NL2034548A - A Preparation Method for Embedding n-3 Long Chain Polyunsaturated Fatty Acid Microcapsules - Google Patents
A Preparation Method for Embedding n-3 Long Chain Polyunsaturated Fatty Acid Microcapsules Download PDFInfo
- Publication number
- NL2034548A NL2034548A NL2034548A NL2034548A NL2034548A NL 2034548 A NL2034548 A NL 2034548A NL 2034548 A NL2034548 A NL 2034548A NL 2034548 A NL2034548 A NL 2034548A NL 2034548 A NL2034548 A NL 2034548A
- Authority
- NL
- Netherlands
- Prior art keywords
- ppi
- sbp
- fish oil
- solution
- preparation
- Prior art date
Links
- 239000003094 microcapsule Substances 0.000 title claims abstract description 69
- 238000002360 preparation method Methods 0.000 title claims abstract description 26
- 235000020978 long-chain polyunsaturated fatty acids Nutrition 0.000 title description 3
- 235000021323 fish oil Nutrition 0.000 claims abstract description 105
- 239000000243 solution Substances 0.000 claims abstract description 71
- 239000007764 o/w emulsion Substances 0.000 claims abstract description 20
- 108010084695 Pea Proteins Proteins 0.000 claims abstract description 16
- 235000019702 pea protein Nutrition 0.000 claims abstract description 16
- 238000004945 emulsification Methods 0.000 claims abstract description 10
- 239000007921 spray Substances 0.000 claims abstract description 9
- 238000001694 spray drying Methods 0.000 claims abstract description 7
- 239000008055 phosphate buffer solution Substances 0.000 claims abstract description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 33
- 238000000034 method Methods 0.000 claims description 26
- 238000009833 condensation Methods 0.000 claims description 14
- 230000005494 condensation Effects 0.000 claims description 14
- 239000008363 phosphate buffer Substances 0.000 claims description 11
- 239000000203 mixture Substances 0.000 claims description 10
- 238000003756 stirring Methods 0.000 claims description 9
- 229920001277 pectin Polymers 0.000 claims description 8
- 239000001814 pectin Substances 0.000 claims description 8
- 235000010987 pectin Nutrition 0.000 claims description 8
- 235000016068 Berberis vulgaris Nutrition 0.000 claims description 6
- 241000335053 Beta vulgaris Species 0.000 claims description 6
- 238000001914 filtration Methods 0.000 claims description 4
- 239000012535 impurity Substances 0.000 claims description 4
- 230000036571 hydration Effects 0.000 claims description 2
- 238000006703 hydration reaction Methods 0.000 claims description 2
- 239000011550 stock solution Substances 0.000 claims 8
- 230000001804 emulsifying effect Effects 0.000 claims 6
- 238000004519 manufacturing process Methods 0.000 claims 2
- 101100481793 Arabidopsis thaliana TOC33 gene Proteins 0.000 claims 1
- 101150031304 ppi1 gene Proteins 0.000 claims 1
- 239000002131 composite material Substances 0.000 abstract description 38
- 239000006185 dispersion Substances 0.000 abstract description 21
- 239000000843 powder Substances 0.000 abstract description 13
- 238000005538 encapsulation Methods 0.000 abstract description 10
- 230000002776 aggregation Effects 0.000 abstract description 5
- 230000036425 denaturation Effects 0.000 abstract description 4
- 238000004925 denaturation Methods 0.000 abstract description 4
- 238000004220 aggregation Methods 0.000 abstract description 3
- 239000000839 emulsion Substances 0.000 description 28
- 239000002245 particle Substances 0.000 description 20
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 16
- 238000001000 micrograph Methods 0.000 description 11
- 230000003993 interaction Effects 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 10
- 241000251468 Actinopterygii Species 0.000 description 9
- 230000000694 effects Effects 0.000 description 9
- 239000003921 oil Substances 0.000 description 9
- 230000006399 behavior Effects 0.000 description 8
- 238000005259 measurement Methods 0.000 description 8
- 235000019198 oils Nutrition 0.000 description 8
- 238000001556 precipitation Methods 0.000 description 8
- 230000015572 biosynthetic process Effects 0.000 description 7
- 238000010586 diagram Methods 0.000 description 7
- 229920001222 biopolymer Polymers 0.000 description 6
- 238000002844 melting Methods 0.000 description 6
- 230000008018 melting Effects 0.000 description 6
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 6
- 238000001878 scanning electron micrograph Methods 0.000 description 6
- 238000001228 spectrum Methods 0.000 description 6
- 230000009881 electrostatic interaction Effects 0.000 description 5
- 235000013305 food Nutrition 0.000 description 5
- 230000002209 hydrophobic effect Effects 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 238000001157 Fourier transform infrared spectrum Methods 0.000 description 4
- 230000007423 decrease Effects 0.000 description 4
- 238000004626 scanning electron microscopy Methods 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 3
- 229910052782 aluminium Inorganic materials 0.000 description 3
- 238000004458 analytical method Methods 0.000 description 3
- 230000003247 decreasing effect Effects 0.000 description 3
- 235000014113 dietary fatty acids Nutrition 0.000 description 3
- 239000000194 fatty acid Substances 0.000 description 3
- 229930195729 fatty acid Natural products 0.000 description 3
- 150000004665 fatty acids Chemical class 0.000 description 3
- 235000018102 proteins Nutrition 0.000 description 3
- 108090000623 proteins and genes Proteins 0.000 description 3
- 102000004169 proteins and genes Human genes 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 238000005411 Van der Waals force Methods 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 2
- 238000005054 agglomeration Methods 0.000 description 2
- 150000001413 amino acids Chemical class 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 239000002775 capsule Substances 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 238000012512 characterization method Methods 0.000 description 2
- 230000005591 charge neutralization Effects 0.000 description 2
- 238000003053 completely randomized design Methods 0.000 description 2
- 239000002270 dispersing agent Substances 0.000 description 2
- 238000005189 flocculation Methods 0.000 description 2
- 230000016615 flocculation Effects 0.000 description 2
- 150000002632 lipids Chemical class 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000000178 monomer Substances 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000004533 oil dispersion Substances 0.000 description 2
- 238000005191 phase separation Methods 0.000 description 2
- 230000005588 protonation Effects 0.000 description 2
- 239000013049 sediment Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 230000006641 stabilisation Effects 0.000 description 2
