methodology the conditions for vitamin E microencapsulation | High encapsulation efficiency (93.42%), when the core material is 4 g and surfactant is 0.5% (% | [ |
| Alpha-tocopherol | Vitamin E | Nano-hydroxyapatite as a Pickering stabilizer | Pickering emulsions | Uses a mixer with continuous mode; O/W ratio of 20/80 ( | Improved bioavailability, bioaccessibility and stability | Particle sizes were 7.53, 11.56 and 17.72 μm; improved bioaccessibility of vitamin E by 10.87 ± 1.04% for gelatin and 18.07 ± 2.90% for fortified milk | [ |
Technologies used for the microencapsulation of bioactive compounds.
| Microencapsulation | Method | Applications | References |
|---|---|---|---|
| Physical | Spray-drying | Phenolic acids, carotenoids | [ |
| Spray chilling | Pigments | ||
| Spray coating | Pigments | ||
| Supercritical microencapsulation—micronization | Carotenoids | ||
| Ionic gelation | Nutraceutical | ||
| Cocrystallization | Food ingredients | ||
| Freeze-drying | Carotenoids, Pigments | ||
| Fluidized bed coating | Carotenoids | ||
| Centrifugal extrusion | Food ingredients | ||
| Chemical | Interfacial polymerization | Food | [ |
| Molecular inclusion | Nutraceutical | ||
| In situ polymerization | Nutraceutical | ||
| Physical-chemical | Coacervation | Volatile flavor oils | [ |
| Complex coacervation | Lycopene | ||
| Emulsion-solvent evaporation | Food ingredients | ||
| Solidification emulsion | Food ingredients | ||
| Liposomes | Food ingredients, nutraceuticals |
Figure 3Advantages and applications of encapsulation in the agricultural sector.
Figure 4Advantages and applications of encapsulation in the food area.