Milk powder composition
US-2024074447-A1 · Mar 7, 2024 · US
US9894923B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9894923-B2 |
| Application number | US-201214008148-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 30, 2012 |
| Priority date | Mar 31, 2011 |
| Publication date | Feb 20, 2018 |
| Grant date | Feb 20, 2018 |
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The present invention relates to a process for the production of a powdered composition from a liquid composition comprising fat, protein or both, to the powdered composition obtained thereby and products containing said powdered composition.
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The ivention claimed is: 1. A process for the production of a powdered composition from a liquid composition comprising fat, protein or both, which process comprises: a) a first atomizing step comprising: i. feeding a mixture of gas and steam into a mixing chamber, and ii. feeding the liquid composition into the mixing chamber containing the mixture of gas and steam by spraying the liquid composition through an inlet nozzle into the mixing chamber so as to obtain a mixture, wherein the liquid composition is atomized through the inlet nozzle, and wherein the mixture of gas and steam creates a non-evaporative zone in which the feeding of the liquid composition into the mixing chamber takes place without simultaneous evaporation, b) a second atomizing step, comprising: i. spraying the mixture out of the mixing chamber through an outlet nozzle and into a drying chamber, wherein the mixture is atomized through the outlet nozzle and c) drying the mixture in the drying chamber, so as to obtain the powdered composition. 2. The process according to claim 1 , wherein the gas is air. 3. The process according to claim 1 , wherein the liquid composition has a dry matter content from 55 to 70 weight % based on total weight of the liquid composition. 4. The process according to claim 1 , wherein the liquid composition has a temperature from 55 to 90° C. when sprayed into the mixing chamber. 5. The process according to claim 1 , wherein the weight/hour ratio of gas:steam in the mixing chamber is from 1:0.5 to 1:25. 6. The process according to claim 1 , wherein the weight/hour ratio of gas:steam:liquid composition in the mixing chamber is 0.5 to 5:2 to 15:100. 7. The process according to claim 1 , wherein the equilibrium temperature in the mixing chamber is from 90 to 155° C. 8. The process according to claim 1 , wherein the liquid composition is sprayed into the mixing chamber at a flow-rate from 250 to 700 kg/hour. 9. The process according to claim 1 , wherein the mixing chamber has a length of 2 to 10 cm. 10. The process according to claim 1 , wherein the pressure in the mixing chamber is 2 to 10 bar. 11. The process according to claim 1 , wherein the liquid composition comprises fat, protein and carbohydrates. 12. The process according to claim 1 , wherein the liquid composition has a fat content of 20 to 35 weight % based on dry weight of the liquid composition and a protein content of 10 to 25 weight % based on dry weight of the liquid composition. 13. A powdered composition, wherein the powdered composition is obtained according to the process of claim 1 . 14. The powdered composition according to claim 13 , wherein the powdered composition has a particle size distribution D (v, 0.5) of 80 to 320 μm. 15. The powdered composition according to claim 13 , wherein the powdered composition has a particle size distribution D (4.3) of 80 to 350 μm. 16. The powdered composition according to claim 13 , wherein the powdered composition has a bulk density of 0.4 to 0.6 g/ml. 17. A nutritional product comprising the powdered composition according to claim 13 , where the nutritional product is a food or feed product. 18. The process according to claim 1 , further comprising: collecting the powdered composition from the drying chamber through a recovery outlet. 19. A process for the production of a powdered composition from a liquid composition comprising fat, protein or both, which process comprises: spraying the liquid composition through an inlet nozzle into a mixing chamber containing a mixture of gas and steam having a gas:steam weight ratio of from 1:0.5 to 1:25, wherein the mixture of gas and steam creates a non-evaporative zone in which the spraying of the liquid composition into the mixing chamber takes place without simultaneous evaporation, and wherein the liquid composition is atomized through the inlet nozzle and heated by the mixture of gas and steam to generate a mixture; spraying the mixture out of the mixing chamber through an outlet nozzle and into a drying chamber, wherein the mixture is atomized through the outlet nozzle; and drying the mixture in the drying chamber to generate the powdered composition. 20. The process according to claim 1 , wherein feeding a mixture of gas and steam into the mixing chamber comprises separately feeding the gas and steam into the mixing chamber, the steam having a temperature of 164° C. into the mixing chamber at a rate of 21.2 kg/hour and the air having a temperature of 170° C. into the mixing chamber at a rate of 3.8 kg/hour. 21. The process according to claim 1 , wherein the gas comprises about 78 vol. % nitrogen, and about 21 vol. % oxygen.
Shaping or working-up of animal feeding-stuffs · CPC title
free-flowing powder or instant powder, i.e. powder which is reconstituted rapidly when liquid is added (A23P10/20, A23P10/30 take precedence) · CPC title
Fatty acids; Fats; Products containing oils or fats · CPC title
Sugars; Polysaccharides · CPC title
Dairy proteins · CPC title
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