The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.
The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.
Patent No.:
Date of Patent:
Jun. 12, 2012
Filed:
Sep. 12, 2007
Helmut Schmidtke, Bensheim, DE;
Oliver Buβmann, Ludwigshafen, DE;
Ralph Versch, Eppelsheim, DE;
Udo Rheude, Otterstadt, DE;
Uwe Leyk, Worms, DE;
Manfred Julius, Limburgerhof, DE;
Martin Rudloff, Gönnheim, DE;
Erhard Henkes, Einhausen, DE;
Helmut Schmidtke, Bensheim, DE;
Oliver Buβmann, Ludwigshafen, DE;
Ralph Versch, Eppelsheim, DE;
Udo Rheude, Otterstadt, DE;
Uwe Leyk, Worms, DE;
Manfred Julius, Limburgerhof, DE;
Martin Rudloff, Gönnheim, DE;
Erhard Henkes, Einhausen, DE;
BASF SE, Ludwigshafen, DE;
Abstract
Process for the continuous fractional distillation of mixtures including morpholine (MO), monoaminodiglycol (ADG), ammonia and water obtained by reaction of diethylene glycol (DEG) with ammonia, which includes separating off ammonia at the top of a first distillation column K10, feeding the bottoms from K10 to a second distillation column K20 in which water and organic products are separated off at the top at a temperature at the top in the range from 45 to 198° C. and a pressure in the range from 0.1 to 15 bar, feeding the bottoms from K20 to a third distillation column K30 in which MO and organic products having a boiling point of <140° C. (1.013 bar) are separated off at the top or at a side offtake and ADG and organic products having a boiling point of >190° C. (1.013 bar) are separated off at the bottom, feeding the MO including stream which is separated off at the top or at a side offtake of the column K30 to a fourth column K40 in which organic products having a boiling point of ≦128° C. (1.013 bar) are separated off at the top and MO and organic products having a boiling point of ≧128° C. (1.013 bar) are separated off at the bottom and the bottoms from K40 are fed to a fifth distillation column K55 in which MO is separated off at the top and organic products having a boiling point of ≧128° C. (1.013 bar) are separated off at the bottom.