Dow Global Technolgoies LLC

Blue Cube IP LLC

Heinz Groenewald

Max Markus Tirtowidjojo

Kurt Frederick Hirsekorn

Debashis Chakraborty

Juergen Eiffler

Thomas U Luebbe

Manfred Kokott

Marcus Wobser

William Jack Kruper, Jr

Shirley Shaw Sexton

Peter Wenzel

Hua Bai

Avani Maulik Patel

Bruce D Hook

William J Kruper

Charles William Lipp

William W Fan

Thomas J Parsons

Patrick H Au-Yeung

Christian D Kneupper

Michael D Cloeter

Sascha Noormann

Ranate Patrascu

Holger Meemann

Holger Meeman

Patrick Ho-Sing Au-Yeung

Thomas Ulrich Luebbe

The present invention provides adiabatic plug flow reactors suitable for the production of chlorinated and/or fluorinated propene and higher alkenes from the reaction of chlorinated and/or fluorinated alkanes and chlorinated and/or fluorinated alkenes. The reactors comprise one or more designs that minimize the production of by-products at a desired conversion.

Adiabatic plug flow reactors and processes incorporating the same

The present invention provides continuous, gas phase, free radical processes for the production of chlorinated and/or fluorinated propenes or higher alkenes from the reaction of chlorinated and/or fluorinated alkanes and chlorinated and/or fluorinated alkenes, wherein wherein at least a portion of any intermediate boiler by-products generated by the process are removed from the process.

Processes for the production of hydrofluoroolefins

The present invention provides isothermal multitube reactors suitable for the production of chlorinated and/or fluorinated propene and higher alkenes from the reaction of chlorinated and/or fluorinated alkanes and chlorinated and/or fluorinated alkenes. The reactors utilize a feed mixture inlet temperature at least 20&#xb0; C. different from a desired reaction temperature.

Isothermal multitube reactors

Processes for the production of chlorinated and/or fluorinated propenes and higher alkenes

Isothermal multitube reactors and processes incorporating the same

A process for producing epoxide, the process including contacting an organic phase including at least one halohydrin(s) with at least one aqueous phase including a base in a plug-flow mixer/reactor system to disperse the organic phase in the aqueous phase via a mixing device imparting a power-to-mass ratio of at least 0.2 W/kg to convert at least a portion of the at least one halohydrin to an epoxide.

Process for producing epoxides

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Hammah, Germany

Heinz Groenewald