Abstract Disclosed is a process and apparatus for purifying and regenerating urea solutions which have been contaminated with biuret and triuret and the like during the use of the urea solutions such as in dewaxing processes. The contaminated urea solution is first contacted with ammonia in gaseous or liquid form and about one to ten percent of the ammonia is absorbed into the contaminated solution. The contaminated solution and absorbed ammonia are reacted in a reactor with heating for a period of time sufficient to complete the reaction of biuret and triuret to produce urea. The purified product solution may then be returned for further use in dewaxing processes. Excess ammonia and CO 2 formed during the reaction process by the decomposition of urea may optionally be separated from the purified solution and from each other with the separated excess ammonia being returned to the absorber for reuse.
A process for the purification and regeneration of urea solution contaminated by urea conversion products such as biuret, triuret and the like, comprising the steps of contacting the contaminated urea solution with ammonia whereby about 1% to about 10% by weight of ammonia based on the total amount of urea is absorbed, maintaining said contaminated urea solution in contact with ammonia for a period of about 30-240 minutes at a temperature of about 110° to about 170° C. to react the conversion products with the ammonia, separating CO 2 and excess ammonia from said urea solution and separating said CO 2 and excess ammonia from each other, said steps of contacting, maintaining, separating CO 2 and excess ammonia from the urea solution and separating the CO 2 from the excess ammonia being carried out simultaneously.
Claim 2
Dependent Claim
135 words
A process for the purification and regeneration of urea solution contaminated by urea conversion products such as biuret, triuret and the like, comprising the steps of contacting the contaminated urea solution with ammonia whereby about 1% to about 10% by weight of ammonia based on the total amount of urea is absorbed, maintaining said contaminated urea solution in contact with ammonia for a period of about 30-240 minutes at a temperature of about 110° to about 170° C. to react the conversion products with the ammonia, separating CO 2 and excess ammonia from said urea solution and separating said CO 2 and excess ammonia from each other, said steps of contacting, maintaining, separating CO 2 and excess ammonia from the urea solution and separating the CO 2 from the excess ammonia being carried out simultaneously.
Claim 3
Dependent Claim
35 words
The process as set forth in claim 1 further including the step of reusing the separated ammonia as a portion of the ammonia utilized in the step of contacting the contaminated urea solution with ammonia.
Claim 4
Dependent Claim
25 words
The process as set forth in either of claims 1 or 2 wherein said contaminated urea solutions are urea cycling solutions from a dewaxing process.