Partial calcification of free fatty acid mixtures, livestock feed compositions including them, and methods of making same

11219227 · 2022-01-11

Assignee

Inventors

Cpc classification

International classification

Abstract

The present invention includes a nutritional supplement composition that may be used for livestock and the like, as well as to a livestock feed mixture containing same. Also included are methods of preparing the nutritional supplement composition, the livestock feed mixture, as well as methods of providing nutrition to livestock and the like. The livestock feed composition comprises: (a) a solid particulate livestock feed material and (b) a solidified particulate mixture of (i) free fatty acid and (ii) a calcium salt of a fatty acid, the calcium salt of a fatty acid being present in a molar ratio amount in the range of from about 25% to about 55% of the amount of the free fatty acid. The preferred mixture is a solid having an onset melt point of between about 140 and 170 degrees Fahrenheit, and a hardness of from about 5 to about 15 Shore A units at 170 degrees Fahrenheit.

Claims

1. A method of improving handling characteristics of an animal feed product, the method comprising: providing the animal feed product; providing a partially calcified free fatty acid mixture comprising: free fatty acid; and neutralized fatty acid comprising a calcium salt of the fatty acid in an amount from about 25% to about 55%, on a molar basis, of total fatty acid in the mixture; wherein the composition has an onset melt point of from 170° F. to 205° F.; and blending the partially calcified free fatty acid mixture into the animal feed.

2. The method of claim 1, wherein the free fatty acid comprises tallow, non-tallow fatty acids, or a mixture thereof.

3. The method of claim 1, wherein the free fatty acid comprises a non-tallow fatty acid comprising a fatty acid from palm oil, soy oil, fish oil, linseed oil or flax oil.

4. The method of claim 1, wherein the partially calcified free fatty acid mixture has a hardness of at least about 15 shore A units at 170° F.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) FIG. 1 is a graph of temperature versus reaction time showing a typical reaction profile as may arise in accordance with one embodiment of the present invention;

(2) FIG. 2 is a graph of melt point versus percent calcification showing a profile as may arise in accordance with one embodiment of the present invention;

(3) FIG. 3 is a graph of Shore A hardness versus temperature for multiple percentages of calcification, and showing a profile as may arise in accordance with one embodiment of the present invention;

(4) FIG. 4 is a graph of temperature for a specified Shore A hardness versus percent calcification for multiple percentages of calcification, and showing a profile as may arise in accordance with one embodiment of the present invention;

(5) FIG. 5 is a graph of Shore A hardness versus temperature for multiple percentages of calcification, and showing a profile as may arise in accordance with one embodiment of the present invention;

(6) FIG. 6 is a graph of Shore A hardness versus temperature for multiple percentages of calcification, and showing a profile as may arise in accordance with one embodiment of the present invention; and

(7) FIG. 7 is a graph of temperature for a specified Shore A hardness of 15 versus percent calcification, and showing a profile as may arise in accordance with one embodiment of the present invention.

(8) FIG. 8 is a picture of a compression testing experimental setup used to assess the physical characteristics of compositions of the present invention.

(9) FIG. 9 is a picture of test results of particulate matter as a result of compression testing, showing the comparative physical characteristics of compositions of the present invention and those of the prior art.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

(10) In accordance with the foregoing summary of the invention, the following presents a detailed description of the preferred embodiments, which are considered to be the best mode thereof.

(11) The preferred method and compositions described herein are not intended to be exhaustive or to limit the invention to the precise forms disclosed. They are chosen and described to explain the principles of the invention and the application of the method to practical uses so that others skilled in the art may practice the invention.

Example 1 of the Manufacturing Process of the Present Invention

(12) As a preferred but non-limiting example of the method by which compositions of the present invention may be made, the following steps may be followed:

(13) 1. Heat mixture of free fatty acids to 205-240 degrees F.

(14) 2. Add desired molar equivalents of calcium as calcium oxide or calcium hydroxide with good mixing. The exothermic reaction of calcium oxide or hydroxide with free fatty acids causes temperature to rise to about 260-280 degrees F. (dependent on insulation and heat loss of reactor system).

(15) 3. Hold reaction mixture at 240-260 degrees F. until reaction is complete as measured by change in Acid Value (AV). The reaction may be monitored by determining Acid Value (AV) of the material; for example: for a target of 40% calcification the AV at completion would be about 60% of the starting AV (i.e., AV final=0.6*AV starting).

