CN101744111A - Preparation method of microencapsulated coating amino acid - Google Patents

Preparation method of microencapsulated coating amino acid Download PDF

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Publication number
CN101744111A
CN101744111A CN200810162307A CN200810162307A CN101744111A CN 101744111 A CN101744111 A CN 101744111A CN 200810162307 A CN200810162307 A CN 200810162307A CN 200810162307 A CN200810162307 A CN 200810162307A CN 101744111 A CN101744111 A CN 101744111A
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CN
China
Prior art keywords
amino acid
preparation
coating
powder
microencapsulated
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Pending
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CN200810162307A
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Chinese (zh)
Inventor
李浙烽
占秀安
陈强
余荣
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Individual
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Individual
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Priority to CN200810162307A priority Critical patent/CN101744111A/en
Publication of CN101744111A publication Critical patent/CN101744111A/en
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Abstract

The invention relates to a preparation method of aquatic feed micro encapsulated coating amino acid. The components of the micro encapsulated coating amino acid are: 30-60 percent of glyceride, 30-60 percent of amino acid powder and 5-15 percent of stearic acid. In the method, main amino acids necessary for animals are processed by micro encapsulated coating, and therefore, the coated crystalline amino acid is kept in the coating material and do not dissolve out and lose due to the environment; and the amino acid in coating microencapsulation can be slowly released in the intestinal tracts of animals, thereby realizing the synchronous absorption of the coated amino acid and the bonded amino acid, improving the bioavailability of the crystalline amino acid by aquatic animals, lowering the feed rate and cost, and reducing the environmental pollution.

Description

A kind of preparation method of microencapsulated coating amino acid
Technical field
The present invention relates to a kind of novel aquatic feeds microencapsulation bag by amino acid whose manufacture method.
Background technology
Amino acid is the necessary nutritional labeling of aquatic animal to grow, and amino acid content in the raw material of aquatic product feed stuff and kind all can not satisfy the needs of aquaculture, therefore, in present aquatic feeds, generally add multiple free amino acid, but the free amino acid that adds absorbs with the amino acid that decomposes generation through feed protein asynchronous.The amino acid whose absorption of the absorption of free amino acid prior in native protein, decomposing, also influence the synchronization that other amino acid absorbs simultaneously, make amino acid whose absorbing not reach the balance complementation, cause aquatic livestock to free amino acid utilize variation so that the utilization of the whole feed protein of influence, the growth of aquatic livestock etc. is not had substantial help; In addition, the fishes and shrimps process of searching for food is slow, and the free amino acid in the feed is soluble in water, can dissolve to ooze out from feed in water, reduces amino acid whose effective rate of utilization.Studies show that at present the method that protection amino acid commonly used absorbs mainly contains the microencapsulation processing and free amino acid and carrier protein are formed compound, and latter's course of reaction complexity, cost is higher, is unsuitable for applying.For this reason, it is low to the invention provides a kind of cost, easy to prepare, homogeneous grain diameter, and feed coefficient is low, and the proteinosis rate is low, can polluted-water, a kind of aquatic feeds microencapsulation bag that is beneficial to the fishes and shrimps growth is by the preparation method of amino acid preparation.
Summary of the invention
The object of the present invention is achieved like this: a kind of production method of aquatic product feed crystal amino acid slow-releasing preparation is characterized in that it forms (by mass percentage calculate) by following material:
Glyceride 30-60%
Powder of amino acids 30-50%
Stearic acid 5-15%
Embodiments of the present invention are as follows: a kind of microencapsulation bag is by amino acid whose preparation method, it is characterized in that earlier powder of amino acids with 30-60% joins in the glyceride of heat fused (30-60%), under the 30-90rpm rotating speed, stir 20-50min, high speed dispersion, rotational speed regulation is at 1000-2000rpm, time 1-3min, carry out spray-drying after high speed dispersion is even, EAT is a normal temperature, leaving air temp normal temperature, feed rate 1-3L/min, the spray-drying thing carries out granulating and coating under 50-80 ℃, coating solution is the stearic acid ethanolic solution of 1-3%, and the time is 2-4h.
Main feature of the present invention is: it is processed that animal mainly must acidic amino acid be carried out the microencapsulation bag, make bag by after crystal amino acid be in the packaging material, because of water environment stripping loss; Granularity is suitable simultaneously, help wrapping by the amino acid in the micro-capsule and in animal intestinal, slowly discharge, can realize the bag by amino acid (methionine, lysine etc.) with combine the amino acid whose synchronous absorption of attitude, improve the bioavailability of aquatic animal to crystal amino acid, thereby improve the utilization rate of feed protein, reduce dietary protein level, save the fish meal addition, reduce fodder and bait coefficient and cost, and reduce environmental pollution or the like.
Description of drawings
Fig. 1 is processing process figure of the present invention
Fig. 2 is the equipment schematic diagram that the present invention uses
The specific embodiment
Embodiment 1
Take by weighing 1000g glyceride, after being heated to 80 ℃ of whole fusings, join the powder of amino acids (90% cross 150 mesh sieves) of 800g through ultramicro grinding, continue to stir 25min, rotating speed 60rpm, high speed dispersion then, rotational speed regulation is at 1500rpm, and time 2min tells the cooling of spraying after being uniformly dispersed, air intake and leaving air temp are normal temperature, feed rate 2L/min, spraying cooling thing carries out dressing under 50-80 ℃, and the time is 2-4h, coating solution is 2% stearic acid (taking by weighing the 200g stearic acid is dissolved in the 10000ml ethanol), and product granularity 80% is by 60 mesh sieves.
Embodiment 2
Take by weighing 800g glyceride, after being heated to 80 ℃ of whole fusings, add the powder of amino acids (90% cross 150 mesh sieves) of 1000g through ultramicro grinding, continue to stir 20min, rotating speed 90rpm, high speed dispersion then, rotational speed regulation is at 15000rpm, time 2min, the high speed dispersion cooling of spraying after evenly, air intake and leaving air temp are normal temperature, feed rate 2L/min, spraying cooling thing carries out dressing under 50-80 ℃, and the time is 2-4h, coating solution is 2% stearic acid (taking by weighing the 200g stearic acid is dissolved in the 10000ml acetone), and product granularity 80% is by 60 mesh sieves.

