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US3895050A Expired / Lapsed US ⏱️ 0.0 years remaining

Disposal of waste materials from unsaturated nitrile

Assignee: Badger Co Inc
•
Filing: 1973-11-08
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Granted: 1975-07-15
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Expires: 1993-11-08
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Abstract

Abstract A method of recovering and disposing of waste materials from a plant for manufacturing unsaturated aliphatic nitriles or aromatic nitriles whereby waste water, unreacted ammonia and byproducts such as HCN and acetonitrile are not condensed but remain with the absorber off-gas for ultimate disposal by incineration. The method employs a hydrocarbon solvent to adiabatically quench the reactor effluent and, after removal of polymer by-products, the partially quenched effluent is passed to a hot absorber column where the nitrile product but no ammonia and only some of the HCN are absorbed by the hydrocarbon solvent. The nitrile-solvent mixture is distilled to separately recover the solvent and nitrile product. The solvent is recycled. The hot absorber off-gases are cooled to recover water and then incinerated, with ammonia, HCN, acetonitrile and some vaporized solvent furnishing the necessary fuel values. In a preferred embodiment, solvent in the absorber overhead vapors is recovered by scrubbing with a high boiling oil.

Inventors

  • 👤 Harold R Sheely

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 01:07
CPC Classifications
C; C07; C07C; C07C255/00; C07C253/00; C07C253/32; C07C253/34

