CN107141240B - Preparation method of feed-grade zinc hydroxy methionine chelate - Google Patents

Preparation method of feed-grade zinc hydroxy methionine chelate Download PDF

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CN107141240B
CN107141240B CN201710465113.2A CN201710465113A CN107141240B CN 107141240 B CN107141240 B CN 107141240B CN 201710465113 A CN201710465113 A CN 201710465113A CN 107141240 B CN107141240 B CN 107141240B
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zinc
hydroxymethionine
chelate
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washing
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CN107141240A (en
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吴兵
邵勇杰
李奉仙
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Sichuan jilongda Biotechnology Group Co.,Ltd.
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GUANGHAN LONGDA FEED CO Ltd
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    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C319/00Preparation of thiols, sulfides, hydropolysulfides or polysulfides
    • C07C319/14Preparation of thiols, sulfides, hydropolysulfides or polysulfides of sulfides
    • C07C319/20Preparation of thiols, sulfides, hydropolysulfides or polysulfides of sulfides by reactions not involving the formation of sulfide groups
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
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    • A23K20/00Accessory food factors for animal feeding-stuffs
    • A23K20/10Organic substances
    • A23K20/142Amino acids; Derivatives thereof
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23KFODDER
    • A23K20/00Accessory food factors for animal feeding-stuffs
    • A23K20/20Inorganic substances, e.g. oligoelements
    • A23K20/30Oligoelements

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Abstract

The invention relates to a production method of a feed additive, and particularly discloses a preparation method of a feed-grade zinc hydroxy methionine chelate, which comprises the following steps: A. adding a sodium hydroxide reagent into an inorganic salt water solution of zinc to obtain a solid phase substance; B. washing the solid phase with water to remove soluble components; C. adding water into the washing slag for homogenate; D. adding hydroxymethionine according to the proportion that the molar ratio of the zinc content in the slurry to the hydroxymethionine is less than or equal to 0.5 to carry out chelation reaction; E. and carrying out post-treatment on the reaction product to obtain the product. The invention has the advantages that: 1) the hydroxyl zinc methionine product with higher purity can be prepared and is more suitable to be used as a feed additive; 2) the hydroxyl zinc methionine chelate can be prepared by the method; 3) the chelating reaction rate is high, the energy consumption is low, and the industrial popularization is facilitated.

