Method for inhibiting polymerization during the recovery and purification of unsaturated mononitriles
AssigneeBP Corporation North America Inc.
InventorsBruce I. Rosen, Bruce E. Firth
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AssigneeBP Corporation North America Inc.
InventorsBruce I. Rosen, Bruce E. Firth
Estimating the term…
Economical processes are disclosed for recovery and refining of valuable nitrogen-containing organic compounds formed by catalytic oxidation of least one feed compound selected from the group consisting of propane, propylene, isobutane and isobutylene in the presence of ammonia to produce a gaseous. Processes of the invention include quenching the gaseous reactor effluent with an aqueous quench liquid; forming an aqueous solution comprising the corresponding unsaturated mononitrile, hydrogen cyanide and other organic co-products; and using an integrated sequence of distillations and phase separations to recover for recycle of a useful aqueous liquid, and obtain the desired nitrogen-containing products. According to the invention aqueous solutions are fractionated in an integrated system of multi-stage columns while an effective polymerization inhibiting amount of at least one member of a preselected class of p-phenylenediamine compounds is maintained therein.
A process for manufacturing an unsaturated mononitrile which process comprises:
A process for recovery of valuable nitrogen-containing organic compounds formed by catalytic ammoxidation of propane, propylene or isobutylene with ammonia and a gaseous source of dioxygen which process comprises:
A process for recovery of valuable nitrogen-containing organic compounds formed by catalytic ammoxidation of propylene and/or propane with ammonia and a gaseous source of dioxygen which process comprises:
19 The process according to claim 17 wherein the phenylenediamine compounds are members of a group consisting of N,N′-di-sec-propyl-p-phenylenediamine, N,N′-di-sec-butyl-p-phenylenediamine, N,N′-di-isobutyl-p-phenylenediamine, and N,N′-di-tert-butyl-p-phenylenediamine.
The process according to claim 19 wherein the compound is N,N′-di-sec-butyl-p-phenylenediamine.
A process for recovery of valuable nitrogen-containing organic compounds formed by catalytic ammoxidation of propylene or propane with ammonia and a gaseous source of dioxygen which process comprises:
23 The process according to claim 21 wherein the phenylenediamine compounds are members of a group consisting of N,N′-di-sec-propyl-p-phenylenediamine, N,N′-di-sec-butyl-p-phenylenediamine, N,N′-di-isobutyl-p-phenylenediamine, and N,N′-di-tert-butyl-p-phenylenediamine.
The process according to claim 23 wherein the compound is N,N′-di-sec-butyl-p-phenylenediamine.
A process for recovery of valuable nitrogen-containing organic compounds formed by catalytic ammoxidation of isobutylene or isobutane with ammonia and a gaseous source of dioxygen which process comprises:
26 The process according to claim 25 wherein the phenylenediamine compounds are members of a group consisting of N,N′-di-sec-propyl-p-phenylenediamine, N,N′-di-sec-butyl-p-phenylenediamine, N,N′-di-isobutyl-p-phenylenediamine, and N,N′-di-tert-butyl-p-phenylenediamine.
The process according to claim 26 wherein the compound is N,N′-di-sec-butyl-p-phenylenediamine.
A process for recovery of valuable nitrogen-containing organic compounds which process comprises:
29 The process according to claim 28 wherein the phenylenediamine compounds are members of a group consisting of N,N′-di-sec-propyl-p-phenylenediamine, N,N′-di-sec-butyl-p-phenylenediamine, N,N′-di-isobutyl-p-phenylenediamine, and N,N′-di-tert-butyl-p-phenylenediamine.
The process according to claim 29 wherein the compound is N,N′-di-sec-butyl-p-phenylenediamine.
Dependencies are inferred from the claim text.