- 238000011105 stabilization Methods 0.000 description 2
- DCXXMTOCNZCJGO-UHFFFAOYSA-N tristearoylglycerol Chemical compound CCCCCCCCCCCCCCCCCC(=O)OCC(OC(=O)CCCCCCCCCCCCCCCCC)COC(=O)CCCCCCCCCCCCCCCCC DCXXMTOCNZCJGO-UHFFFAOYSA-N 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 241000219310 Beta vulgaris subsp. vulgaris Species 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 208000024172 Cardiovascular disease Diseases 0.000 description 1
- 229920001661 Chitosan Polymers 0.000 description 1
- 239000004278 EU approved seasoning Substances 0.000 description 1
- 238000001134 F-test Methods 0.000 description 1
- IAJILQKETJEXLJ-UHFFFAOYSA-N Galacturonsaeure Natural products O=CC(O)C(O)C(O)C(O)C(O)=O IAJILQKETJEXLJ-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- QIVBCDIJIAJPQS-VIFPVBQESA-N L-tryptophane Chemical compound C1=CC=C2C(C[C@H](N)C(O)=O)=CNC2=C1 QIVBCDIJIAJPQS-VIFPVBQESA-N 0.000 description 1
- 235000021536 Sugar beet Nutrition 0.000 description 1
- QIVBCDIJIAJPQS-UHFFFAOYSA-N Tryptophan Natural products C1=CC=C2C(CC(N)C(O)=O)=CNC2=C1 QIVBCDIJIAJPQS-UHFFFAOYSA-N 0.000 description 1
- 108010046377 Whey Proteins Proteins 0.000 description 1
- 102000007544 Whey Proteins Human genes 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 229920001586 anionic polysaccharide Polymers 0.000 description 1
- 150000004836 anionic polysaccharides Chemical class 0.000 description 1
- 150000001450 anions Chemical class 0.000 description 1
- 101150099875 atpE gene Proteins 0.000 description 1
- 101150018639 atpFH gene Proteins 0.000 description 1
- 101150048329 atpH gene Proteins 0.000 description 1
- 238000005102 attenuated total reflection Methods 0.000 description 1
- 230000000975 bioactive effect Effects 0.000 description 1
- 230000004641 brain development Effects 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 235000014633 carbohydrates Nutrition 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 1
- -1 carboxylate ions Chemical class 0.000 description 1
- 230000036996 cardiovascular health Effects 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 229930002875 chlorophyll Natural products 0.000 description 1
- 235000019804 chlorophyll Nutrition 0.000 description 1
- ATNHDLDRLWWWCB-AENOIHSZSA-M chlorophyll a Chemical compound C1([C@@H](C(=O)OC)C(=O)C2=C3C)=C2N2C3=CC(C(CC)=C3C)=[N+]4C3=CC3=C(C=C)C(C)=C5N3[Mg-2]42[N+]2=C1[C@@H](CCC(=O)OC\C=C(/C)CCC[C@H](C)CCC[C@H](C)CCCC(C)C)[C@H](C)C2=C5 ATNHDLDRLWWWCB-AENOIHSZSA-M 0.000 description 1
- 238000005352 clarification Methods 0.000 description 1
- 238000005354 coacervation Methods 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 235000011850 desserts Nutrition 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 235000005911 diet Nutrition 0.000 description 1
- 230000037213 diet Effects 0.000 description 1
- 238000000113 differential scanning calorimetry Methods 0.000 description 1
- 238000001938 differential scanning calorimetry curve Methods 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 230000008034 disappearance Effects 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 235000019197 fats Nutrition 0.000 description 1
- 229940013317 fish oils Drugs 0.000 description 1
- 235000013312 flour Nutrition 0.000 description 1
- MHMNJMPURVTYEJ-UHFFFAOYSA-N fluorescein-5-isothiocyanate Chemical compound O1C(=O)C2=CC(N=C=S)=CC=C2C21C1=CC=C(O)C=C1OC1=CC(O)=CC=C21 MHMNJMPURVTYEJ-UHFFFAOYSA-N 0.000 description 1
- 235000011194 food seasoning agent Nutrition 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 238000000892 gravimetry Methods 0.000 description 1
- 239000011440 grout Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 230000000877 morphologic effect Effects 0.000 description 1
- 230000004660 morphological change Effects 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- VOFUROIFQGPCGE-UHFFFAOYSA-N nile red Chemical compound C1=CC=C2C3=NC4=CC=C(N(CC)CC)C=C4OC3=CC(=O)C2=C1 VOFUROIFQGPCGE-UHFFFAOYSA-N 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- 235000020660 omega-3 fatty acid Nutrition 0.000 description 1
- 239000006174 pH buffer Substances 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 238000003921 particle size analysis Methods 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 238000010587 phase diagram Methods 0.000 description 1
- 238000005498 polishing Methods 0.000 description 1
- 229920000447 polyanionic polymer Polymers 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 235000020777 polyunsaturated fatty acids Nutrition 0.000 description 1
- 125000002924 primary amino group Chemical group [H]N([H])* 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000000750 progressive effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 235000015067 sauces Nutrition 0.000 description 1
- 229940071440 soy protein isolate Drugs 0.000 description 1
- 238000007619 statistical method Methods 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000002076 thermal analysis method Methods 0.000 description 1
- 238000004448 titration Methods 0.000 description 1
- UFTFJSFQGQCHQW-UHFFFAOYSA-N triformin Chemical compound O=COCC(OC=O)COC=O UFTFJSFQGQCHQW-UHFFFAOYSA-N 0.000 description 1
- 125000001493 tyrosinyl group Chemical group [H]OC1=C([H])C([H])=C(C([H])=C1[H])C([H])([H])C([H])(N([H])[H])C(*)=O 0.000 description 1
- 229910021642 ultra pure water Inorganic materials 0.000 description 1
- 239000012498 ultrapure water Substances 0.000 description 1
- 238000007473 univariate analysis Methods 0.000 description 1
- 230000000007 visual effect Effects 0.000 description 1
- 235000021119 whey protein Nutrition 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L33/00—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
- A23L33/10—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof using additives
- A23L33/115—Fatty acids or derivatives thereof; Fats or oils
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23D—EDIBLE OILS OR FATS, e.g. MARGARINES, SHORTENINGS OR COOKING OILS
- A23D9/00—Other edible oils or fats, e.g. shortenings or cooking oils
- A23D9/02—Other edible oils or fats, e.g. shortenings or cooking oils characterised by the production or working-up
- A23D9/04—Working-up
- A23D9/05—Forming free-flowing pieces
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L29/00—Foods or foodstuffs containing additives; Preparation or treatment thereof
- A23L29/03—Organic compounds
- A23L29/045—Organic compounds containing nitrogen as heteroatom
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23P—SHAPING OR WORKING OF FOODSTUFFS, NOT FULLY COVERED BY A SINGLE OTHER SUBCLASS
- A23P10/00—Shaping or working of foodstuffs characterised by the products
- A23P10/30—Encapsulation of particles, e.g. foodstuff additives