Description

Preparation method of feed-grade zinc hydroxy methionine chelate
Technical Field
The invention relates to the field of animal breeding, in particular to a preparation method of a feed additive.
Background
Since the first confirmation of the animal nutrition of zinc by rat experiments in 1934 by Todd et al, zinc is a component of more than 200 kinds of metalloenzymes, hormones and insulin in animal organisms, and has great nutritional value in the aspects of promoting the growth and development of the organisms, maintaining the normal metabolism of the organisms, promoting appetite, maintaining the normality of sexual organs and sexual functions, accelerating wound healing, protecting skin health, enhancing immune mechanism, improving resistance and the like.
The hydroxyl zinc methionine has the characteristics of low toxicity, low rumen degradation rate, promotion of rumen microorganism synthesis, protein saving in daily ration, improvement of production performance of dairy cows, improvement of animal production performance and immunity, reduction of nitrogen emission, less environmental pollution, simple production process, lower price and the like, and is the most economical and effective amino acid source and zinc source for animals. Therefore, zinc hydroxy methionine is gradually replacing some amino acids with higher price in the market.
The preparation method of the hydroxyl zinc methionine is generally as follows: mixing hydroxy methionine and inorganic salt water solution of zinc, and maintaining certain reaction temperature in the presence of alkaline solution.
For example, patent document CN1287795A discloses a method for preparing zinc hydroxymethionine feed additive, which comprises reacting liquid hydroxymethionine and zinc inorganic salt aqueous solution at a molar ratio of 1: 1-2 at 50-100 ℃ and in the presence of sodium hydroxide at a pH of 6-8 under normal pressure for 0.8-1.2 hours, washing and drying the reaction product to obtain the final product.
And for example, patent document No. CN102617426A discloses a method for preparing zinc hydroxymethionine for prawns, which comprises the steps of using zinc chloride and hydroxymethionine, oscillating the zinc chloride and hydroxymethionine with an ultrasonic cell disruptor for 5min, mixing the zinc chloride and hydroxymethionine uniformly according to the mass ratio of 1:2, adjusting the pH to 6.8-7.2 with 0.2mol/L NaOH, and finally adsorbing, drying and crushing the zinc hydroxymethionine with zeolite powder to obtain the zinc hydroxymethionine product.
Zinc hydroxy methionine is classified into complexes and chelates:
the hydroxyl methionine zinc complex is generated by complexing one mole of zinc and one mole of hydroxyl methionine through a coordination bond to form a complex cation, and the complex is positively charged. Hydroxymethionine complex formula: ZnC5H8O3S。
The zinc hydroxymethionine chelate is formed by chelating one mole of zinc and two moles of hydroxymethionine through coordination bonds and covalent bonds to form an inner complex salt, and the chelate is electrically neutral. The molecular formula of the hydroxyl zinc methionine chelate is as follows: zn (C)5H10O3S)2
However, the methods of the two patent documents only can produce hydroxyl zinc methionine complex through complexation reaction, and cannot obtain hydroxyl zinc methionine chelate.
Disclosure of Invention
In order to obtain a feed-grade zinc hydroxymethionine chelate product with less impurity content and higher purity and optimize the production rate, the invention provides a preparation method of the feed-grade zinc hydroxymethionine chelate.
The technical scheme adopted by the invention is as follows: the preparation method of the feed-grade zinc hydroxy methionine chelate comprises the following steps:
A. adding a metered sodium hydroxide reagent into an inorganic salt water solution of zinc, and carrying out solid-liquid separation after full reaction to obtain a solid-phase substance;
B. washing the solid phase substance with water to remove soluble components therein to obtain washing slag;
C. adding water into the washing slag for homogenate to obtain slurry;
D. adding hydroxymethionine according to the proportion that the molar ratio of the zinc content in the slurry to the hydroxymethionine is less than or equal to 0.5 to carry out chelation reaction, and obtaining a reaction product after the reaction is finished;
E. and carrying out solid-liquid separation, washing and drying on the reaction product to obtain a feed-grade zinc hydroxy methionine chelate product.
In the invention, the inventor prepares the intermediate slurry first and then carries out chelation reaction on the intermediate slurry and the hydroxymethionine to prepare the zinc hydroxymethionine chelate. The method can effectively avoid mixing anions and impurity cations in the zinc inorganic salt aqueous solution and non-target product impurities such as cations or anions in the alkaline solution into the product, thereby being capable of preparing the hydroxyl zinc methionine product with higher purity and being more suitable for being used as a feed additive.
On the other hand, the intermediate slurry in the invention can generate chelation reaction with the hydroxymethionine, thereby realizing the hydroxymethionine chelate Zn (C)5H10O3S)2And (4) preparing. The zinc hydroxy methionine chelate is a slightly soluble substance, so that the zinc hydroxy methionine chelate cannot absorb moisture and is beneficial to feed processing; in addition, zinc hydroxymethionine is more stable in acid environment, and the absorption rate of zinc in the intestinal tract cannot be reduced due to the combination of substances such as phytic acid and oxalic acid.
In the third aspect, the intermediate slurry is formed, so that the chelating reaction is more favorably carried out, the reaction rate is higher, and the energy is saved.
As a further improvement of the invention, the chelating reaction conditions of the step D are as follows: the reaction temperature is 50-60 ℃, the reaction time is 20-40 minutes, the stirring speed in the reaction process is 40-80 r/min, and the pH value of a reaction system is 6-7. The scheme is a better chelation reaction condition summarized by a large number of experiments, under the reaction condition, the chelation reaction can be carried out at a higher speed, and the energy consumption can be maintained at a lower level, so that the scheme is more favorable for industrial popularization.
It will be understood by those skilled in the art that aqueous solutions of inorganic salts capable of reacting with sodium hydroxide reagents to form hydroxide precipitated zinc are generally useful as starting materials for the present invention, but zinc sulfate solutions and zinc chloride solutions are preferred as the starting materials from the standpoint of cost of the starting materials and safety of production.
As a further improvement of the method, the mass percent concentration of zinc (calculated as Zn) in the slurry in the step C is 22-26%, and the proper slurry concentration can ensure that the chelation reaction is performed at a faster rate.
As a further improvement of the method, after the reaction in the step A is finished, the pH value of the liquid phase is 9-10, and the pH value can be used as a control index of the adding amount of the sodium hydroxide reagent to ensure that zinc in the solution is fully precipitated, and excessive sodium hydroxide reagent is not added, so that the waste of raw materials is reduced, and the load of a subsequent washing process is avoided.
The invention has the beneficial effects that: 1) the hydroxyl zinc methionine product with higher purity can be prepared and is more suitable to be used as a feed additive; 2) the hydroxyl zinc methionine chelate can be prepared by the method; 3) the chelating reaction rate is high, the energy consumption is low, and the industrial popularization is facilitated.
Drawings
FIG. 1 is a process flow diagram of the first embodiment.
Detailed Description
The invention is further illustrated with reference to the following figures and examples.
The first embodiment is as follows:
a feed-grade zinc hydroxy methionine chelate product A is prepared according to the following method:
(1) dissolving solid zinc sulfate, and removing insoluble substances in a filter pressing mode to obtain a zinc sulfate solution.
(2) Adding a sodium hydroxide solution into a zinc sulfate solution, fully reacting, collecting a solid-phase substance in a filter pressing mode, washing soluble substances such as sodium sulfate, sodium hydroxide and the like contained in the solid-phase substance in a washing mode, and detecting whether sulfate radicals are washed out or not by utilizing barium chloride to obtain washing residues.
(3) Transferring the water washing slag into a reaction tank, and adding clear water for homogenate. The zinc content of the homogenate was 23.3% (mass percent).
(4) By measuring the content of zinc, a chelation reaction is carried out according to the molar ratio of zinc to hydroxymethionine of 1:2.05, the reaction temperature is 50 ℃, the reaction time is 30 minutes, the stirring speed is 60 revolutions per minute, and the pH value of the reaction system is 6.
(5) And removing excessive hydroxymethionine by filter pressing and washing the precipitate of the zinc hydroxymethionine chelate.
(6) And (3) flash drying the obtained hydroxyl methionine zinc chelate crude product to remove redundant water, and finally obtaining a product A.
The composition of product A was analyzed and the results are shown in Table 1.
Example two:
preparing a feed-grade zinc hydroxy methionine chelate product B according to the following method:
(1) dissolving solid zinc chloride, and removing insoluble substances in a filter pressing mode to obtain a zinc chloride solution.
(2) Adding a sodium hydroxide solution into a zinc chloride solution, fully reacting, collecting a solid-phase substance in a filter pressing mode, and washing soluble substances such as sodium chloride, sodium hydroxide and the like contained in the solid-phase substance in a water washing mode to obtain water washing slag.
(3) Transferring the water washing slag into a reaction tank, and adding clear water for homogenate. Extracting homogenate to detect the zinc content of 25.1% (mass percentage)
(4) By measuring the content of zinc, chelation reaction is carried out according to the molar ratio of zinc to hydroxymethionine of 1:2.1, the reaction temperature is 60 ℃, the reaction time is 20 minutes, the stirring speed is 80 r/min, and the pH value of the reaction system is 6.8.
(5) And removing excessive hydroxymethionine by filter pressing and washing the precipitate of the zinc hydroxymethionine chelate.
(6) And (3) carrying out flash evaporation drying on the obtained hydroxyl methionine zinc chelate crude product to remove redundant water, and finally obtaining a product B.
The composition of product B was analyzed and the results are shown in Table 1.
Table 1: feed-grade hydroxyl zinc methionine chelate product ingredient analysis table
Zn(C5H10O3S)2 Moisture content Lead (mg/kg) Arsenic (mg/kg) Cadmium (mg/kg) Yield of
Product A 86.2% 7.6% 4.6 3.2 6.8 96.8%
Product B 85.9% 7.7% 5.3 4.1 5.2 96.2%

