Microencapsulated omega-3 oil powder for animal feed

Abstract

Disclosed are a microcapsule fat powder of Ω3-enriched meat, egg and milk and its preparation method, and the powder includes a water-soluble wall material and an Ω3 oil core material embedded in the wall material. The water-soluble wall material is prepared by mixing dextrin, water-soluble syrup, whey powder or chitosan with starch paste, and the Ω3 oil core material is prepared by mixing linseed oil, deep sea fish oil or algae oil with a composite emulsifier which is stearic acyl lactylate. The microcapsule fat powder can be combined with intestinal and pancreatic lipases very easily to improve the digestion, absorption and utilization of Ω3 oils.

Claims

1. A method for preparing a microencapsulated omega-3 (Ω3) polyunsaturated fatty acid (PUFA) powder for Ω3-enriching animal feeds for meat, egg, and milk production, comprising the steps of: (a) heating to 30-35° C. a starch paste that has been formed by mixing starch and water with continuous stirring and adding sodium hydroxide until the starch paste has a pH value of 8.5-9; (b) following step (a) with continuous stirring gradually over 1-2 hours adding to the starch paste a composition comprising sodium octenylsuccinate diluted in ethanol while maintaining a pH value of 8.2-8.8 by adding sodium hydroxide until addition of sodium octenylsuccinate is complete and the pH value is stabilized at 8.5; (c) following step (b) with continuous stirring adding dilute nitric acid to the starch paste until the pH value is 6.5 and then heating the starch paste to 90° C. to obtain a neutralized starch paste; (d) combining, while stirring and heating to a temperature of 70-80° C. in an aqueous phase tank, water, disodium hydrogen phosphate, sodium citrate, and at least one material selected from the group consisting of dextran, water-soluble syrup, whey powder and chitosan, and then adding to the aqueous phase tank the neutralized starch paste of step (c) until the starch paste is dissolved, to obtain an aqueous solution; (e) combining, while stirring and heating to a temperature of 70-80° C. in an oil phase tank, an Ω3 oil, stearic acyl lactylate and a composite emulsifier, to obtain an oil phase solution that is maintained at 70-80° C. and in which the stearic acyl lactylate and the composite emulsifier are dissolved; (f) mixing the aqueous solution of (d) with the oil phase solution of (e) to form a feed solution; (g) homogenizing the feed solution by a high pressure controlled at 20˜45 MPa after milling the feed solution with a colloid mill or shearing the feed solution with a shear pump and pressuring to 2˜12 MPa, to obtain a homogenized feed solution; and (h) pressure spray drying the homogenized feed solution by controlling an inlet air temperature of a drying tower at 135˜190° C. and an outlet air temperature of the drying tower at 55˜95° C., thereby to obtain the microencapsulated omega-3 (Ω3) polyunsaturated fatty acid (PUFA) powder.

2. The method of claim 1, wherein the Ω3 oil is at least one oil selected from the group consisting of linseed oil, deep sea fish oil, and algae oil.

Description

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

(1) The technical content of the present invention will become apparent with the detailed description of preferred embodiments and the illustration of related drawings as follows.

(2) The present invention relates to a microcapsule fat powder of Ω3-enriched meat, egg and milk, and the microcapsule fat powder includes a plurality of microcapsule granules, each having a water-soluble wall material and an Ω3 oil core material embedded in the wall material.

(3) The water-soluble wall material is prepared by mixing at least one material selected from the group consisting of dextrin, water-soluble syrup, whey powder and chitosan with starch paste, and the Ω3 oil core material is prepared by mixing at least one oil selected from the group consisting of linseed oil, algae oil and deep sea fish oil with a composite emulsifier and stearic acyl lactylate.

(4) The mass ratio of the linseed oil or the algae oil to the deep sea fish oil is 0%˜100%:100%˜0%.

(5) The present invention further relates to a preparation method of the aforementioned microcapsule fat powder of Ω3-enriched meat, egg and milk, and the method comprises the following steps:

(6) Step 10: Mix starch with water to form a starch paste. Stir and heat the starch paste to 30˜35° C. Add sodium hydroxide into the starch paste until the pH value is 8.5˜9. Continue the stirring and activation. Gradually add starch sodium octenylsuccinate diluted by ethanol within 1˜2 hours while maintaining and controlling the pH value of the reaction system within a range of 8.2˜8.8 during the adding process. Continue the stirring and reaction after the addition of starch sodium octenylsuccinate is completed until the pH value is stabilized at 8.5. Add dilute nitric acid to neutralize the reaction system to a pH of 6.5, and heating up to 90° C. to form the starch paste.

(7) Step 20: Put an Ω3 oil into an oil phase tank. Heat it up to 70˜80° C. Put in a composite emulsifier and stearic acyl lactylate while stirring. Maintain the temperature within a range of 70-80° C. and stir until the composite emulsifier and stearic acyl lactylate are dissolved to form an oil phase solution

(8) Step 30: Put water into an aqueous phase tank. Put in at least one material selected from the group consisting of dextrin, water-soluble syrup, whey powder and chitosan, and disodium hydrogen phosphate, and sodium citrate while stirring. Heat the materials to a temperature of 70˜80° C. Add the starch paste prepared in Step 10. Maintain the temperature within a range of 70˜80° C. Stir until the starch paste is dissolved to form an aqueous solution.