- A23P10/35—Encapsulation of particles, e.g. foodstuff additives with oils, lipids, monoglycerides or diglycerides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
- B01J13/02—Making microcapsules or microballoons
- B01J13/04—Making microcapsules or microballoons by physical processes, e.g. drying, spraying
- B01J13/043—Drying and spraying
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
- B01J13/02—Making microcapsules or microballoons
- B01J13/06—Making microcapsules or microballoons by phase separation
- B01J13/10—Complex coacervation, i.e. interaction of oppositely charged particles
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
- A23V2002/00—Food compositions, function of food ingredients or processes for food or foodstuffs
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Polymers & Plastics (AREA)
- Food Science & Technology (AREA)
- Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Organic Chemistry (AREA)
- Nutrition Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Dispersion Chemistry (AREA)
- Mycology (AREA)
- Biophysics (AREA)
- Molecular Biology (AREA)
- Manufacturing Of Micro-Capsules (AREA)
- Fats And Perfumes (AREA)
Abstract
The invention discloses a preparation method of fish oil microcapsules based on emulsification and aggregation of pea protein isolate, which comprises the following steps: 81. Preparation of PPI solution and SBP solution: PPl and SBP are dissolved respectively in phosphate buffer solution and stirred until fully dissolved to obtain PPl reserve solution and SBP reserve solution respectively; 82. Preparation of PPI stabilized oil-in-water emulsion of fish oil: PPl reserve solution was stirred and mixed with FO to obtain PPl oil-in- water emulsion of fish oil; 83. Preparation of FO-PPl-SBP complex condensates: PPl fish oil in water emulsion was mixed with SBP reserve solution, pH value was adjusted to 3.5- 4.5, and then standing for 24 hours to obtain FO-PPl-SBP complex condensates. 84. Preparation of fish oil microcapsules: the composite condensates of FO-PPl-SBP were sent into the micro spray dryer to form fish oil microcapsules through spray drying; By using FO- PPl-SBP composite condensate as the feed dispersion of fish oil microcapsules, this application greatly improves the powder yield, payload and encapsulation rate of fish oil microcapsules, and improves the denaturation temperature and network thermal stability of fish oil microcapsules
Description
Chongqing University of Education, CQUE 23/029 NL
A Preparation Method for Embedding n-3 Long Chain
Polyunsaturated Fatty Acid Microcapsules
The invention relates to the technical field of fish oil microcapsule preparation, in particular to a fish oil microcapsule based on emulsification and condensation of pea protein isolate and a preparation method thereof.
Background Technology
A large number of studies have shown that w-3 long-chain polyunsaturated fatty acids (n-3 LC-PUFA) are one of the most effective bioactive lipids to improve human health, which can maintain infant visual and brain development, maintain cardiovascular health, and improve cardiovascular disease (CVD). To meet the demand for w-3 fatty acids in daily diets and communicate their benefits to consumers through traditional means, the food industry has worked to incorporate them into a variety of foods. Typically, w-3 fatty acids are found naturally in the form of triacylglycerol (TAG), such as Marine fish oil (also known as omega- 3 fish oil). As a result, they are extremely low in water solubility and generally do not disperse directly in water-based foods such as drinks, desserts, seasonings and sauces. Therefore, how to improve the dispersion of w-3 fatty acids in hydrophilic food substrates has been a major challenge for the food industry.
In view of the above shortcomings of the prior art, the invention aims to provide a method for preparing fish oil microcapsules based on emulsification and condensation of pea protein isolate.
Further, the application provides a fish oil microcapsule based on emulsification and condensation of pea protein isolate.
To realize the above purposes, the technical means adopted by the invention are:
A method for preparing fish oil microcapsules based on emulsification and condensation of pea protein isolate comprises the following steps:
S1. Preparation of PPI solution and SBP solution: PPI and SBP were dissolved in phosphate buffer solution and stirred until fully dissolved to obtain PPI reserve solution and
SBP reserve solution respectively;
S2. Preparation of PPI stabilized oil-in-water emulsion for fish oil: PPI reserve solution prepared in Step S1 was mixed with FO at a mass ratio of 9:1 to obtain PPI oil-in-water emulsion for fish oil;
S3. Preparation of FO-PPI-SBP complex condensate: The PPI fish oil in water emulsion prepared in Step S2 and SBP reserve solution prepared in Step S1 were mixed according to the mass ratio of 5:1, the pH value was adjusted to 3.5~4.5, and then stood at 4°C for 24 hours to obtain FO-PPI-SBP complex condensate.
S4. Preparation of fish oil microcapsules: the FO-PPI-SBP composite condensates prepared in Step S3 were sent to the micro spray dryer at a feed rate of 0.15L /h and a suction flow rate of 40 L/h, and fish oil microcapsules were formed through spray drying.
Additional aspects and advantages of this application will be given in part in the description below, and in part will become apparent from the description below, or will become known through the practice of this application.
In order to more clearly illustrate the specific implementation methods of the invention or the technical scheme in the prior art, a brief introduction of the drawings required to be used in the description of the specific implementation methods or the prior art is presented below. In all drawings, similar elements or parts are generally identified by similar drawings markings. In the drawings, the components or parts are not necessarily drawn to the actual scale.
Figure 1a shows the Zeta (2) potential diagram of PPI solution, SBP solution, oil-in- water emulsion of PPI stabilized fish oil and FO-PPI-SBP composite condensate.
Figure 1b shows the average particle diameter of PPI stabilized oil-in-water emulsion and FO-PPI-SBP composite condensate.
Figure 2a shows the phase diagram of the PPI stable FO emulsion and FO-PPI-SBP complex dispersion during the acid titration process.
Figure 2b shows the appearance of FO-PPI-SBP composite dispersion changing with pH value.
Wherein, o represents the cloudy solution; A represents precipitation and turbid solution; = represents precipitation and clear solution;
Figure 3a shows the CLSM micrograph of PPI reserve solution with pH value of 7.0.