(16) 4. When reaction is complete as determined in 3 above, material is either prilled in a prilling (spray chilling) tower or flaked on a rotary drum flaker by use of methods and apparatus well known in the field.

(17) Normally, the maximum percentage of fat attainable for the 100% calcium soaps or the prior art is about 80-82% due to the 100% calcium level while the maximum percentage of fat attainable is over 90 percent fat for products made in accordance with the present invention.

(18) While the 100% calcium soap products do not melt, the melt point and hardness can be controlled for the partially calcified products made in accordance with the present invention.

(19) The calcium soaps have historically been made from palm oil and soybean oil. Both these oils and free fatty acid mixtures from these oils are liquids at room temperature and so to sell these products as a solid into the dairy industry the companies using these starting materials had to make the calcium soaps.

Example 2 of the Manufacturing Process of the Present Invention

(20) A repeatable, controlled process was developed for partial calcification of free fatty acids which included heating melted free fatty acids to 205 F, slowly adding the calculated amount of calcium oxide and allowing the reaction to proceed for approximately 2 hours after all calcium oxide was added. The temperature typically rises to 230-240 F shortly after the final addition of calcium oxide and remains in the range of 220-230 F throughout the 2 hour reaction.

(21) As an alternative to a timed reaction, the initial Acid Value (AV) can be obtained by known titration methods and the AV monitored throughout the reaction until AV value levels out (e.g. initial AV=185; for 40% calcification final AV=111).

(22) A typical temperature-time profile is plotted in FIG. 1.

(23) Melt Point and Hardness Properties of the Compositions

(24) Melt point and hardness vs. temperature properties were determined for two different mixtures of fatty acids.

(25) First Mixture=Initial AV of 185.

(26) Second Mixture=Initial AV of 192.

(27) Two Melt Points were determined.

(28) Onset Melt Point=temperature at which first signs of melting are observed.

(29) Clear Melt Point=temperature at which no solid remains.

(30) The Hardness was determined at various temperatures with a Rex Vest Pocket 1500 Durometer with a Shore A hardness scale.

(31) Results are shown in FIGS. 2-7, the composition(s) made in accordance with the present invention are designated as “EBH.”

(32) Product Compression Properties

(33) The product made from a fatty acid mixture with initial AV=185 was calcified to 35% Ca and subjected to a simple compression test along with prilled 0% starting material and a 100% Ca-Salt commercial product (i.e., Megalac).

(34) The set-up used to do this test is shown in FIG. 8.

(35) Prilled materials were placed into a beaker with weights compressing the prills to create either 2 psi or 4 psi to simulate the compressive forces of bulk storage.

(36) The weighted beaker of prills was placed in a 50 degrees C. oven for 30 min and then cooled to room temperature and tested for pourability and appearance.

(37) Pictures were taken and are shown in FIG. 9.

(38) From the data, a conclusion is that prilled 0% Ca starting material melted-compressed such that it was not pourable, while the 35% Ca prilled material showed no significant signs of compression and poured out of the beaker very well.

(39) Product in accordance with the present invention may be suitable for bulk storage, such as in silos or otherwise. It may also be bagged for storage and can even be transported or stored in relatively warmer climates. By contrast prior art formulations, such as the EB100 product and other mixtures of free fatty acids from tallow, palm or soy cannot.

(40) The product of the present invention also features a controllable, increased onset melt point, as well as a controllable, increased hardness at all temperatures relative to free fatty acid mixtures of the prior art.

(41) The product can be used as a feed supplement and may be formulated into fat supplementing animal feeds for livestock and the like. Examples may include dairy cow rations. The animal feeds may be rendered into particulate or pelletized form in accordance with and through the use of equipment and methods known and used in the art. By contrast, the pelleted feed applications compare favorably to the EB100 product and other mixtures of free fatty acids from tallow, palm or soy, which cannot be effectively pelleted.

(42) While specific configurations and arrangements are discussed, it should be understood that this is done for illustrative purposes only. A person skilled in the relevant art will recognize that other process and composition variations can be used without departing from the spirit and scope of the invention. It will be apparent to a person skilled in the relevant art that this invention can also be employed in a variety of other applications.