Claims (2)

1. The preparation method of the feed-grade zinc hydroxy methionine chelate comprises the following steps:
A. dissolving solid zinc sulfate, and removing insoluble substances in a filter pressing mode to obtain a zinc sulfate solution;
B. adding a sodium hydroxide solution into a zinc sulfate solution, fully reacting, collecting a solid-phase substance in a filter pressing mode, and washing soluble substances in the solid-phase substance in a water washing mode to obtain washing slag;
C. transferring the water washing slag into a reaction tank, adding clear water for homogenate, and extracting the homogenate to detect that the mass percentage content of zinc is 23.3%;
D. according to the measured zinc content, carrying out chelation reaction according to the molar ratio of zinc to hydroxymethionine of 1:2.05, wherein the reaction temperature is 50 ℃, the reaction time is 30 minutes, the stirring speed is 60 revolutions per minute, and the pH of the reaction system is = 6;
E. removing excessive hydroxymethionine by filter pressing and water washing of the precipitate of the zinc hydroxymethionine chelate;
F. and (3) flash drying the obtained hydroxyl methionine zinc chelate crude product to remove redundant moisture to obtain the hydroxyl methionine zinc chelate.
2. The preparation method of the feed-grade zinc hydroxy methionine chelate comprises the following steps:
A. dissolving solid zinc chloride, and removing insoluble substances in a filter pressing mode to obtain a zinc chloride solution;
B. adding a sodium hydroxide solution into a zinc chloride solution, fully reacting, collecting a solid-phase substance in a filter pressing mode, and washing soluble substances in the solid-phase substance completely in a water washing mode to obtain washing residues;
C. transferring the water washing slag into a reaction tank, adding clear water for homogenate, and extracting the homogenate to detect that the mass percentage content of zinc is 25.1%;
D. according to the measured zinc content, carrying out chelation reaction according to the molar ratio of zinc to hydroxymethionine of 1:2.1, wherein the reaction temperature is 60 ℃, the reaction time is 20 minutes, the stirring speed is 80 r/min, and the pH of the reaction system is = 6.8;
E. removing excessive hydroxymethionine by filter pressing and water washing of the precipitate of the zinc hydroxymethionine chelate;
F. and (3) flash drying the obtained hydroxyl methionine zinc chelate crude product to remove redundant moisture to obtain the hydroxyl methionine zinc chelate.
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