Claims (6)

1. the preparation method of a microencapsulated coating amino acid is characterized in that it forms (counting by weight percentage) by following material:
Glyceride 30-60%
Powder of amino acids 30-60%
Stearic acid 5-15%
2. the preparation method of microencapsulated coating amino acid according to claim 1 is characterized in that organic solvent is ethanol or acetone soln.
3. the preparation method of microencapsulated coating amino acid according to claim 1 is characterized in that amino acid can be methionine or lysine or lysine or arginine or threonine or phenylalanine.
4. according to the preparation method of claim 1 and 3 described microencapsulated coating amino acids, it is characterized in that amino acid is feed grade.
5. the preparation method of microencapsulated coating amino acid according to claim 1 is characterized in that powder of amino acids is the powder of ultramicro grinding, and granularity is the 100-150 order.
6. the preparation method of a microencapsulated coating amino acid, it is characterized in that earlier powder of amino acids with 30-60% joins in the glyceride of heat fused (30-60%), under the 30-90rpm rotating speed, stir 20-50min, high speed dispersion, rotational speed regulation is at 10000-20000rpm, time 1-3min, carry out spray-drying after high speed dispersion is even, EAT is a normal temperature, leaving air temp normal temperature, feed rate 1-3L/min, the spray-drying thing carries out granulating and coating under 50-80 ℃, coating solution is the stearic acid ethanolic solution of 1-3%, and the time is 2-4h.
CN200810162307A 2008-12-01 2008-12-01 Preparation method of microencapsulated coating amino acid Pending CN101744111A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN200810162307A CN101744111A (en) 2008-12-01 2008-12-01 Preparation method of microencapsulated coating amino acid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN200810162307A CN101744111A (en) 2008-12-01 2008-12-01 Preparation method of microencapsulated coating amino acid

Publications (1)

Publication Number Publication Date
CN101744111A true CN101744111A (en) 2010-06-23

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN200810162307A Pending CN101744111A (en) 2008-12-01 2008-12-01 Preparation method of microencapsulated coating amino acid

Country Status (1)

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CN (1) CN101744111A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102908337A (en) * 2012-10-12 2013-02-06 大连医诺生物有限公司 Microencapsulated amino-acid composition and preparation method of microencapsulated amino-acid composition
WO2017114339A1 (en) * 2015-12-30 2017-07-06 大连医诺生物有限公司 Microencapsulation of β-alanine
CN110574832A (en) * 2019-10-15 2019-12-17 湖州师范学院 Coated amino acid and preparation method thereof
CN111568881A (en) * 2020-06-08 2020-08-25 广东悦生生物科技有限公司 Nucleocapsid slow-release amino acid tonic and preparation method thereof
CN113995058A (en) * 2021-10-11 2022-02-01 珠海市德海生物科技有限公司 Coated amino acid and preparation method and application thereof

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102908337A (en) * 2012-10-12 2013-02-06 大连医诺生物有限公司 Microencapsulated amino-acid composition and preparation method of microencapsulated amino-acid composition
WO2014056280A1 (en) * 2012-10-12 2014-04-17 大连医诺生物有限公司 Microencapsulated amino acid composition and preparation method thereof
US10525008B2 (en) 2012-10-12 2020-01-07 Innobio Corporation Limited Microencapsulated amino acid composition and the method of manufacturing the microencapsulated amino acid composition
WO2017114339A1 (en) * 2015-12-30 2017-07-06 大连医诺生物有限公司 Microencapsulation of β-alanine
US10555909B2 (en) 2015-12-30 2020-02-11 Innobio Corporation Limited Microencapsulation of B-alanine
CN110574832A (en) * 2019-10-15 2019-12-17 湖州师范学院 Coated amino acid and preparation method thereof
CN111568881A (en) * 2020-06-08 2020-08-25 广东悦生生物科技有限公司 Nucleocapsid slow-release amino acid tonic and preparation method thereof
CN113995058A (en) * 2021-10-11 2022-02-01 珠海市德海生物科技有限公司 Coated amino acid and preparation method and application thereof

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Application publication date: 20100623