Mario Joseph Nappa - Newark DE, US Patricia Cheung - Glen Mills PA, US Karl R. Krause - Kennett Square PA, US Michael A. Sisk - Hockessin DE, US
Assignee:
E. I. DU PONT DE NEMOURS AND COMPANY - Wilmington DE
International Classification:
C07C 17/395
US Classification:
570180
Abstract:
A process is disclosed for reducing the amount of monofluoroacetate. The process involves (a) contacting a hydrofluorocarbon with a reactant basic aqueous solution to produce an organic phase solution containing a hydrofluoroolefin and an aqueous phase solution containing a monofluoroacetate; and (b) heating the aqueous phase solution to an effective temperature to reduce the amount of monofluoroacetate in the aqueous phase solution, wherein fluoride concentration in the aqueous phase solution is substantially high. Another process is disclosed for reducing the amount of monofluoroacetate. The process involves (a) contacting a first batch of hydrofluorocarbon with a first batch of reactant basic aqueous solution to produce a first batch of organic phase solution containing a hydrofluoroolefin and a first batch of aqueous phase solution containing a monofluoroacetate; (b) separating the first batch of organic phase solution from the first batch of aqueous phase solution; (c) mixing a second batch of hydrofluorocarbon and a second batch of reactant basic aqueous solution with the separated first batch of organic phase solution to produce a second batch of organic phase solution containing a hydrofluoroolefin and a second batch of aqueous phase solution containing a monofluoroacetate; (d) combining the first batch of aqueous phase solution with the second batch of aqueous phase solution; and (e) heating the combined aqueous phase solutions to an effective temperature to reduce the amount of monofluoroacetate in the combined aqueous phase solutions, wherein fluoride concentration in the combined aqueous phase solutions is substantially high.
E. I. Du Pont de Nemours and Company - Wilmington DE
International Classification:
C07C 1124
US Classification:
4232453
Abstract:
Process for the conversion of waste gas streams containing volatile carbon compounds to carbon monoxide by contacting the gas stream with an electrically conductive metal or electrically conductive metal oxide catalyst that is heated to reaction temperature by induction heating.
Process For Continuous Hydrogenation Of Adiponitrile
Sourav Kumar Sengupta - Wilmington DE Theodore Augur Koch - Wilmington DE Karl Robert Krause - Orange TX
Assignee:
E. I. de Pont de Nemours and Company - Wilmington DE
International Classification:
C07C20948
US Classification:
564492
Abstract:
A process for continuous hydrogenation of adiponitrile (ADN) to hexamethylene diamine (HMD) and optionally to amninocapronitrile (ACN) involving the catalytic hydrogenation of adiponitrile at relatively low temperature (e. g. , 75. degree. C. ) and pressure (e. g. , 500 psig) using a sponge cobalt catalyst (Raney. RTM. Co) in a reaction medium that is substantially free of caustic. In such a process periodic addition of water controls the production of side reaction products and the periodic addition of ammonium hydroxide rejuvenates the catalyst. Hexamethylene diamine is an important intermediate for the synthesis of polyamides such as Nylon-6,6 and aminocapronitrile is a potential intermediate of Nylon-6.
Mehrdad Mehdizadeh - Wilmington DE Theodore A. Koch - Wilmington DE Karl Robert Krause - Orange TX Sourav Kumar Sengupta - Wilmington DE Benny Earl Blackwell - Newark DE
Assignee:
E.I. du Pont de Nemours and Company - Wilmington DE
International Classification:
C01C 302
US Classification:
423376
Abstract:
This invention relates to improvements in processes and catalysts for elevated temperature, gas phase, catalyzed reactions in general; it is particularly illustrated by reference to the manufacture of hydrogen cyanide.
Apparatus And Process For The Preparation Of Hydrogen Cyanide
Theodore A. Koch - Wilmington DE Karl R. Krause - Wilmington DE Mehrdad Mehdizadeh - Wilmington DE
Assignee:
E. I. Du Pont de Nemours and Company - Wilmington DE
International Classification:
B01J 1908
US Classification:
422186
Abstract:
An apparatus and process for production of HCN from ammonia and a hydrocarbon gas by the use of microwave energy using a single mode microwave reactor.
Theodore A. Koch - Wilmington DE Karl Robert Krause - Orange TX Mehrdad Mehdizadeh - Wilmington DE Sourav Kumar Sengupta - Wilmington DE Benny Earl Blackwell - Newark DE
Assignee:
E. I. du Pont de Nemours and Company - Wilmington DE
International Classification:
H05B 626
US Classification:
219651
Abstract:
An improved induction heated reactor apparatus involving a reaction zone with inlet and outlet and containing an array of electrically conductive catalyst entities (susceptor entities) comprising pellets, rings, or rods containing a core externally coated with a substantially uniform and complete catalyst metal (e. g. , platinum, platinum-iridium alloy, or platinum-rhodium alloy) wrap, coating, or surface impregnated, or containing the catalyst metal as a foam which are inductively heated to produce chemical product from a catalytic reaction. Such an apparatus is particularly useful in the catalytic generation of HCN at elevated temperatures.
Apparatus And Process For The Preparation Of Hydrogen Cyanide
Theodore A. Koch - Wilmington DE Karl R. Krause - Wilmington DE Mehrdad Mehdizadeh - Wilmington DE
Assignee:
E. I. Du Pont de Nemours and Company - Wilmington DE
International Classification:
C01B 300
US Classification:
20415743
Abstract:
An apparatus and process for production of HCN from ammonia and a hydrocarbon gas by the use of microwave energy using a single mode microwave reactor.
- Wilmington DE, US Karl Krause - Kennett Square PA, US
International Classification:
C07C 17/25
Abstract:
A dehydrohalogenation product includes a hydrochlorofluorocarbon mixture of a fluoroolefin of formula RCX═CZQ and a halofluoroalkane of formula RCXYCZQT. R is a perfluorinated alkyl group and X, Z, and Q are independently H or halogen. One of Y and T is H and the other is Cl, Br, or I. About 80% or greater of the hydrochlorofluorocarbon mixture is the fluoroolefin. The dehydrohalogenation product also includes a caustic agent and a solvent. In some embodiments, the dehydrohalogenation product is free of any catalyst, including any phase transfer catalyst.