Method and apparatus to produce fatty acids from methyl esters throughout non-catalytic process
An autocatalytic process for producing fatty acids from fatty acids methyl esters with an overall conversion higher than 90% which includes multiple hydrolysis reactions in series, in purely thermal conditions, with intermediate separation of phases after each hydrolysis reaction and before the subsequent, operating in excess of water, in order to separate the methanol/water phases from the equilibrium phase and favor the formation of fatty acids product.
1. An autocatalytic process for producing fatty acids from fatty acids methyl esters in a number of reactor units and a number of Vapor/Liquid/Liquid separators, wherein the process has an overall conversion higher than 90%, the process comprising:
multiple hydrolysis reactions in series, in purely thermal conditions;
intermediate separation of phases after each hydrolysis reaction and before the subsequent, operating in excess of water;
formation of fatty acids product with achievement of an equilibrium phase; and
separation of the methanol/water phases from the equilibrium phase in order to favor the formation of fatty acids product,
wherein a ratio by weight water/methyl ester in each hydrolysis reaction is keeping in the range of 0.4-1.5 and wherein the number of reactors and the number of Vapor/Liquid/Liquid separators are at least three.
2. The autocatalytic process according to claim 1 wherein the ratio by weight water/methyl ester in each hydrolysis reaction is equal to 0.9.
3. The autocatalytic process for producing fatty acids from fatty acids methyl esters with an overall conversion higher than 90% according to claim 1 , further comprising integrating with the hydrolysis reaction process a methanol rectification step to produce pure methanol and recover the excess of water to be recirculated back to the reaction unit.
4. The autocatalytic process for producing fatty acids from fatty acids methyl esters with an overall conversion higher than 90% according to claim 1 , further comprising operating a distillation of an organic phase containing C8-C10 fatty acids out coming from a last separator.
5. The autocatalytic process for producing fatty acids from fatty acids methyl esters with an overall conversion higher than 90% according to claim 1 , further comprising:
a) carrying out a hydrolysis reaction of a mixture of C8-C10 methyl esters, under stirring conditions, in a sealed high pressure stainless steel reactor (R1) at a temperatures ranging from 100 and 350° C., maintaining constant in the range of 0.4-1.5 by weight a C8-C10 methyl esters/water ratio;
separating aqueous and organic phase, containing mainly methyl esters, fatty acids and a part of methanol, through a first Vapor/Liquid/Liquid separator (S1);
b) using the organic phase of a) as charge for a second hydrolysis step, in a consecutive hydrolyzing reactor (R2), adding a quantity of water to the sample to keep the ratio by weight water/methyl ester C8-C10 in the range of 0.4-1.5;
separating aqueous and organic phase through a second Vapor/Liquid/Liquid separator (S2);
c) using the organic phase of b) as charge for a third hydrolysis step, in a consecutive hydrolyzing reactor (R3), adding a quantity of water to the sample to keep the ratio by weight water/methyl ester C8-C10 in the range of 0.4-1.5;
separating aqueous and organic phase through a third Vapor/Liquid/liquid separator (S3).
6. The autocatalytic process for producing fatty acids from fatty acids methyl esters with an overall conversion higher than 90% according to claim 5 wherein the ratio by weight water/methyl ester in each of the three hydrolysis steps is equal to 0.9.
7. The autocatalytic process for producing fatty acids from fatty acids methyl esters with an overall conversion higher than 90% according to claim 5 wherein the step c) is repeated “n” times.
8. The autocatalytic process for producing fatty acids from fatty acids methyl esters with an overall conversion higher than 90% according to claim 5 , further comprising carrying out a distillation of the organic phases containing C8-C10 fatty acids out coming from a last separator.
9. The autocatalytic process according to claim 1 where hydrolysis reaction temperatures have been selected in the range 130-300° C.
10. The autocatalytic process according to claim 1 where temperatures of phases after the separation reaction have been selected in the range 50-150° C.
11. The autocatalytic process according to claim 1 where hydrolysis reaction pressures have been selected in the range 10-100 Bar.g.
12. The autocatalytic process according to claim 1 where distillation pressures of produced fatty acids have been selected in the range 0-2000 mBar.a.
13. The autocatalytic process according to claim 1 , wherein a light cut obtained by distillation, being a mixture of not reacted C8-10 methyl-esters, is recycled to the reaction steps.
14. The autocatalytic process according to claim 1 , wherein an achieved purity of C8-10 Fatty acids is higher than 99% w/w.
15. An apparatus as defined for the process according to claim 1 for producing fatty acids from fatty acids methyl esters with an overall conversion higher than 90%, the apparatus comprising a plurality of hydrolysis reactors in series to carry out the hydrolysis of fatty acids methyl esters auto catalytically, in purely thermal conditions, wherein each hydrolysis reactor is immediately followed by Liquid vapor separators in order to separate, after each hydrolysis reaction step, aqueous phase, that is discharged, and organic phase, that is fed as reactant in the subsequent hydrolysis reactor, to increase the amount of fatty acids in the solution.
16. The apparatus for producing fatty acids from fatty acids methyl esters with an overall conversion higher than 90% according to claim 15 , further comprising a distillation column to carry out a liquid/liquid separation of organic phase coming out from the a last separator.
17. The apparatus for producing fatty acids from fatty acids methyl esters according to claim 16 wherein the distillation column is under vacuum at a total pressure in the range 0-0.5 bar.
18. The apparatus for producing fatty acids from fatty acids methyl esters according to claim 16 wherein the distillation column is under vacuum at a total pressure of 0.02 bar.
19. The apparatus of claim 15 , wherein the hydrolysis reaction units are integrated with at least a methanol rectification column to produce pure methanol and recover the excess of water to be recirculated back to the reaction units.
20. The apparatus of claim 15 comprising means to select a hydrolysis reaction temperature and a separation temperature.
21. The apparatus of claim 15 wherein the hydrolysis reactor is a sealed high pressure stainless steel reactor.
22. The autocatalytic process according to claim 9 , wherein a hydrolysis reaction temperatures are in a range of 150-250° C.
23. The autocatalytic process according to claim 10 , wherein a temperatures of phases after the separation reaction are in a range of 80-110° C.
24. The autocatalytic process according to claim 11 , wherein a hydrolysis reaction pressures are in a range of 40-60 Bar.g.
25. The autocatalytic process according to claim 12 , wherein a distillation pressures of produced fatty acids are in a range of 50-400 mBar.a.
26. The autocatalytic process according to claim 14 , wherein an achieved purity of C8-10 Fatty acids is higher than 99.5% w/w.