(9) Step 40: Mix the aqueous solution with the oil phase solution to form a feed solution. Homogenize the feed solution by a high pressure controlled at 20˜45 MPa after milling the feed solution by a colloid mill or shearing the feed solution by a shear pump, pressuring to 2˜12 MPa. Control an inlet air temperature of a drying tower at 135˜190° C. and an outlet air temperature at 55˜95° C. to perform a pressure-spray drying process of the feed solution to obtain the microcapsule fat powder of Ω3-enriched meat, egg and milk.

(10) The present invention is illustrated by the following preferred embodiments:

Preferred Embodiment 1

(11) An Ω3 enriched microcapsule fat powder is prepared by the method as described below:

(12) Step 10: Add 20 kg of corn starch into 30 kg of drinking water to form a starch paste. Stir and heat the corn starch paste to 30-35° C. Add sodium hydroxide solution (4%) until the pH value is 8.5˜9. Continue the stirring and activation for half an hour. Gradually add 0.6 kg of sodium octenylsuccinate anhydride (diluted by 2.4 kg of absolute ethanol or 95% ethanol) within 1˜2 hours. As the pH value drops, add sodium hydroxide solution (4%) and maintain the reaction system at pH=8.2˜8.8. Continue the stirring and reaction until the pH value is stabilized at 8.5 after sodium octenylsuccinate anhydride has been added. Add dilute hydrochloric acid (3%) to neutralize the reaction system to pH=6.5. Heat up the reaction system to 90° C. to form the starch paste.

(13) Step 20: Put 500 kg of the Ω3 oil into an oil phase tank. Heat it up to 70˜80° C. Put in 13 kg of a composite emulsifier and 5.5 kg of stearic acyl lactylate while stirring. Maintain the temperature within a range of 70-80° C. and stir until the composite emulsifier and stearic acyl lactylate are dissolved to form an oil phase solution.

(14) Step 30: Put 950 kg of water into an aqueous phase tank. Put in 470 kg of at least one material selected from the group consisting of dextrin, water-soluble syrup, whey powder and chitosan, and 6 kg of disodium hydrogen phosphate, and 6 kg of sodium citrate while stirring. Heat to a temperature of 70˜80° C. Add the starch paste prepared in Step 10. Maintain the temperature within a range of 70˜80° C. Stir until the starch paste is dissolved to form an aqueous solution.

(15) Step 40: Mix the aqueous solution with the oil phase solution to form a feed solution, and stir the solution for 20 minutes. Homogenize the feed solution by a high pressure controlled at 20˜45 MPa after milling the feed solution by a colloid mill or shearing the feed solution by a shear pump, pressuring to 2˜12 MPa. Control an inlet air temperature of a drying tower at 135˜190° C. and an outlet air temperature at 55˜95° C. to perform a pressure-spray drying process of the feed solution to obtain the microcapsule fat powder of Ω3-enriched meat, egg and milk.

Preferred Embodiment 2

(16) The feed of the Ω3 enriched microcapsule fat powder of the present invention enhances the egg yolk DHA.

(17) Group Division of Experiment: A: Control Group (BD: Feeds for laying hens supplied by Longyan Company, Hualong Group, Fujian) B: Experimental Group I (BD+0.5% Fat Hormone) C: Experimental Group II (BD+1% Fat Hormone)

(18) Each group includes five Hy-line laying hens of 70 weeks age and fed continuously for two weeks, and the results are listed in Table 1:

(19) TABLE-US-00001 TABLE 1 A B C Average Egg Weight (g) in 66.8 65.3 72.7 Full Course 100 g Yolk C22:6n3 Content (g) 0.177 0.234 0.282 Increase Percentage (%) — 32.2 59.3

(20) The results show that: (1) An addition of 1% of the enriched Ω3 microcapsule fat powder in the daily feeds increases the egg weight by 8.8%. (2) An addition of 0.5% and 1.0% of the enriched Ω3 microcapsule fat powder in the daily feeds increases the yolk DHA (or C22:6n3) by 32.2% and 59.3% respectively.

Preferred Embodiment 3

(21) The feed by enriched Ω3 microcapsule fat powder of the present invention enriches the DHA better than the feed by enriched liquid oil.

