Process for manufacturing unsaturated mononitriles to improve on-stream time and reduce fouling
The process for manufacturing unsaturated mononitriles, such as acrylonitrile and methacrylonitrile, has been modified to add a partially condensed quench effluent stripper column to remove high boiling organic compounds from the reactor effluent prior to introduction into the extractive distillation recovery column. The high boiling organic compounds are preferably removed after the ammonia in the reactor effluent has been neutralized and the neutralization products have been removed. The targeted high boiling organic compounds are associated with fouling in the recovery section of the plant.
1 . In a process for purifying an unsaturated mononitrile in which an ammoxidation reactor effluent containing an unsaturated mononitrile and high boiling organic compounds is quenched and condensed to provide an aqueous solution: the improvement being that a portion of the aqueous solution containing a substantial amount of the high boiling organic compounds is removed as partially condensed quench effluent and directed to a partially condensed quench effluent stripper column to remove high boiling organic compounds from said process.
2 . The process of claim 1 , wherein said high boiling organic compounds include compounds having a boiling point of 78° C. or higher.
3 . The process of claim 1 , wherein said unsaturated mononitrile is acrylonitrile.
4 . The process of claim 3 , wherein said partially condensed stream includes 2-10 wt. % acrylonitrile, 0.25-1 wt. % hydrogen cyanide, 1-3 wt. % high boiling organic compounds, and the remainder being water to total 100 wt %.
5 . The process of claim 3 , wherein said reactor effluent is quenched using a hot quenching technique.
6 . The process of claim 5 , wherein said partially condensed quench effluent contains 80-95% of the high boiling organic compounds from the aqueous solution.
7 . The process of claim 3 , wherein said partially condensed quench effluent stripper column provides a distillate that contains less than 2 wt. % high boiling organic compounds fed to the partially condensed quench effluent stripper column.
8 . The process of claim 7 , wherein said partially condensed quench effluent stripper column provides a distillate that contains less than 0.5 wt. % high boiling organic compounds fed to the partially condensed quench effluent stripper column.
9 . The process of claim 1 , further comprises an absorber including a partially condensed section operating at 80-155° F. providing the partially condensed quench effluent.
10 . A process for manufacturing an unsaturated mononitrile which process comprises:
a) reacting at least one olefin with ammonia and a source of oxygen in the presence of a catalyst in a reactor to produce a reactor effluent containing the corresponding unsaturated mononitrile and high boiling organic compounds;
b) transferring the reactor effluent to a quencher to cool the effluent resulting in a quench effluent, and thereafter the quench effluent is contacted with an aqueous stream producing an aqueous solution; and
c) transferring a partially condensed quench effluent containing a substantial amount of the high boiling organic compounds from the aqueous solution to a partially condensed quench effluent stripper column to remove high boiling organic compounds from the process.
11 . The process of claim 10 , wherein said high boiling organic compounds include compounds having a boiling point of 78° C. or higher.
12 . The process of claim 10 , wherein said unsaturated mononitrile is acrylonitrile.
13 . The process of claim 12 , wherein said partially condensed quench effluent includes 2-10 wt. % acrylonitrile, 0.25-1 wt. % hydrogen cyanide, 1-3 wt. % high boiling organic compounds, and the remainder being water to total 100 wt %.
14 . The process of claim 12 , wherein said reactor effluent is quenched using a hot quenching technique.
15 . The process of claim 14 , wherein said partially condensed quench effluent contains 80-95% of the high boiling organic compounds from the aqueous solution.
16 . The process of claim 12 , wherein said partially condensed quench effluent stripper column provides a distillate that contains less than 2 wt. % high boiling organic compounds fed to the partially condensed quench effluent stripper column.
17 . The process of claim 16 , wherein said partially condensed quench effluent stripper column provides a distillate that contains less than 0.5 wt. % high boiling organic compounds fed to the partially condensed quench effluent stripper column.
18 . The process of claim 10 , further comprising an absorber including a partially condensed section operating at 80-155° F. to provide the partially condensed quench effluent.
19 . The process of claim 10 , further comprising
d) transferring distillate from the partially condensed quench effluent stripper column to a recovery column.