Process for obtaining oleochemicals with reduced content of by-products
Processes for obtaining fatty acids with reduced content of by-products, wherein unrefined fats or oils are subjected to steam stripping in a counter-current column to produce a bottom fraction of de-acidified fats or oils, a first distillate consisting mainly of fatty acids and glycerides, and a second distillate comprising fatty acids and essentially all unwanted ketones, aldehydes and phenols, and the bottom fraction containing the de-acidified fats or oils is combined with the first distillate containing fatty acids and glycerides.
1. A process for obtaining fatty acids with reduced content of by-products by subjecting unrefined fats or oils to purification, wherein
(a) steam stripping the unrefined fats or oils under vacuum in a counter-current column, wherein the unrefined oils or fats are fed to a top of the column while the stripping steam is led counter-currently from a bottom of the column, to produce
(i) a bottom fraction of de-acidified fats or oils,
(ii) a first distillate consisting essentially of fatty acids and glycerides, and
(iii) a second distillate comprising fatty acids and ketones, aldehydes and phenols; and
(b) combining said bottom fraction (i) containing the de-acidified fats or oils and said first distillate (ii) containing fatty acids and glycerides to provide a combined fraction;
and wherein the unrefined oils or fats are selected from the group consisting of palm oil, palm kernel oil, coconut oil, olive oil, sunflower oil, sailor oil, soy oil, line oil, rape oil, fish oil, lard oil, tallow and their mixtures.
2. A process for obtaining fatty acid alkyl esters with reduced content of by-products by subjecting unrefined fats or oils to purification, the process comprising
(a) steam stripping unrefined fats or oils under vacuum in a counter-current column, wherein the unrefined oils or fats are fed to a top of the column while the stripping steam is led counter-currently from a bottom of the column, to produce
(i) a bottom fraction of de-acidified fats or oils,
(ii) a first distillate consisting essentially of fatty acids and glycerides, and
(iii) a second distillate comprising fatty acids and essentially all unwanted ketones, aldehydes and phenols; and
(b) combining said bottom fraction (i) containing the de-acidified fats or oils and said first distillate (ii) containing fatty acids and glycerides to provide a combined fraction; and
(c) transesterifying said combined fraction with lower C 1 -C 4 alcohols; and wherein the unrefined oils or fats are selected from the group consisting of palm oil, palm kernel oil, coconut oil, olive oil, sunflower oil, sailor oil, soy oil, line oil, rape oil, fish oil, lard oil, tallow and their mixtures.
3. A process for obtaining fatty alcohols with reduced content of by-products by subjecting unrefined fats or oils to purification, the process comprising
(a) steam stripping unrefined fats or oils under vacuum in a counter-current column, wherein the unrefined oils or fats are fed to a top of the column while the stripping steam is led counter-currently from a bottom of the column, to produce
(i) a bottom fraction of de-acidified fats or oils,
(ii) a first distillate consisting essentially of fatty acids and glycerides, and
(iii) a second distillate comprising fatty acids and essentially all unwanted ketones, aldehydes and phenols; and
(b) combining said bottom fraction (i) containing the de-acidified fats or oils and said first distillate (ii) containing fatty acids and glycerides to provide a combined fraction;
(c) transesterifying said combined fraction with lower C 1 -C 4 alcohols to provide transesterification products; and
(d) hydrogenating said transesterification products thus obtained are subjected to hydrogenation
and wherein the unrefined oils or fats are selected from the group consisting of palm oil, palm kernel oil, coconut oil, olive oil, sunflower oil, sailor oil, soy oil, line oil, rape oil, fish oil, lard oil, tallow and their mixtures.
4. Process according to claim 1 , wherein oils of fats showing an acid value of from 1 to 20 are subjected to purification.
5. Process according to claim 1 , wherein the counter-current column contains packings.
6. Process according to claim 1 , wherein the column contains packings above a feed to the column.
7. Process according to claim 1 , wherein the column is run with a small reflux of the first distillate.
8. Process according to claim 1 , wherein the column is operated at a reduced pressure of 2 to 20 mbar.
9. Process according to claim 1 , wherein the column is operated at temperatures of 225 to 280° C.
10. Process according to claim 1 , wherein one or more condensers are operated at temperatures of 70 to 100° C.
11. Process according to claim 1 , wherein at least a part of the second distillate is refluxed and fractionated in a packing section in a top of the column.
12. Process according to claim 1 , wherein the second distillate is no more than 1% b.w. of the total mass of the bottom fraction, first distillate and second distillate.