Figure 3b shows the CLSM micrograph of SBP reserve solution with pH value of 7.0.
Figure 3c shows the CLSM micrograph of PPI water-in-water fish oil emulsion with pH value of 7.0.
Figure 3d shows the CLSM micrograph of PPI fish oil in water emulsion with pH value of 3.5.
Figure 3e shows the CLSM micrograph of FO-PPI-SBP complex condensates with pH value of 7.0.
Figure 3f shows the CLSM micrograph of FO-PPI-SBP complex condensates with pH value of 4.5.
Figure 3g shows the CLSM micrograph of FO-PPI-SBP complex condensates with pH value of 4.0.
Figure 3h shows the CLSM micrograph of FO-PPI-SBP complex condensates with pH value of 3.5.
Figure 4a shows the microstructure of PPI water-in-water fish oil emulsion with pH value of 3.5.
Figure 4b shows the microstructure of FO-PPI-SBP complex condensates with pH value of 4.5.
Figure 4c shows the microstructure of FO-PPI-SBP composite condensates with pH value of 4.0.
Figure 4d shows the microstructure of FO-PPI-SBP complex condensates with pH value of 3.5.
Figure 5 shows FTIR spectra of different wall materials.
Figure 6 shows the DSC thermogram of fish oil microcapsules prepared by different dispersion systems.
Figure 7a shows the SEM micrograph of SBP.
Figure 7b shows the SEM micrograph of PPI.
Figure 7c shows the SEM micrograph of PPI water-in-water fish oil emulsion.
Figure 7d shows the SEM micrograph of FO-PPI-SBP composite condensate with pH value of 4.5.
Figure 7e shows the SEM micrograph of FO-PPI-SBP composite condensate with pH value of 4.0.
Figure 7f shows the SEM micrograph of FO-PPI-SBP complex condensate with pH value of 3.5.
Specific Implementation Methods
The invention is further described in combination with specific implementation methods as follows:
Implementation methods
This implementation method provides a method for preparing fish oil microcapsules based on emulsification and condensation of pea protein isolate, consisting of the following steps:
S1. Preparation of PPI solution and SBP solution: PPI (pea protein isolate) and SBP (beet pectin) were dissolved in phosphate buffer and stirred until fully dissolved, respectively, to obtain PPI reserve solution and SBP reserve solution, wherein the mass concentration of said PPI reserve solution is 2.22wt%, pH is 7.0, and the mass concentration of said SBP reserve solution is 0.4wt%. The pH is 7.0.
The preparation of PPI solution includes the following steps:
S111. The PPI was dissolved in the phosphate buffer and stirred with a mechanical agitator at 500rpm at room temperature for 0.5 h to make the PPI fully dissolved in the phosphate buffer; The concentration of phosphate buffer is 10mM, pH is 7.0, and the temperature is maintained at 21-22°C.
Add 0.1-2M NaOH solution into the solution prepared by Step S111, adjust its pH value to 9.5, stir for 2 hours to promote hydration, then add 0.1-2M HCI to adjust the pH of the solution to 7.0, stir for 10-12h to ensure that the solution is fully dissolved.
The solution prepared by Step S112 was centrifuged at 6000rpm and 4°C for 15 min, and the insoluble impurities were removed by filtration. The pH value of the solution was checked again, and 0.1-2M NaOH or HCI was used to adjust the pH value to 7.0 if necessary to obtain a PPI reserve solution with a mass concentration of 2.22wt%.
The preparation of SBP solution includes the following steps:
S121. The beet pectin was dispersed in the phosphate buffer and stirred with a mechanical mixer at 500rpm at room temperature for 5 hours, so that the beet pectin was fully dissolved in the phosphate buffer. Then NaOH or HCI was added to adjust the pH value of the solution to 7.0; The concentration of phosphate buffer is 10mM, pH is 7.0, and the temperature is maintained at 21-22°C.
The solution prepared by Step S121 was centrifuged at 6000 rpm and 4°C for 15 min, and the insoluble impurities were removed by filtration. The pH value of the solution was checked again, and 0.1-2M NaOH or HCI was used to adjust the pH value to 7.0 if necessary to obtain the SBP reserve solution with a mass concentration of 0.4 %.
S2. Preparation of PPI stabilized oil-in-water emulsion for fish oil: PPI reserve solution prepared in Step S1 was mixed with FO (fish oil) in accordance with the mass ratio of 9:1, and a high-speed mixer was used to mix and stir at 10000 rpm for 2 minutes to prepare PPI oil-in-water emulsion for fish oil.
In order to obtain the fine emulsion drops, the coarse emulsion prepared was homogenized three times by a two-stage high-pressure valve homogenizer, with the pressure of 5000 psi in the first stage and 500 psi in the second stage, respectively. The final emulsion consisted of 10% fish oil and 2.22% PPI reserve solution.
S3. Preparation of FO-PPI-SBP complex condensates: PPI fish oil in water emulsion prepared in Step S2 and SBP reserve solution prepared in Step S1 were mixed according to the mass ratio of 5:1. Stir the mixture magnetically at 500 rpm for 10 minutes to mix the two solutions well. Adjust pH from 7.0 to 3.5 to 4.5 by adding HCI (0.1-2.0M). The dilution effect and conductivity change of the mixed solution can be reduced by using different concentrations of HCI. Finally, the aqueous mixture of FO-PPI-SBP was left to stand at 4°C for 24 hours to achieve phase equilibrium.
S4. Preparation of fish oil microcapsules: The FO-PPI-SBP composite condensates prepared in Step S3 were sent to the micro spray dryer at a feed rate of 0.15L /h and a 5 suction flow rate of 40 L/h to form fish oil microcapsules.
Inlet and outlet air temperatures should be maintained at 180°C and 105°C respectively.
The above operating parameters were optimized through preliminary experiments. The total solids content of all prepared mixtures is approximately 6.0-6.2 %. All the spray-dried powders were collected and stored in glass bottles at 4°C for characterization.
In this implementation method, EPA content in fish oil 29%, DHA content >12.5%, total n-3 PUFA content in triglyceride >30%; Pea protein isolate (PPI) is extracted from commercial pea flour by alkali extract-isoelectric precipitation method and its composition is 79.50% protein, 5.28% moisture, 0.77% fat, 4.61% crude ash and 9.84% carbohydrate. Beet pectin (SBP). The sodium hydroxide (NaOH), hydrochloric acid (HCI) and other chemicals and reagents used in this application are analytical grade. All solutions are prepared with ultra-pure water.
