Drying in baby food

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General Description

For a general overview of infant formula production, please see ‘Evaporation’ in the ‘Baby Food’ subsection.


BF FlowSheet.jpg


Figure: Infant formula baby food process flow sheet Source: http://www.spx.com/en/apv/industries/dairy/evaporated-dried/baby-food/



Drying

Drying takes place in a spray dryer system. The concentrate is atomised to droplets, using either a centrifugal or a nozzle atomiser, and it is then dried by hot air. The spray drying stage of infant formula production is key to producing a powder with a long stable shelf life.


A spray dryer system typically consists of:

  • one or several high pressure nozzles or a rotary atomizer wheel for the atomization of the concentrate
  • a drying chamber/tower
  • an integrated fluid bed for secondary drying
  • an external fluidizer
  • one or several cyclone(s) and/or bag filter(s) as an air/powder separation system
  • a fines return system to improve the agglomeration


When designing a spray drying plant for powder production the following must be taken into consideration:

  • production time between CIP cleaning
  • powder structure
  • drying parameters

To order to minimise the need for cleaning, plants may include an efficient high-pressure air broom, which reduces the powder deposits in the dryer, thereby achieving prolonged running times.


Spray drying.jpg

Figure:Lower part of spray drying chamber and Vibro-Fluidizer® for after drying / cooling of powder. Source: GEA Niro


Spray drying2.jpg

Figure: Spray Drying Unit. Source: GEA Niro


Application

Baby Food


Typical Parameters

The drying temperature and solids content are a high as possible In order to improve production efficiency. Product composition, however, is a decisive factor as to what parameters can be selected. In general: The drying efficiency and capacity of a spray dryer is increased by increasing the difference between the drying air and exhaust air temperature. High ambient air humidity requires a lower spray drying temperature or a dehumidification of the air, which obviously increases the production costs. Solids content prior to spray drying 45-60% Solids content after spray drying approx 97%


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