Method for producing highly unsaturated fatty acid calcium salt
An unsaturated fatty acid and unsaturated technology, applied in the field of preparation of rumen bypass feed additives, can solve the problems of lack of storage stability, inability to grind fine particles, etc.
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Embodiment 1
[0059] 13.8 lbs of calcium oxide was added to an upright mixer (equipped with Cowles type mixing blades) containing 69.6 lbs of CLA-60. CLA-60 contains a concentration of 65% by weight CLA and 95% by weight free fatty acids. The total unsaturated fatty acid content is 90% by weight. Heat the CLA-60 to 60°C before adding calcium oxide. After the calcium oxide was uniformly dispersed, 10.8 lbs of water was added and the temperature of the mixture was raised to 120°C. Stirring is continued until a uniform homogeneous mixture is obtained, which is then poured from the container into a plate, where the reaction is complete, and the product is then cooled. The final product was milled to obtain free-flowing non-dusty granules with a total fat content of approximately 83% by weight.
Embodiment 2
[0061] 33.8 lbs of palm fatty acid distillate (PFAD) was added to 68.5 lbs of CLA-60 which had been heated to 60°C and stirred until a homogeneous homogeneous mixture was obtained. Continue to add 18.4 lbs of calcium oxide with stirring. After the calcium oxide was uniformly dispersed, 15.2 lbs of water was added and the temperature of the mixture was raised to 120°C. The product was collected as in Example 1 (its fat content was 85% by weight).
[0062] Free-flowing obtained despite reduced calcium oxide (relative to fat content)
[0063] of granular products. The content of calcium oxide corresponds to 20% by weight (relative to CLA) and 14% by weight (relative to PFAD).
Embodiment 3
[0065] Adopt following composition, react by embodiment 2 method:
[0066] 4,884 lb CLA
[0067] 2,085 lbs PFAD
[0068] 1,504 lbs calcium oxide
[0069] 1,716 lbs water
[0070] The resulting free-flowing granular product had a total fat content of 82.25% by weight.
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