Case Contrast
Different from the implementation method, in this ratio, after preparing PPI stabilized fish oil in-water emulsion in Step S2, the PPI stabilized fish oil in-water emulsion is directly sent into Buchi micro spray dryer to prepare fish oil microcapsules.
In order to further characterize the structure and properties of PPI solution, SBP solution, PPI stabilized fish oil oil-in-water emulsion, FO-PPI-SBP composite condensate and fish oil microcapsules prepared in this application, the above solutions or products will be tested and analyzed as follows:
Test method: 1. Surface charge and particle size analysis of the feed dispersion
The surface charge and particle size of PPI stabilized emulsion and FO-PPI SBP complex dispersants were measured with pH(7.0-3.0) and reported as Z potential (, mV) and Z-mean diameter (nm), respectively. Before each measurement, the sample was diluted 20 times with the corresponding pH buffer and equilibrated at 25°C for 2 minutes. All measurements are taken in duplicate, with three readings recorded for each measurement. 2. Construction of state diagram
After standing for 24h, the state diagram of PPI stabilized emulsion and FO-PPI-SBP was obtained. After standing for 24 hours, state maps of the PPI stabilized emulsion and
FO-PPI-SBP complex dispersion were drawn based on observations of each phase equilibrium mixture. The phase is divided into five groups, marked with three symbols, namely: o,A.® represents turbidity solution, precipitation and turbidity solution and precipitation and clarification solution respectively. 3. Characterization of spray dried fish oil microcapsules 3.1 Encapsulation Efficiency (EE)
The surface oil content was measured by dispersing 2.5g microencapsulated powder in 10 mL hexane and rotating it for 2 min. The grout was then centrifuged at ambient temperature at 4000rpm for 10 min. Then wash the sediment twice and recover all the supernatant. The hexane was removed by nitrogen washing for 6h and the surface oil content was determined by gravimetry. The total oil content of the dry microcapsules (2.59) was determined by Soxhlet extractor. Then the solvent was completely removed by rotary evaporator, and the total oil content was determined by gravimetric method. The encapsulation efficiency (EE) of microcapsules was calculated using the following method.
EE=(Wt-Ws)/Wtx 100% where, Wt and Ws were the mass of total oil and surface oil of microcapsules, respectively (9). 3.2 Differential scanning calorimetry
The thermal properties of spray dried samples and control samples were studied by differential scanning calorimeter. Place a sample containing 10uL of distilled water (about 3.5 mg) into a 40 uL aluminum pot. Then, seal the pot and balance at room temperature overnight to distribute the water evenly. Samples were measured from 20 °C to 120 °C at a heating rate of 10 °C /min using a sealed empty aluminum disk as a reference. 3.3 Fourier Transform infrared spectrum
FTIR spectra of spray-dried samples and control samples were recorded at 25°C using a spectrophotometer equipped with a attenuated total reflection attachment, a Globar (MIR) source, a KBr beam separator, and a MCT detector. By accumulating 32 scans at a resolution of 4 cm-1, the sample was scanned in absorption mode from 4000 to 400 cm-1.
Sample background was collected before measurement. 3.4. The surface morphology was observed by scanning electron microscopy
The spray-dried powder adheres to a bonded carbon sheet on a cylindrical aluminum bracket, and the excess is blown off with a nitrogen stream. Then, the sample is sputtered and plated with gold to make it conductive. Finally, the same scanning electron microscope is used for detection. A micrograph (5000x) was selected as a representative of each sample. 5. Statistical analysis
The experimental data were processed in a completely randomized design (CRD) with two replicates. At least two measurements were made using the newly prepared sample, and the measurements were expressed as mean + standard deviation. Univariate analysis of variance and the F-test of SAS software were used to protect the least significant difference method for significant differences between the means (p< 0.05) analysis.
Test results and analysis 1. Effect of pH value on surface charge and particle size of fish oil dispersion
The formation of complex condensates between PPI and SBP is realized by electrostatic attraction between them. At a fixed biopolymer ratio (PPI/SBP=5:1), the environmental pH value is the main factor that determines the electrostatic interaction strength. The surface charge (Z- potential) and particle size (z-mean) of each dispersion were measured in order to determine the appropriate pH range for the formation of the fish
FO-PPI-SBP complex condensates. The effect of pH on the surface charge and particle size of PPI stabilized fish oil emulsions was also measured for comparison.
The measurement results are shown in Figure 1, where Figure 1a is the Zeta (0) potential diagram of PPI solution, SBP solution, PPI stabilized oil-in-water emulsion of fish oil and FO-PPI-SBP composite condensate, and Figure 1b is the average particle diameter of PPI stabilized oil-in-water emulsion of fish oil and FO-PPI-SBP composite condensate.
As shown in Figure 1a, the Z potential of PPI solution values is -24.17mV when it at pH=7.0, it is +27.18mV when it at pH=3.0, and zero net charge occurs at pH=4.7. The ( potential of SBP solution is negative throughout the pH range, which is a common surface charge pattern for anionic polysaccharides. The Z potential of SBP solution decreased gradiently when the pH value decreased from 7.0 to 5.0. The net value of the Z potential drops sharply with a further drop in pH value. This is because the SBP of galacturonic acid carboxyl functional groups on the unit (pKa= 3.5) caused by the protonation between. The Z potential of fish oil is between monomer PPI and monomer SBP at pH 7.0-3.0, and net zero charge occurs at pH 3.5. In general, composite condensation driven by electrostatic attraction requires that biopolymers have opposite electric charges. According to the results of {- potential, when pH is less than 4.5, the positive charge PPI(-NH4+) can generate electrostatic attraction with the anion SBP(-coo-) to form the complex condensation. For PPI and stable water bag fish oil emulsion, fish oil droplets of zeta potential and PPI solution is very similar, when pH value away from the isoelectric point, net charge increase (the ieps require curricular modules = 4.7).
