Continuous fractionation of triglyceride oils
A continuous process for the dry fractionation of edible oils and fats using one or more crystallisers in series, said process comprising the steps of: (a) providing a molten fat; (b) continuously feeding said molten oil or fat to the first of said one or more crystallisers in series in which the fat is gradually cooled by using heat exchangers containing a cooling medium so that a crystal slurry is formed, each of said one or more crystallisers exhibiting a temperature gradient, the temperature at the point where the molten or partially crystallised fat enters one of the crystallisers being higher than that at the point where the slurry leaves that crystalliser; (c) continuously withdrawing said slurry from the last of said one or more crystallisers; (d) separating said crystal slurry by filtration in a filter cake and a filtrate, wherein said process further comprises the step of at least partially melting fat encrustations deposited on said heat exchangers; and an oil fraction produced by therefrom.
1. A continuous process for the dry fractionation of edible oils and fats using one or more crystallisers in series, said process comprising the steps of:
a) providing a molten fat,
b) continuously feeding said molten oil or fat to the first of said one or more crystallisers in series in which the fat is gradually cooled by using heat exchangers containing a cooling medium so that a crystal slurry is formed, each of said one or more crystallisers exhibiting a temperature gradient, the temperature at the point where the molten or partially crystallised fat enters one of the crystallisers being higher than that at the point where the slurry leaves that crystalliser;
c) continuously withdrawing said slurry from the last of said one or more crystallisers,
d) separating said crystal slurry by filtration in a filter cake and a filtrate, wherein said process further comprises the step of at least partially melting fat encrustations deposited on said heat exchangers.
2. The continuous process according to claim 1 , wherein said continuous process further comprises the step of continuously cooling said molten fat in a cooler to a temperature above the cloud point of said fat before entry of said molten fat into the first of said one or more crystallisers, said cooler comprising at least one heat exchange element.
3. The process according to claim 2 , in which the at least partial melting of fat encrustations in the cooler is effectuated by temporarily interrupting the flow of said cooling medium to the at least one heat exchange element of said cooler or electrically heating the surface of the at least one heat exchange element of said cooler.
4. The process according to claim 3 , in which the temporary interruption of the cooling medium flow is actuated by a temperature difference switch.
5. The process according to claim 3 , in which the temporary interruption of the cooling medium flow is actuated by a programmable timer.
6. The process according to claim 1 , in which said step to at least partially melt fat encrustations comprises electrical heating of the surface of said heat exchangers.
7. The process according to claim 1 , in which a heating medium that is sufficiently hot to at least partially melt fat encrustations that may have been deposited in the heat exchangers used in step b) and at least partial melt fat encrustations on the at least one heat exchange element of said cooler is made to flow through said heat exchangers and/or the at least one heat exchange element of said cooler.
8. The process according to claim 7 , in which said heat exchangers and/or the at least one heat exchange element of said cooler are at least partially drained before a heating medium is made to flow through said heat exchangers and/or the at least one heat exchange element of said cooler.
9. The process according to claim 7 , in which said heating medium is steam.
10. The process according to claim 9 , in which said steam has been generated in the scrubber of a vacuum stripping unit in a nearby refinery complex.
11. The process according to claim 7 , in which said heating medium is heated water.
12. The process according to claim 11 , in which said heated water has been heated by having been used as a cooling medium in a nearby refinery complex.
13. The process according claim 7 , in which the switch from cooling medium to heating medium in said heat exchangers and/or the heat exchange elements of said cooler is actuated by a decrease in the temperature difference between the outgoing and incoming cooling medium.
14. The process according to claim 7 , in which the switch from cooling medium to heating medium is actuated by a programmable timer.
15. The process according to claim 1 , in which the agitators of the one or more crystallisers hardly exert a net vertical force on the crystalliser contents.
16. The process according to claim 1 , in which agitators also acts as a heat exchanger.
17. The process according to claim 1 , in which the construction of the one or more crystallisers promotes a plug flow.
18. The process according to claim 17 in which the one or more crystallisers is compartmented.
19. The process according to claim 1 , in which the stearin cake resulting from the filtration of the final crystal slurry is melted by a heating medium recovered from upstream oil treatments in a nearby refinery complex such as degumming and/or deodorisation.