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.