Method for recovering di-trimethylolpropane by distillation
View Patent ↗Distillative process for obtaining ditrimethylolpropane from solutions includes separating ditrimethylolpropane from the solution in a first distillation unit into a first tops fraction comprising low-boiling compounds having a lower boiling point than ditrimethylolpropane and a first bottoms fraction; introducing the first bottoms fraction into a second distillation unit having at least 5 theoretical plates, said unit being configured as a thin-film evaporator with a column attachment and drawing off a second tops fraction comprising intermediate-boiling compounds having a lower boiling point than ditrimethylolpropane as well as withdrawing a second bottoms fraction from the second distillation unit and introducing the second bottoms fraction into a third distillation unit having at least 4 theoretical plates, said unit being configured as a thin-film evaporator with a column attachment, such that ditrimethylolpropane is obtained as a third tops fraction and high boilers are removed as a third bottoms fraction.
1. Distillative process for obtaining ditrimethylolpropane from solutions comprising ditrimethylolpropane, consisting of:
(a) separating the solution comprising ditrimethylolpropane in a first distillation unit into a first tops fraction comprising low-boiling compounds having a lower boiling point than ditrimethylolpropane and a bottoms fraction;
(b) introducing the bottoms fraction as obtained after step a) into a second distillation unit having at least 5 theoretical plates, said unit being configured as a thin-film evaporator with a column attachment, and drawing off a second tops fraction comprising intermediate-boiling compounds having a lower boiling point than ditrimethylolpropane, and withdrawing a bottoms fraction; and
(c) introducing the bottoms fraction as obtained after step b) into a third distillation unit having at least 4 theoretical plates, said unit being configured as a thin-film evaporator with a column, attachment, in which ditrimethylolpropane is obtained as a third tops fraction and high boilers are removed as a bottoms fraction.
2. Process according to claim 1 , characterized in that the second distillation unit has at least 8 theoretical plates.
3. Process according to claim 1 , characterized in that, in step b) the column attachment is configured as a column with random packing or column with structured packing.
4. Process according to claim 1 , characterized in that the second distillation unit is operated at a temperature of 210 to 280° C. and at a pressure of 2 to 10 hPa.
5. Process according to claim 1 , characterized in that the second distillation unit is operated with a residence time of 2 to 60 seconds.
6. Process according to claim 1 , characterized in that the third distillation unit has 4 to 20 theoretical plates.
7. Process according to claim 1 , characterized in that, in step c) the column attachment is configured as a column with random packing or column with structured packing.
8. Process according to claim 1 , characterized in that the third distillation unit is operated at a temperature of 240 to 280° C. and at a pressure of 0.2 to 5 hPa.
9. Process according to claim 1 , characterized in that the residence time of the tops fraction in the third distillation unit is 1 to 30 seconds.
10. Process according to claim 1 , characterized in that a solution of ditrimethylolpropane in a polar solvent is separated in the first distillation unit.
11. Process according to claim 10 , characterized in that the content of the polar solvent in the bottoms fraction of the first distillation unit is up to 5000 ppm by weight, based on the bottoms fraction.
12. Process according to claim 11 , characterized in that the content of the polar solvent in the bottoms fraction of the first distillation unit is up to 1000 ppm by weight, based on the bottoms fraction.
13. Process according to claim 10 , characterized in that the polar solvent used is a C 1 -C 5 aliphatic alcohol, a C 2 -C 10 dialkyl ether or water.
14. Process according to claim 3 , characterized in that the second distillation unit is operated at a temperature of 210 to 280° C. and at a pressure of 2 to 10 hPa.
15. Process according to claim 3 , characterized in that the second distillation unit is operated with a residence time of 2 to 60 seconds.
16. Process according to claim 7 , characterized in that the third distillation unit is operated at a temperature of 240 to 280° C. and at a pressure of 0.2 to 5 hPa.
17. Process according to claim 7 , characterized in that the residence time of the tops fraction in the third distillation unit is 1 to 30 seconds.
18. Distillative process for obtaining ditrimethylolpropane from solutions comprising ditrimethylolpropane, consisting of:
(a) producing the solution comprising ditrimethylolpropane from the residues of trimethyl propane with the addition of water and separating the comprising ditrimethylolpropane in a first distillation unit into a first tops fraction comprising low-boiling compounds having a lower boiling point than ditrimethylolpropane and a bottoms fraction;
(b) introducing the bottoms fraction as obtained after step a) into a second distillation unit having at least 5 theoretical plates, said unit being configured as a thin-film evaporator with a column attachment, and drawing off a second tops fraction comprising intermediate-boiling compounds having a lower boiling point than ditrimethylolpropane is, and withdrawing a bottoms fraction; and
(c) introducing the bottoms fraction as obtained after step b) into a third distillation unit having at least 4 theoretical plates, said unit being configured as a thin-film evaporator with a column attachment, in which ditrimethylolpropane is obtained as a third tops fraction and high boilers are removed as a bottoms fraction.
19. Distillative process for obtaining ditrimethylolpropane from solutions comprising ditrimethylolpropane, consisting of:
(a) treating the solution comprising ditrimethylolpropane with an ion exchanger and separating the solution comprising ditrimethylolpropane in a first distillation unit into a first tops fraction comprising low-boiling compounds having a lower boiling point than ditrimethylolpropane and a bottoms fraction;
(b) introducing the bottoms fraction as obtained after step a) into a second distillation unit having at least 5 theoretical plates, said unit being configured as a thin-film evaporator with a column attachment, and drawing off a second tops fraction comprising intermediate-boiling compounds having a lower boiling point than ditrimethylolpropane, and withdrawing a bottoms fraction; and
(c) introducing the bottoms fraction as obtained after step b) into a third distillation unit having at least 4 theoretical plates, said unit being configured as a thin-film evaporator with a column, attachment, in which ditrimethylolpropane is obtained as a third tops fraction and high boilers are removed as a bottoms fraction.
20. Process according to claim 19 , characterized in that the ion exchanger treatment is effected both with a basic and with an acidic ion exchanger in any sequence.