Process for producing high-energy feed of aquatic product
A manufacturing process and high-energy technology, applied in the field of aquatic feed manufacturing process, can solve the problems of high crude fat content, unable to meet the production needs of compound feed, and unable to meet the production process.
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Embodiment 1
[0013] Taking the floating material with 10% crude fat in the finished product as an example, set the mold size to 4.0mm, and the processing steps are as follows:
[0014] Prepare materials according to the requirements of compound feed formula, and grind all raw materials except flour, fish oil and additives, pass through 60 to 100 mesh screens, and then mix until the coefficient of variation of mixing uniformity C.V.<10%, ready for use: in this step, The raw materials can also be mixed first, crushed, and then sieved.
[0015] For secondary mixing, use general mixing equipment to put the mixture, flour and additives of the above-mentioned part of the raw materials into mixing, and spray 1% of the total weight of fish oil, and mix until the coefficient of variation of mixing uniformity C.V.<7.5%.
[0016] For puffing treatment, single-screw or twin-screw puffing machines can be used, and the mold size is set to 4.0mm. Put the above mixed material into the extruder, control t...
Embodiment 2
[0022] When the crude fat content of the finished product is higher than more than 18%, the feed produced can only be sinking feed. Taking the processing of sinking material with a finished crude fat content of 25% as an example, the processing steps are the same as the above example, and the processing parameters are adjusted as follows:
[0023] 3% of the total weight of fish oil is added during the secondary mixing, and the inherent crude fat content in the raw material is 5%, and the expanded material is then sprayed with 17% of the total weight of fish oil. During production, the extruder adopts a double-tooth structure Twin-screw extruder, the extruding tempering temperature is 90-100°C, the moisture content of the material after conditioning is 24-26%, the expansion coefficient of feed pellets is 1.3-1.4, and the bulk density of feed pellets is controlled between 520-580g / L During the period, the drying temperature is set at 95-105°C, and the drying time is controlled a...
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Abstract
Description
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Application Information
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