The dependence between the z mean diameter and pH value of fish oil emulsion and fish FO-PPI-SBP composite dispersion is shown in Figure 1b. At different pH values, the particle size of PPI stable fish oil emulsions showed a bell shape change, which is a typical protein stable lipid droplet morphology. At pH 7.0 or 3.0, fish oil emulsions with PPI stability have a higher net charge (>20mV), so there is a strong electrostatic repulsion between them, which prevents polymerization. When pH value is 4.0~6.0, the particles have little or no net charge, resulting in extensive aggregation of particles (>10um). In contrast, the fish FO-PPI-
SBP complex dispersions have the smallest particle size at pH 7.0 and 6.5, suggesting that the interaction between PPI and SBP is weak or non-existent. The particle size increases significantly with the decrease of pH. The appearance of larger particles may be due to the enhanced protonation of the amino side group of PPI, which triggers the electrical attraction with the negatively charged carboxyl group of SBP value. In the medium pH range, the particle size of the fish FO-PPI-SBP complex dispersion is even smaller than that of the emulsion. This may be caused by electrostatic repulsion being insufficient to counteract attractive interactions (such as van der Waals forces or hydrophobic interactions). 2. The effect of pH value on the phase behavior and microstructure of fish oil dispersion
In order to better visualize the effect of pH on the appearance of fish oil in two different feed dispersions, we constructed a state diagram (Figure 2a) to show that the phase behavior of the PPI stable fish oil emulsion and the FO-PPI-SBP complex dispersions after 24h at 25°C is a function of pH (7.0-3.0). PPI stabilizes the phase behavior of fish oil emulsions very classically (Figure 2a), and single-phase solutions are observed at pH(7.0,6.5,2.0). But as pH decreases, it changes to a precipitation and cloudy form (A), and atpH 5.0 to a condensed sediment (m). For the fish FO-PPI-SBP complex dispersion system, the state diagram shows three distinguishable phase behaviors. At neutral to acidic pH values (7.0,6.5,6.0), a homogeneity (0) was observed in the mixture as a result of the same charge repulsion of PPI and SBP (Figure 2b). When the pH is reduced to acidic conditions (5.5-2.0), two insoluble complexes (condensation or precipitation) with different phase behavior appear, with different structural properties. Since the pH (5.5-4.0) is close to the
PPI IEP, condensation shows a precipitation and cloudy appearance (4). This phase behavior is due to the mutual attraction between the negative charge of the polyanion SBP and the opposite stain on the PPI surface. However, at higher pH values (5.5, 5.0, 4.5), the repulsive force within the system is strong, preventing violent phase separation, while at pH 4.0, significant phase separation occurs. At pH 3.5 and 3.0, the phase behavior of precipitated and transparent solutions (=) is formed.
CLSM (confocal laser scanning microscope) was then applied to evaluate the effect of pH on the in-situ morphological properties of PPI stabilized fish oil emulsion and fish FO-
PPI-SBP composite dispersions (Figure 3). The PPI is labeled by the FITC and appears as green dots in the CLSM micrograph (Figure 3a), while the fish oil is stained with Nile red.
Compared with CLSM micrographs of PPI and SBP solutions (Figure 3 a and b}, no signs of flocculation of emulsified droplets were observed at pH 7.0 (Figure 3c), which may be attributed to the high Z potential of the droplets. When the emulsion was acidified to a pH of 3.5, locally clustered large particle sizes appeared (white arrow in Figure 3d), which was consistent with particle size measurements. The increased droplet flocculation is due to the added acid lowering the pH from 7.0 to 3.5. This allows the pH value to be absorbed through the PPIl's IEP, thus bringing the droplets close to each other. For the fish FO-PPI-SBP composite dispersion (Figure 3e), the microstructure is similar to that of the emulsified droplets at pH 7.0. When the pH of the mixture was reduced from 7.0 to 4.5 or 4.0 (close to the PPI IEP), only a small amount of flocculant mixed with green particles (Figure 3f and 39) was observed, and the microstructure was similar to that of emulsion with a pH of 3.5. The observed size of the condensate is also consistent with the results in Figure 1b. Under this pH composite condensed the number and size of low may be due to dispersion of relatively strong electrostatic repulsion ([Z/>20). As a rule, a slight decrease in pH from 4.0 to 3.5 significantly promotes the formation of complex, irregularly shaped condensates (Figure 3h).
This trend reflects the progressive charge neutralization of the system, in which biopolymer interactions reach electrical equivalent points while allowing attractive forces such as van der Waals forces and hydrophobic forces to dominate the interactions.
According to scanning electron microscopy (SEM), at different pH values, the microstructure of the freeze-dried fish oil emulsion and FO-PPI-SBP composite condensates is different without polishing (Figure 4a), and their shapes are flacy-like, with smooth surfaces and no fragments, which may be caused by the aggregation of emulsion droplets during drying. Similar morphology was observed in the FO-PPi-SBP complex condensates formed at pH 4.5, except that the microstructure became less condensed as it extended to one dimension (Figure 4b). Again, this indicates that no composite condensates will form due to the strong repulsion between biopolymers. Notably, the spongy porous structure appears as pH decreases. A multi-dimensional network with multiple patterned apertures is formed when the pH of the condensate is 4.0 (Figure 4c). Further lowering the pH value to 3.5 causes the network to become more concentrated (Figure 4d). This morphological change in lyophilized composite condensates confirms that the strength of electrostatic interactions varies at different pH values, which may significantly affect biopolymer interactions. Combined with the results of the state diagram, CLSM and SEM, it can be confirmed that the FO-PPI-SBP condensate exhibits a relatively dense network structure at pH 3.5, which is mainly due to charge neutralization. 3. Microcapsule analysis of fish oil 3.1 Encapsulation efficiency
Table 1 shows the powder yield (PY), encapsulation efficiency (EE), encapsulation yield (EY) and payload (PL) of spray-dried microcapsule powders prepared by emulsification and composite condensation. Powder yield is the key parameter to determine the recovery rate of solid substance after spray drying. All microencapsulated powders had very similar
PY values, except that the composite condensates formed at pH 3.5 produced powders with the lowest PY values (42.0%). Of the two different dispersion preparation methods, the microcapsule powder prepared by PPI stabilized emulsion had the lowest EE (p< 0.05), indicating improved EE of the latter method and higher packaging efficiency in the pH range of 3.5-4.5. The EE of the three fish oil microcapsules prepared by composite condensation is the same, which is independent of the pH value at the time of formation. Two factors can lead to low EE values. In this study, fewer wall materials were used, which had a direct impact on EE values. In addition, a more rigorous and powerful solvent washing regimen was used to try to completely remove the surface oil, rather than determine the content of the easily extracted ail in it. Compared with the control study without SBP, the encapsulation efficiency (EE), encapsulation rate (EY) and payload (PL) of fish oil microcapsules with SBP can achieve similar or better effects under wider pH conditions. Fish oil microcapsule powder dried by PPI stabilization emulsion and fish FO-PPI -- SBP composite condensate spray showed similar PY, EY, and PL.