(22) Group Division of Experiment: A: Control Group (BD: Feeds for laying hens supplied by Longyan Company, Hualong Group, Fujian+1.0% Corn Syrup) B: Experimental Group I (BD+0.5% Liquid Mixed Oil+0.5% Corn Syrup) C: Experimental Group II (BD+1% Fat Hormone)

(23) Each group includes five Hy-line laying hens of 80 weeks age and fed continuously for two weeks, and the results are listed in Table 2:

(24) TABLE-US-00002 TABLE 2 A B C Average Egg Weight (g) in 68.6 72.5 72.9 Full Course 100 g Yolk C22:6n3 Content (g) 0.170 0.220 0.292 Increase Percentage (%, for A) — 29.4 71.8 Increase Percentage (%, for B) — — 32.7 100 g of Chicken Breast 0.065 0.090 0.121 C22:6n3 Content (g) Increase Percentage (%, for A) — 38.5 86.2 Increase Percentage (%, for B) — — 34.4

(25) The results show that: (1) An addition of 1% of the enriched Ω3 microcapsule fat powder in the daily feeds increases the egg weight by 6.3%. (2) An addition of 1% of the enriched Ω3 microcapsule fat powder in the daily feeds increases the yolk and chicken breast Ω3 by 32.7% and 34.4% than the liquid mixed oil respectively.

(26) In summation of the description above, the products of the present invention has better Ω3 absorption and conversion rates than other products available in the market, and the aforementioned C22:6n3 is docosahexaenoic acid.

Preferred Embodiment 4

(27) The feed of the Ω3 enriched microcapsule fat powder of the present invention enhances the ALA content and the intramuscular fat content in Huai pork.

(28) Group Division of Experiment: A: Control Group (BD: Feeds for Huai Pig Farm, Gu Tian, Shanghang County, Longyan City, Fujian) B: Experimental Group (BD+1% Fat Hormone)

(29) Each group includes 15 Huai pigs with a weight of 120˜190 catties and fed continuously for one month, and the results are listed in Table 2:

(30) TABLE-US-00003 TABLE 3 A B ALA Content of 100 g in Huai 0.2571 0.5625 Pork (g) Increase Percentage (%) — 118.8 Fat Content in 100 g of Huai 3.911  4.205 Pork (g) Increase Percentage (%) — 7.52

(31) The results show that: (1) An addition of 2% of the enriched Ω3 microcapsule fat powder in the daily feeds increases the ALA content by 118.8%. (2) An addition of 2% of the enriched Ω3 microcapsule fat powder in the daily feeds increases the fat content in Huai pork by 7.52%.

(32) When the products of the present invention is under a uniform pressure of 20˜45 Mpa, a main structure with a plurality of triglycerides bounded by the bonding forces of molecular bonds is decomposed into a single triglyceride, and the particle size of the oil drops from 20 microns to 2 microns. In the condition of the same particle size, the quantity of emulsified homogeneous single triglycerides is 100,000 times of the quantity of the unprocessed triglycerides. In other words, when the microcapsule wall material is dissolved in the aqueous intestinal environment, single glycerides are formed from disintegration and combined with intestinal lipases and absorbed and used with a chance of 100,000 times more. Animal digestion experiments show that the homogenous emulsified oil has digestion and utilization rates better than those of the unprocessed oil by 15%. The younger the animal, the more significant the difference. If a piglet of 7 weeks age has digestion rates for short and long chained oils equal to 92% and 78% respectively, a piglet of 3 weeks age will have digestion rates for short and long chained oils equal to 90% and 37% respectively.

(33) The present invention has the following advantages: 1. Good water solubility: The wall material of the products of the present invention is water soluble, and the emulsified oil core material is suspendable in an aqueous environment. When entering into an aqueous intestinal environment of animals, the products of the present invention are combined with intestinal and pancreatic lipases easily to improve the digestion, absorption and utilization of the Ω3 oils. 2. Anti-oxidation: Materials such as fish oils with high unsaturation and price may be oxidized and spoiled easily, particularly in summer time, and such materials are difficult to produce, store and use. On the other hand, the products of the present invention overcomes the aforementioned problem by special formulation and technology, wherein the Ω3 oil is used as a core material, and water-soluble syrup, whey powder, or chitosan is used as a wall material, and the coated water-soluble wall material isolates the core material from the contact of oxygen, so that the Ω3 fatty acids will not be spoiled or oxidized easily, and its potency is protected to extend the shelf life of oil products and final products significantly and reduce the burden of requiring the very strict conditions for the production, storage and usage of these materials and products, so as to achieve the effect of lowering the Ω3 content of the feed products due to the oxidation and spoilage of oils. 3. Good spreadability: The products of the present invention can be manufactured into microcapsule granule groups of 80-120 meshes which are substantially equal to the particle size of most feed materials, so as to improve the mixing uniformity of the feeds and avoid negative benefits such as agglomeration, non-uniformity, and fermentation and spoilage of residues caused by adding the oil directly. In the meantime, the present invention improves the inconvenience caused by adding oil by feed factories or cultivators, so that users may directly, precisely and conveniently add feeds packaged in a bag into feeds.

(34) While the invention is described in some detail hereinbelow with reference to certain illustrated embodiments, it is to be understood that there is no intent to limit it to those embodiments. On the contrary, the aim is to cover all modifications, alternatives and equivalents falling within the spirit and scope of the invention as defined by the appended claims.