Process for producing powder from milk or similar liquids

• US 3,956,521 A
• Filed: 10/18/1974
• Issued: 05/11/1976
• Est. Priority Date: 10/22/1973
• Status: Expired due to Term

• Current Assignee: Aktieselskabet Niro Atomizer
• Original Assignee: Aktieselskabet Niro Atomizer
• Inventors: Pisecky, Jan, Westergaard, Vagn
• Primary Examiner(s): Hunter, Jeanette M.
• Application Number:
  US05/515,956
• Time in Patent Office: 571 Days
• Field of Search: 426/187, 426/358, 426/467, 426/471, 426/588
• US Class Current: 426/588
• CPC Class Codes: A23C 1/04 by spraying into a gas stream
• CPC Class Codes: A23C 2210/05 Conventional drying followed by fluidised bed drying; Fluidised bed drying at the bottom of a spray-drier
• CPC Class Codes: A23L 3/46 Spray-drying

Abstract

Milk or similar liquids are spray-dried into a powder having a considerable residual humidity, using an inlet temperature for the drying gas higher than usual. This spray-dried powder is after-dried in a fluidized bed. The fine particles entrained by the gas leaving the spray-drier and the fluidized bed are separated from said gases and added to the main bulk of powder after the latter has left the spray-drier and if necessary has been dried to such an extent that the fine particles will not stick thereto. A powder having very high bulk density is obtained and the heat economy is improved.

Claims

1. In a process for producing powder from liquids which when spray-dried form particles containing a substantial amount of vacuoles, such as milk, in which process the liquid, preferably in the form of a concentrate, is, by the use of a rotary atomizer in a first stage, spray-dried in hot gas into a moist powder which in a second stage is after-dried in hot gas in a fluidized bed to the moisture content of the final product desired, while the particles carried along are separated from the gas leaving the two stages, wherein the improvement comprises the steps of:

a. raising the temperature of the hot gas which is supplied to the first stage to at least 10°

C higher than the highest temperature which would be permissible for the liquid in question if the spray drying for the production of the final product with the moisture content desired were to be performed in only one stage and with the same degree of heat damage,

b. spray drying in the first stage wherein the moisture content of the powder obtained from this stage, dependently on the liquid to be dried, is 2-15% higher than the desired moisture content in the final product and the highest value of which moisture content is determined with due regard to the fact that agglomeration shall be substantially avoided, and

c. separating the fine particles from the the gas and adding them to the main bulk of the powder produced after the latter has been dried to a moisture content of at the most 2-10%, so that the fine particles do not stick thereto to such an extent that stable agglomerates are formed.

2. A process as claimed in claim 1 for the production of whole milk powder with a moisture content of 1.0-2.5% by weight and with a Solubility index according to ADMI of at the most 0.5 from a whole milk concentrate with a content of dry matter of 45-57%, wherein the hot gas, which is supplied to the first stage, has a temperature of between 190°

and 270°

C and the spray drying in the first stage is carried on to a moisture content of the powder of 4-10% by weight.

3. A process as claimed in claim 2 in which the starting material is a whole milk concentrate having a content of dry matter of 50-54% by weight, wherein the gas supplied to the first stage has a temperature of between 240°

and 260°

C and the spray drying in the first stage is carried on to a moisture content of 5-7% by weight.

4. A process as claimed in claim 1 for the production of skim-milk powder with a moisture content of 1-4% by weight and with a Solubility index according to ADMI of at the most 0.5 from a skim-milk concentrate having a content of dry matter of 45-57% by weight, wherein the hot gas supplied to the first stage has a temperature of between 210°

and 420°

C and the spray drying in the first stage is carried on to a moisture content in the powder of 5-18% by weight.

5. A process as claimed in claim 4 in which the starting material is a skim-milk concentrate with a content of dry matter of 48-52% by weight wherein the gas supplied to the first stage has a temperature of between 265°

and 285°

C and the spray drying in the first stage is carried on to a moisture content of 4-6% by weight.

6. A process as claimed in claim 1 for the production of powder of milk containing products, wherein the fine particles separated from the gas leaving the first stage and the second stage are added to the main bulk of the powder in the lower part of the first stage.

7. Powder produced by a process as claimed in claim 1.

8. Whole milk powder produced by a process as claimed in claim 3.

9. Whole milk powder as claimed in claim 8 and having a bulk density higher than 0.65 g/cm³.

10. Skim-milk powder produced by a process as claimed in claim 5.

11. Skim-milk powder as claimed in claim 10 and having a bulk density higher than 0.70 g/cm³.