Table 1
Powder yield (PY), package efficiency (EE), package yield (EY}, and payload (PL) * of PPI stabilized emulsion or PPI-SBP Composite condensate spray dried FO microcapsules. * Values in a column with different superscript letters indicate that in p< 0.05, there was a statistically significant difference (FO: fish oil; PPI: pea protein isolate; SBP: sugar beet pectin)
The major chemical functional groups of SBP are identified in spectra with wave number range 1000-2000cm™. It includes 1734cm (C=O stretching vibration), 1622cm™’ (tensile carboxylate ions) and 1441cm™ (asymmetric stretch-CH3). In the position of 3012cm™, we can observe fish oils olefin double bond (-HC=CH-) absorption peak.
As shown in Figure 5, in the spectra of fish oil microcapsules prepared with PPI stabilization emulsion at pH 3.5, the intensity of absorption peaks at 3012, 2926, 2852 and 1146cm™ gradually increased, indicating the presence of fish oil. In addition, when the fish oil was encased, PPI initial peak of 1633, 1529, 1450cm™, the blue shift magnitude 8, 4, and 4 cm, respectively or so. These results suggest that the hydrophobic regions of fish oil and
PPI may interact with each other during spray drying. A similar FTIR spectrum was found in spray-dried microcapsules, where low water soluble chlorophyll was able to bind to tryptophan or tyrosine residues of whey protein, causing blue shift. Although the spectra of fish oil microcapsules formed by composite condensation are very similar to those of fish ail microcapsules formed by emulsification, some significant differences have been found. The spectra of fish oil microcapsules formed by composite condensation showed a new peak at 1016cmrt, indicating that SBP had been successfully introduced into the composite condensate. In addition, the peak value of 1392cm™ in PPI and emulsified fish oil micro- capsules was not found in all complex condensed microcapsules. Because this peak was assigned to -COO- of the amino acid, its disappearance confirmed that SPB and PPI formed complex condensates through electrostatic interaction. In addition, the spectra of the fish oil microcapsules based on the composite agglomerations show a wide band (about 1020-1080cm™), which may be attributed to the superposition of the spectra of PPI (peak 1063 cm} and SBP (peak 1012cm), mainly due to their electrostatic interaction during the formation of the composite agglomerations. 3.3. Thermal analysis
The thermal properties of PPI in different fish oil microcapsules were studied by DSC in this application (Figure 6).
The DSC maps of both PPI and SBP showed endothermic peaks corresponding to the melting of the network structure of the two biopolymers. PPI raw material melting point of about 86.66°C. The melting point of PPI may be that water evaporation from SBP leads to the destruction and breaking of non-covalent bonds and hydrogen interactions between polar and non-polar groups, thus destroying the secondary and tertiary structure of PPI.
When PPI was used as emulsifier to cover the surface of FO droplets, the melting point of microcapsules decreased to 76.83°C, indicating that the synergic structure of PPI was poor after spray drying. This is reasonable because the hydrophobic interaction between FO and the high-pressure homotropic PPI is weaker than the interaction between the hydrophobic amino acid patch in the raw PPI. On the contrary, the FO microcapsules prepared by the
FO-PPI-SBP composite coacervation system showed a small and narrow melting peak, which was attributed to the formation of a strong new network structure. This structure inhibits denaturation of the PPI and therefore maintains a melting point similar to that of the original PPI. A similar phenomenon is consistently observed in microcapsules made from complex condensates, such as soy protein isolate and chitosan, as this structure generally increases the protein's stability against thermal denaturation. The pH value affects the thermal performance of microcapsules, with larger and wider endothermic peaks forming complexes at higher pH (4.5) than those formed at pH 4.0 and 3.5. This may also be caused by the strong electrostatic interaction between PPI and SBP, as evidenced by their zeta - potentials (Figure 1a). 3.4 Morphology of fish oil microcapsules
Scanning electron microscopy (SEM) can be used to analyze the morphologies of fish oil microcapsules prepared by different feeding dispersants (Figure 7). The microstructure of SBP(Figure 7a) and PPI(Figure 7b) showed irregular and plate morphology, which were difficult to identify, respectively. All of the fish oil microcapsules have some similarities in their morphology, for example, they all have no cracks or holes in their surface, which ensures the capsule's low permeability and provides protection against the fish oil. However, different feed dispersions have different effects on its morphology. For fish oil microcapsules prepared from a PPI stabilized emulsion with a pH of 3.5, the particles were observed to be spherical with a certain roughness (Figure 7c). The size of microcapsules varied greatly from 0.5um to 7.5um. Notably, some oil spots can also be seen on the surface of the microcapsule (red arrow in Figure 7c). The size of fish oil microcapsules obtained from composite agglomerates is generally larger than that obtained from emulsification, because pectin is produced during agglomerate formation. Compared with emulsified microcapsules, there was almost no oil spot, which indicated that the encapsulation effect of composite coagulant had been improved. The pH value affects the size of fish oil microcapsules prepared from complex condensates. Especially when the pH value is 4.5, the size of the capsule changes dramatically (Figure 7d); The maximum particle size appeared at pH 3.5 (Figure 7f). The uniform size of the microcapsules (Figure 7e) was produced at an intermediate pH value (4.0). This observation is consistent with the results in Figure 4, further demonstrating that the composite condensate formed at pH3.5 is the optimal condition for coating fish oil before spray drying.
In this application, FO-PPI-SBP composite condensate is used as the feed dispersion of fish oil microcapsules, which greatly improves the powder yield, payload and encapsulation rate of fish oil microcapsules. Due to the interaction between PPI and SBP,
the denaturation temperature and network thermal stability of the prepared fish oil microcapsules were improved. Since the droplet size, { potential, phase behavior and microstructure of the feed dispersion are all affected by pH, this application is designed to generate fish oil microcapsules with larger particle size and denser network structure by adjusting the FO-PPI-SBP composite condensate at appropriate pH value. The FO-PPI-SBP composite condensates formed at pH3.5 have larger particle size and denser network structure than those formed at higher pH4.5 and pH4.0.
Finally, it shall be noted that the above implementation methods are used only to illustrate the technical scheme of the invention and not to limit the technical scheme.