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 310 words
A PROCESS FOR TREATING A GASEOUS MIXTURE RESULTING FROM THE CATALYTIC VAPOR PHASE AMMOXIDATION REACTION OF AMMONIA AND OXYGEN WITH A MEMBER OF THE CLASS CONSISTING OF PROPYLENE AND ISOBUTYLENE SAID MIXTURE COMPRISING ITS CORRESPONDING UNSATURATED NITRILE FROM THE CLASS CONSISTING OF ACRYLONITRILE AND METHACRYLONTRILE AMMONIA AND REACTION BY-PRODUCTS COMPRISING HYDROGEN CYANIDE ACETONITRLE ACETONE ACROLEIN BY-PRODUCT POLYMERS AND METHACROLEIN OR PROPIONITRILE SAID PROCESS COMPRISING ADIABATICALLY COOLING SAID GASEOUS MIXTURE IN A QUENCHING CHAMBER BY EVAPORATION OF AT LEAST ONE COMPATIBLE VAPORIZABLE LIQUID MEDIUM SUPPLIED TO SAID QUENCHING CHAMBER SUFFICIENTLY TO CONDENSE AT LEAST SOME OF SAID POLYMER BY-PRODUCTS OF SAID REACTION SAID VAPORIZABLE LIQUID MEDIUM BEING A MEMBER OF THE GROUP CONSISTING OF WATER AND A HYDROCARBON THAT IS A SOLVENT FOR SAID UNSATURATED NITRILE SEPAATING CONDENSED BY-PRODUCT POLYMERS FROM SAID GASEOUS MIXTURE, CONTACTING SAID GASEOUS MIXTURE IN AN ABSORBER CHAMBER WITH A WATER-IMMISCIBLE HYDROCARBON ABSORPTION MEDIUM THAT IS A NONREACTIVE SOLVENT FOR AND HAS A BOILING POINT HIGHER THAN SAID UNSATURATED NITRILE WHEREBY SAID UNSATURATED NITRILE IS ABSORBED BY AND FORMS A SOLUTION WITH SAID ABSORPTION MEDIUM SEPARATING AND RECOVERING SAID SOLUTION AND SAID GASEOUS MIXTURE SCRUBBING THE GASEOUS MIXTURE RECOVERED FROM SAID ABSORBER CHAMBER TO REMOVE HYDROCARBON ABSORPTION MEDIUM FROM SAID MIXTURE WITH A SCRUBBING AGENT THAT HAS A BOILING POINT HIGH THAN THAT OF SAID HYDROCARBON ABSORPTION MEDIUM AND THAT IS NON-REACTIVE WITH SAID SOLVENT AND ALSO WITH PRODUCTS FO SAID REACTION CARRIED OVER IN SAID GASEOUS MIXTURE TREATING SAID SOLUTION TO RECOVER AN OVERHEAD FRACTION COMPRISING BY-PRODUCCTS OF SAID REACTION CARRIED OVER THAT HAVE A BOILING POINT LOWER THAN SAID UNSATURATED NITRILE AND A BOTTOM FRACTION COMPRISING SAID UNSATURATED NITRILE AND SAID HYDROCARBON ABSORPTION MEDIUM TREATING SAID BOTTOMS FRACTION TO SEPARATELY RECOVER SAID UNSATURATED NITRILE AND SAID HYDROCARBON ABSORPTION MEDIUM AND RECYCLING AT LEAST A PORTION OF SAID RECOVERED HYDROCARBON ABSORPTION MEDIUM TO SAID ABSORBER CHAMBER.
Claim 2
Dependent Claim 310 words
A PROCESS FOR TREATING A GASEOUS MIXTURE RESULTING FROM THE CATALYTIC VAPOR PHASE AMMOXIDATION REACTION OF AMMONIA AND OXYGEN WITH A MEMBER OF THE CLASS CONSISTING OF PROPYLENE AND ISOBUTYLENE SAID MIXTURE COMPRISING ITS CORRESPONDING UNSATURATED NITRILE FROM THE CLASS CONSISTING OF ACRYLONITRILE AND METHACRYLONTRILE AMMONIA AND REACTION BY-PRODUCTS COMPRISING HYDROGEN CYANIDE ACETONITRLE ACETONE ACROLEIN BY-PRODUCT POLYMERS AND METHACROLEIN OR PROPIONITRILE SAID PROCESS COMPRISING ADIABATICALLY COOLING SAID GASEOUS MIXTURE IN A QUENCHING CHAMBER BY EVAPORATION OF AT LEAST ONE COMPATIBLE VAPORIZABLE LIQUID MEDIUM SUPPLIED TO SAID QUENCHING CHAMBER SUFFICIENTLY TO CONDENSE AT LEAST SOME OF SAID POLYMER BY-PRODUCTS OF SAID REACTION SAID VAPORIZABLE LIQUID MEDIUM BEING A MEMBER OF THE GROUP CONSISTING OF WATER AND A HYDROCARBON THAT IS A SOLVENT FOR SAID UNSATURATED NITRILE SEPAATING CONDENSED BY-PRODUCT POLYMERS FROM SAID GASEOUS MIXTURE, CONTACTING SAID GASEOUS MIXTURE IN AN ABSORBER CHAMBER WITH A WATER-IMMISCIBLE HYDROCARBON ABSORPTION MEDIUM THAT IS A NONREACTIVE SOLVENT FOR AND HAS A BOILING POINT HIGHER THAN SAID UNSATURATED NITRILE WHEREBY SAID UNSATURATED NITRILE IS ABSORBED BY AND FORMS A SOLUTION WITH SAID ABSORPTION MEDIUM SEPARATING AND RECOVERING SAID SOLUTION AND SAID GASEOUS MIXTURE SCRUBBING THE GASEOUS MIXTURE RECOVERED FROM SAID ABSORBER CHAMBER TO REMOVE HYDROCARBON ABSORPTION MEDIUM FROM SAID MIXTURE WITH A SCRUBBING AGENT THAT HAS A BOILING POINT HIGH THAN THAT OF SAID HYDROCARBON ABSORPTION MEDIUM AND THAT IS NON-REACTIVE WITH SAID SOLVENT AND ALSO WITH PRODUCTS FO SAID REACTION CARRIED OVER IN SAID GASEOUS MIXTURE TREATING SAID SOLUTION TO RECOVER AN OVERHEAD FRACTION COMPRISING BY-PRODUCCTS OF SAID REACTION CARRIED OVER THAT HAVE A BOILING POINT LOWER THAN SAID UNSATURATED NITRILE AND A BOTTOM FRACTION COMPRISING SAID UNSATURATED NITRILE AND SAID HYDROCARBON ABSORPTION MEDIUM TREATING SAID BOTTOMS FRACTION TO SEPARATELY RECOVER SAID UNSATURATED NITRILE AND SAID HYDROCARBON ABSORPTION MEDIUM AND RECYCLING AT LEAST A PORTION OF SAID RECOVERED HYDROCARBON ABSORPTION MEDIUM TO SAID ABSORBER CHAMBER.
Claim 3
Dependent Claim 49 words
A process according to claim 1 wherein said gaseous mixture is cooled in said quenching chamber by evaporation of water, and further including the step of recovering water as a liquid from the gaseous mixture recovered from said quenching chamber and recycling said recovered water to said quenching chamber.
Claim 4
Dependent Claim 55 words
A process according to claim 1 wherein said gaseous mixture is cooled in said quenching chamber by evaporation of water and further including the step of recovering water as a liquid from said gaseous mixture by cooling the gaseous mixture recovered from said absorber chamber, and recycling said recovered liquid water to said quenching chamber.
Claim 5
Dependent Claim 54 words
A process according to claim 1 wherein said gaseous mixture is cooled in said quenching chamber by evaporation of said hydrocarbon absorption medium, and further including the step of recovering said hydrocarbon absorption medium from the gaseous mixture recovered from said quenching chamber and returning said recovered hydrocarbon absorption medium to said quenching chamber.
Claim 6
Dependent Claim 53 words
A process according to claim 1 wherein said vaporizeable liquid medium consists of water and said hydrocarbon absorption medium, and further including the steps of recovering water and hydrocarbon absorption medium from the gaseous mixture recovered from said absorbing chamber and recycling said recovered water and hydrocarbon absorption medium to said absorbing chamber.
Claim 7
Dependent Claim 46 words
A process according to claim 1 further including the steps of separately recovering hydrocarbon absorption medium and water from the gaseous mixture recovered from said absorber chamber, recycling said recovered water to said quenching chamber, and recycling said recovered hydrocarbon absorption medium to said absorber chamber.
Claim 8
Dependent Claim 32 words
A process accordinG to claim 1 wherein said scrubbing agent is a hydrocarbon oil having a boiling point that is at least about 40*F higher than that of said hydrocarbon absorption medium.
Claim 9
Dependent Claim 28 words
A process according to claim 7 wherein said hydrocarbon oil has a boiling point at least about 100*F higher than the boiling point of said hydrocarbon absorption medium.
Claim 10
Dependent Claim 75 words
A process according to claim 1 wherein a mixture of said oil and said hydrocarbon absorption medium is recovered from said scrubbing step, and further including the steps of heating said mixture to obtain an oil fraction and a hydrocarbon absorption medium fraction, recycling at least part of said hydrocarbon absorption medium fraction to said absorber chamber and using at least part of said oil fraction to scrub additional gaseous mixture received from said absorber.
Claim 11
Dependent Claim 12 words
A process according to claim 1 wherein said unsaturated nitrile is acrylonitrile.
Claim 12
Dependent Claim 12 words
A process according to claim 1 wherein said unsaturated nitrile is methacrylonitrile.

References Cited (Backward Citations)

US3201918A Cited
US3535849A Cited
US3661723A Cited
US3636067A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-07-14 1979-01-13 1979-07-15 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-07-14 1983-01-13 1983-07-15 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-07-14 1987-01-13 1987-07-15 $7700.00 Window Closed / Lapsed

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