Mixing two immiscible fluids of differing density

Claim 2

A process for mixing and reacting two at least partially immiscible fluids of differing density, one of which is substantially always in a liquid phase, under conditions of substantially equal distribution of said liquids comprising the steps of simultaneously and continuously, but in a sequential manner A. charging the more dense fluid to a first portion of a feed distribution zone, said first portion being located remotely relative to substantially all of the respective end entrance openings of each of a plurality of tubular reaction zones, in a manner such that a substantially uniform velocity profile of each of said plurality of tubular reaction zones in a common chamber, and G. removing said resulting so collected mixture from said chamber.

Claim 3

The process of claim 1 wherein said flowing is in a vertical direction.

Claim 4

The process of claim 2 wherein said flowing is upwardly.

Claim 5

The process of claim 2 wherein said flowing is downwardly.

Claim 6

The process of claim 1 wherein said more dense liquid is water.

Claim 7

The process of claim 1 wherein said less dense liquid is an organic liquid having a molecular weight ranging from about 28 to 200.

Claim 8

The process of claim 2 wherein said organic liquid is nitrile.

Claim 9

The process of claim 4 wherein said nitrile is an alkenyl nitrile.

Claim 10

The process of claim 5 wherein said alkenyl nitrile is acrylonitrile.

Claim 11

The process of claim 1 wherein said more dense liquid and said less dense liquid are so mixed in a weight ratio of more dense liquid to less dense liquid of from about 9:1 to 1:3.

Claim 12

The process of claim 2 wherein said tubular reaction zones each have an average diameter ranging from about 0.4 to 2.6 inches.

Claim 13

In a process for reacting two at least partially immiscible fluids of differing density, one of which is substantially always in a liquid phase, under conditions of substantially equal distribution of said liquids using a plurality of tubular reaction zones wherein a process flow stream comprised of said fluids is subjected to predetermined conditions of temperature, catalysis, pressure and time, the improvements which comprises the steps of simultaneously and continuously, but in a sequential manner: A. charging the more dense fluid to a first portion of a feed distribution zone, said first portion being located remotely relative to the respective end entrance openings of each of said tubular reaction zones, in a manner such that a substantially uniform velocity profile of said more dense fluid is produced transversely across said zone relative to the direction of fluid flow in said feed distribution zone, said feed distribution zone being substantially completely filled with a solid, particulate, inert material having a porosity at least sufficient to permit said more dense fluid to flow therethrough, B. charging the less dense fluid to a second portion of said feed distribution zone, said second portion being located between said first portion and said reaction zone, in a manner such that a substantially uniform velocity profile of said less dense fluid is produced transversely across said zone relative to the direction of fluid flow in said feed distribution zone, C. flowing the resulting mixture of said fluids through said feed distribution zone for a distance at least sufficient to completely and substantially uniformly intermix said respective fluids, D. moving the resulting such intermixture into substantially all of the respective end entrance openings of each of said tubular reaction zones, at a substantially equal flow rate to each of said tubular reaction zones, the weight ratio of such more dense liquid to such less dense liquid in said intermixture as such enters each of said end entrance openings being substantially the same.

Claim 14

In a process for reacting two at least partially immiscible fluids of differing density, one of which is substantially always in a liquid phase, under conditions of substantially equal distribution of said liquids using a plurality of tubular reaction zones wherein a process flow stream comprised of said fluids is subjected to predetermined conditions of temperature, catalysis, pressure and time, the improvements which comprises the steps of simultaneously and continuously, but in a sequential manner: A. charging the more dense fluid to a first portion of a feed distribution zone, said first portion being located remotely relative to the respective end entrance openings of each of said tubular reaction zones, in a manner such that a substantially uniform velocity profile of said more dense fluid is produced transversely across said zone relative to the direction of fluid flow in said feed distribution zone, said feed distribution zone being substantially completely filled with a solid, particulate, inert material having a porosity at least sufficient to permit said more dense fluid to flow therethrough, B. charging the less dense fluid to a second portion of said feed distribution zone, said second portion being located between said first portion and said reaction zone, in a manner such that a substantially uniform velocity profile of said less dense fluid is produced transversely across said zone relative to the direction of fluid flow in said feed distribution zone, C. flowing the resulting mixture of said fluids through said feed distribution zone for a distance at least sufficient to completely and substantially uniformly intermix said respective fluids, D. moving the resulting such intermixture into substantially all of the respective end entrance openings of each of said tubular reaction zones, at a substantially equal flow rate to each of said tubular reaction zones, the weight ratio of such more dense liquid to such less dense liquid in said intermixture as such enters each of said end entrance openings being substantially the same.

Claim 15

The process of claim 9 wherein: A. said tubular reaction zones are each substantially isothermal, and are each maintained at a temperature in the range from about 100° to 300° F., B. the weight ratio of starting acrylonitrile to water in the feed intermixture is between about 0.3 and 3, C. the weight hourly space velocity is between about 0.1 and 10.0 hrs -1 , D. the process pressure is sufficient to maintain substantially liquid phase conditions in both said feed distribution zone and said tubular reaction zones, E. the catalyst particle size is between about 0.01 and 0.49 inches, F. the catalyst has an initial activity between 0.25 and 2.0., G. the catalyst is a Raney copper catalyst.