Notwithstanding the detailed description of the invention by the applicant with reference to the better implementation methods, ordinary technicians in the field shall understand that those technical schemes of the invention modified or substituted without deviating from the purpose and scope of the technical scheme. Shall be covered by the claims of the invention.
Claims (8)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202210625215.7A CN119235013A (en) | 2022-06-02 | 2022-06-02 | Fish oil microcapsules based on pea protein isolate emulsification and coagulation and preparation method thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| NL2034548A true NL2034548A (en) | 2023-04-26 |
| NL2034548B1 NL2034548B1 (en) | 2023-10-10 |
Family
ID=86184033
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| NL2034548A NL2034548B1 (en) | 2022-06-02 | 2023-04-12 | A Preparation Method for Embedding n-3 Long Chain Polyunsaturated Fatty Acid Microcapsules |
Country Status (2)
| Country | Link |
|---|---|
| CN (1) | CN119235013A (en) |
| NL (1) | NL2034548B1 (en) |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2016193373A1 (en) * | 2015-06-03 | 2016-12-08 | Anabio Technologies Limited | Microencapsulates containing stabilised lipid, and methods for the production thereof |
-
2022
- 2022-06-02 CN CN202210625215.7A patent/CN119235013A/en active Pending
-
2023
- 2023-04-12 NL NL2034548A patent/NL2034548B1/en active
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2016193373A1 (en) * | 2015-06-03 | 2016-12-08 | Anabio Technologies Limited | Microencapsulates containing stabilised lipid, and methods for the production thereof |
Non-Patent Citations (3)
| Title |
|---|
| LAN YANG ET AL: "Microencapsulation of hemp seed oil by pea protein isolate-sugar beet pectin complex coacervation: Influence of coacervation pH and wall/core ratio", FOOD HYDROCOLLOIDS, ELSEVIER BV, NL, vol. 113, 19 October 2020 (2020-10-19), XP086454888, ISSN: 0268-005X, [retrieved on 20201019], DOI: 10.1016/J.FOODHYD.2020.106423 * |
| LAN YANG ET AL: "Phase behavior and complex coacervation of concentrated pea protein isolate-beet pectin solution", FOOD CHEMISTRY, ELSEVIER LTD, NL, vol. 307, 30 September 2019 (2019-09-30), XP085893201, ISSN: 0308-8146, [retrieved on 20190930], DOI: 10.1016/J.FOODCHEM.2019.125536 * |
| LEÏLA ABERKANE ET AL: "Encapsulation and Oxidative Stability of PUFA-Rich Oil Microencapsulated by Spray Drying Using Pea Protein and Pectin", FOOD AND BIOPROCESS TECHNOLOGY ; AN INTERNATIONAL JOURNAL, vol. 7, no. 5, 1 May 2014 (2014-05-01), New York, pages 1505 - 1517, XP055315957, ISSN: 1935-5130, DOI: 10.1007/s11947-013-1202-9 * |
Also Published As
| Publication number | Publication date |
|---|---|
| CN119235013A (en) | 2025-01-03 |
| NL2034548B1 (en) | 2023-10-10 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Zhang et al. | Improving the emulsifying property of gliadin nanoparticles as stabilizer of Pickering emulsions: Modification with sodium carboxymethyl cellulose | |
| Ding et al. | Fabrication and characterization of soybean oil bodies encapsulated in maltodextrin and chitosan-EGCG conjugates: An in vitro digestibility study | |
| Zhong et al. | Fabrication and characterization of oil-in-water emulsions stabilized by macadamia protein isolate/chitosan hydrochloride composite polymers | |
| Ghasemi et al. | Production of pectin-whey protein nano-complexes as carriers of orange peel oil | |
| Ren et al. | Novel food-grade Pickering emulsions stabilized by tea water-insoluble protein nanoparticles from tea residues | |
| Plati et al. | Complex coacervate formation between hemp protein isolate and gum Arabic: Formulation and characterization | |
| Guo et al. | Preparation, characterization and stability of pea protein isolate and propylene glycol alginate soluble complexes | |
| Sun et al. | Properties of binary complexes of whey protein fibril and gum arabic and their functions of stabilizing emulsions and simulating mayonnaise | |
| Lan et al. | Complexation between soy peptides and epigallocatechin-3-gallate (EGCG): Formation mechanism and morphological characterization | |
| Dong et al. | Development and characterization of nanoparticles formed by soy peptide aggregate and epigallocatechin-3-gallate as an emulsion stabilizer | |
| Huang et al. | Grape seed proanthocyanidin-loaded gel-like W/O/W emulsion stabilized by genipin-crosslinked alkaline soluble polysaccharides-whey protein isolate conjugates: Fabrication, stability, and in vitro digestion | |
| Li et al. | Synergistic and competitive effects of monoglycerides on the encapsulation and interfacial shear rheological behavior of soy proteins | |
| CN112868817B (en) | A protein-key Antarctic krill oil edible product | |
| de Araujo Padilha et al. | Fabrication of hollow polymer microcapsules and removal of emulsified oil from aqueous environment using soda lignin nanoparticles | |
| Wang et al. | Structural and physical properties of spray-dried fish oil microcapsules via pea protein isolate based emulsification or complex coacervation with sugar beet pectin | |
| Meng et al. | Structure, stability, rheology, and texture properties of ε-polylysine-whey protein complexes | |
| Qi et al. | The viability of complex coacervate encapsulated probiotics during simulated sequential gastrointestinal digestion affected by wall materials and drying methods | |
| Premjit et al. | Synthesis, characterization, and in vitro digestion of electrosprayed and freeze-dried probiotics encapsulated in soy protein isolate-sunflower oil emulsions | |
| Zhao et al. | A novel preparation strategy of emulsion gel solely stabilized by alkaline assisted steam-cooking treated insoluble soybean fiber | |
| Du et al. | Agar-gelatin Maillard conjugates used for Pickering emulsion stabilization | |
| Bahraseman et al. | Segregative phase separation of gelatin and tragacanth gum solution and Mickering stabilization of their water-in-water emulsion with microgel particles prepared by complex coacervation | |
| CN103648295A (en) | Food-grade encapsulate and process for the production thereof | |
| Cao et al. | Physical properties and stability of filled hydrogel particles based on biopolymer phase separation: Influence of the ratio of protein to polysaccharide | |
| US20070104866A1 (en) | Encapsulated emulsions and methods of preparation | |
| Li et al. | Improving emulsifying properties of carboxylated microcrystalline cellulose by calcium bridging to hydrophobic peptides |