Method for preheating the air circulating in an installation comprising an evaporator coupled to a drying unit

• US 4,313,787 A
• Filed: 07/23/1980
• Issued: 02/02/1982
• Est. Priority Date: 08/03/1979
• Status: Expired due to Term

• Current Assignee: Laguilharre SA
• Original Assignee: Laguilharre SA
• Inventors: Ciboit, Jacques J., Pradines, Eric C.
• Primary Examiner(s): Yudkoff, Norman
• Application Number:
  US06/171,295
• Time in Patent Office: 559 Days
• Field of Search: 159/17 A, 159/17 VS, 159/4 MS, 159/4 VM, 159/4 A, 159/DIG. 8, 159/47, 159/48
• US Class Current: 159/48.1
• CPC Class Codes: A23C 1/12 Concentration by evaporation
• CPC Class Codes: B01D 1/26 Multiple-effect evaporating
• CPC Class Codes: F26B 23/001 using waste heat
• CPC Class Codes: F26B 3/12 in the form of a spray , i.e. sprayed or dispersed emulsions or suspensions spray drying of solutions B01D1/18
• CPC Class Codes: Y02P 70/10 Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
• CPC Class Codes: Y10S 159/08 Multieffect or multistage

Abstract

A method for preheating the air circulating and used in an installation comprising a multi-stage evaporator adapted to concentrate a liquid product, in particular a food product such as a milk product, on the one hand, and a drying unit in which is processed and concentrate issuing from said evaporator, or any other concentrate, on the other hand, said method comprising the steps of heating condensates of said multi-stage evaporator by means of a fluid issuing from said evaporator and hotter than said condensates, then driving the thus-heated condensates into a heat-exchanger wherein they cause air to be preheated.

Claims

1. In a method for concentrating a liquid product into a powdered product wherein said liquid product is treated in a multi-stage evaporator system to form a condensed concentrate product and a condensate and said condensed concentrate product is subsequently dried with hot air to produce a powdered product, the improvement which comprises heating the condensates of said multi-stage evaporator by means of a fluid issuing from said evaporator system to form a hot condensate and bringing said hot condensate issuing from said evaporator system into indirect heat exchange with air to form said hot air, said hot air being used to dry said condensed concentrate product.

2. The method according to claim 1, wherein said fluid comprises condensates.

3. The method according to claim 2 wherein, prior to being brought into said heat-exchanger relationship, said heated condensates are admixed with vapour issuing from said evaporator system to form hotter condensates.

4. The method according to any of claims 2 and 3, wherein, prior to being brought into said heat exchanger, the ultimately obtained condensates are admixed with hotter condensates.

5. The method according to claim 4, wherein said fluid comprises vapour.

6. The method according to claim 1, wherein, prior to being brought into said heat exchange relationship, said heated condensates are admixed with other condensates which are hotter than or at the same temperature as said heated condensates.

7. The method according to any of claims 2 and 5, wherein said heating step is carried out either in one of the evaporator stages, or outside said evaporator system.

8. The method according to any of claims 3 and 6, wherein said mixing is made either in one of the evaporator stages, or outside said evaporator system.

9. The method of claim 1 wherein the temperature of the hot air is further increased by bringing it into indirect heat exchange with hot vapor taken from the multi-stage evaporator system.

10. The method of claim 1 wherein the liquid product is a liquid milk product and the powdered product is a powdered milk product.