Isothermal multitube reactors
View Patent ↗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° C. different from a desired reaction temperature.
1. An isothermal multitube reactor comprising a plurality of reactor tubes situated within a shell and suitable for use in a continuous, gas phase, free radical process 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, wherein the reactor comprises a collector configured to accept reactor effluent from the reactor and further configured to minimize backmixing, comprises a temperature reduction mechanism operatively disposed relative to the inlet or feed(s) and wherein at least a portion of at least one reactor tube is definable by a Reynolds number of at least about 2100.
2. The reactor of claim 1 , wherein the reactor comprises a design that minimizes the production of by-products , wherein the reactor design comprises one or more of: i) a design that facilitates heat transfer to and/or from the reactor; ii) a design that facilitates reduced backmixing upon exit from, the reactor, and/or reduced formation of by-products during any backmixing that may occur; iii) a design that optimizes the flow of the reaction components at a boundary between the reaction components and at least a portion of at least one reactor tube wall; and/or iv) a design that facilitates a reduction of the temperature of a reactor effluent to a temperature below which substantial formation of by-products does not occur.
3. The reactor of claim 2 , wherein the reactor design comprises i) a design that facilitates heat transfer to and/or from the reactor; ii) a design that facilitates reduced backmixing upon exit from, the reactor, and/or reduced formation of by-products during any backmixing that may occur; iii) a design that optimizes the flow of the reaction mixture at a boundary between the reaction mixture and at least a portion of at least one reactor tube wall; and iv) a design that facilitates a reduction in temperature of a reactor effluent to a temperature at which substantial formation of by-products does not occur.
4. The reactor of claim 2 , wherein the design facilitating heat transfer comprises the shell being partitioned into at least two sections, so that different temperatures can be maintained within each section.
5. The reactor of claim 2 , wherein the design comprises an inlet header further comprising one or more distributors that provide a substantially even flow of at least one reaction component to a majority of the reactor tubes.
6. The reactor of claim 2 , wherein at least one reactor tube wall is subjected to a pretreatment to minimize surface roughness prior to utilization of the reactor in the desired reaction, with one or more mechanical, electrochemical and/or chemical pretreatments.
7. The reactor of claim 2 , wherein at least a portion of at least one reactor tube wall is coated with a coating that minimizes the deposition of foulants.
8. The reactor of claim 2 , wherein the reactor is operably disposed relative to a source of vibration, sonic or knocking energy.
9. The reactor of claim 2 , wherein the design that facilitates a reduction of the temperature of a reactor effluent comprises a liquid quench function.
10. The reactor of claim 1 , wherein at least a portion of at least one reactor tube wall is coated with a coating that minimizes the deposition of foulants so that the reactor is suitable for use in a continuous, gas phase, free radical process comprising at least one thermally sensitive component.