IP Library Granted Patent US 6,984,749
Granted Patent B2
US 6,984,749 · App. 10/309,962 · Granted Jan 10, 2006

Method for inhibiting polymerization during the recovery and purification of unsaturated mononitriles

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Quick Facts
Patent No.
US 6,984,749
App. No.
10/309,962
Granted
Jan 10, 2006
Kind
B2
Abstract

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.

Claims (14)

1. A process for manufacturing an unsaturated mononitrile which process comprises:

reacting at least one feed compound selected from the group consisting of propane, propylene, isobutane and isobutylene, with ammonia and a source comprising dioxygen in the presence of a catalyst in a reactor to produce a reactor effluent containing the corresponding unsaturated mononitrile;

transferring the reactor effluent containing the unsaturated mononitrile to a quench/absorption section wherein the reactor effluent containing the unsaturated mononitrile is contacted with at least a first aqueous stream to cool the reactor effluent, and thereafter the cool effluent is contacted with at least a second aqueous stream in an absorption column to separate and recover the unsaturated mononitrile in an aqueous solution;

transferring the aqueous solution containing the unsaturated mononitrile to a recovery and purification section where the unsaturated mononitrile is recovered and purified in at least a first distillation column and a second distillation column; and

maintaining within one or more of the distillation columns an effective polymerization inhibiting amount of at least one phenylenediamine compound represented by the formula:

wherein Ph is a phenylene group, and R 1 and R 2 are the same or different and are hydroxyl free organic moieties having about 2 to about 10 carbon atoms with the proviso that neither R 1 nor R 2 is a phenyl group.

2. The process according to claim 1 wherein the effective polymerization inhibiting amount is no less than about 5 parts per million parts of unsaturated mononitrile present in the aqueous solution.

3. The process according to claim 2 which further comprises admixing a liquid source of the phenylenediamine compound with an aqueous solution containing the unsaturated mononitrile which is being transferred into the first distillation column and/or second distillation column.

4. The process according to claim 1 wherein the unsaturated mononitrile is acrylonitrile or methacrylonitrile, and the feed compound is a corresponding olefin selected from the group consisting of propylene and isobutylene.

5. The process according to claim 1 wherein the organic moieties R 1 and R 2 are members of a group consisting of ethyl, propyl, butyl, phenyl, hexyl, heptyl, octyl, nonyl and decyl straight and branched-chain hydrocarbon groups.

6. The process according to claim 1 wherein the phenylenediamine compound is selected from of a group consisting of N,N′-dialkyl-p-phenylenediamine compounds.

7. The process according to claim 1 wherein the unsaturated mononitrile is acrylonitrile, and the feed compounds are members of a group consisting of propane and propylene.

8. The process according to claim 7 wherein the phenylenediamine compound is selected from 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.

9. The process according to claim 8 wherein the compound is N,N′-di-sec-butyl-p-phenylenediamine.

Assignments (4)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 2, 2007
From: BP CORPORATION NORTH AMERICA INC.
To: O&D USA LLC
Reel/Frame 018861/0266 →
CHANGE OF NAME Recorded Feb 2, 2007
From: OND USA LLC
To: INNOVENE USA LLC
Reel/Frame 018898/0119 →
CHANGE OF NAME Recorded Feb 2, 2007
From: INNOVENE USA LLC
To: INEOS USA LLC
Reel/Frame 018904/0384 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 17, 2003
From: ROSEN, BRUCE I.; FIRTH, BRUCE E.
To: STANDARD OIL COMPANY, THE
Reel/Frame 013693/0734 →