Process for the separation of ortho-chloronitrobenzene

Claim 2

A process for separating ortho-chloronitrobenzene from a feed mixture comprising ortho-chloronitrobenzene and at least one other isomer of chloronitrobenzene, which process comprises contacting said mixture at adsorption conditions with an adsorbent comprising a type X or type Y zeolite containing at the exchangeable cationic sites one or more cations selected from the group consisting of Groups IA, IIA and the transition metals of the Periodic Table of Elements, selectively adsorbing ortho-chloronitrobenzene to the substantial exclusion of the remaining isomers, and thereafter recovering high-purity ortho-chloronitrobenzene.

Claim 3

The process of claim 1 further characterized in that said zeolite is essentially completely exchanged with potassium.

Claim 4

The process of claim 1 further characterized in that said zeolite is essentially completely exchanged with calcium.

Claim 5

The process of claim 1 further characterized in that said zeolite is essentially completely exchanged with cobalt.

Claim 6

The process of claim 1 further characterized in that said feed mixture contains para-chloronitrobenzene, meta-chloronitrobenzene, and ortho-chloronitrobenzene.

Claim 7

The process of claim 1 further characterized in that said feed mixture contains ortho-chloronitrobenzene and one other isomer of chloronitrobenzene.

Claim 8

The process of claim 1 including the step of treating the adsorbent containing said ortho-chloronitrobenzene with a desorbent material to remove said ortho-chloronitrobenzene therefrom as a fluid extract stream.

Claim 9

The process of claim 7 further characterized in that said desorbent material has an average boiling point substantially different from that of the feed mixture.

Claim 10

The process of claim 8 further characterized in that said desorbent material comprises one compound or a mixture of compounds selected from the group consisting of nitrobenzene, toluene and 1-heptanol.

Claim 11

The process of claim 1 further characterized in that said adsorption conditions include a temperature within the range of from about 70° F. to about 450° F. and at a pressure within the range of from about atmospheric to about 500 psig.

Claim 12

The process of claim 10 further characterized in being effected in the liquid phase.

Claim 13

A process for separating ortho-chloronitrobenzene from a feed mixture comprising ortho-chloronitrobenzene and at least one other isomer of chloronitrobenzene which process comprises the steps of: (a) contacting said mixture at adsorption conditions with an adsorbent comprising type X or type Y zeolite containing at the exchangeable cationic sites one or more cations selected from the group consisting of Groups IA, IIA and the transition metals of the Periodic Table of Elements, thereby adsorbing substantially all of said ortho-chloronitrobenzene to the substantial exclusion of said other isomers; (b) withdrawing from the adsorbent a raffinate stream comprising said other isomers; (c) contacting the adsorbent at desorption conditions with a desorbent material having a boiling point substantially different from that of the feed mixture to effect the removal of said ortho-chloronitrobenzene; and, (d) withdrawing from the adsorbent an extract stream comprising said ortho-chloronitrobenzene.

Claim 14

A process for separating ortho-chloronitrobenzene from a feed mixture comprising ortho-chloronitrobenzene and at least one other isomer of chloronitrobenzene which process comprises the steps of: (a) contacting said mixture at adsorption conditions with an adsorbent comprising type X or type Y zeolite containing at the exchangeable cationic sites one or more cations selected from the group consisting of Groups IA, IIA and the transition metals of the Periodic Table of Elements, thereby adsorbing substantially all of said ortho-chloronitrobenzene to the substantial exclusion of said other isomers; (b) withdrawing from the adsorbent a raffinate stream comprising said other isomers; (c) contacting the adsorbent at desorption conditions with a desorbent material having a boiling point substantially different from that of the feed mixture to effect the removal of said ortho-chloronitrobenzene; and, (d) withdrawing from the adsorbent an extract stream comprising said ortho-chloronitrobenzene.

Claim 15

The process of claim 12 further characterized in that said zeolite is essentially completely exchanged with potassium.

Claim 16

The process of claim 12 further characterized in that said zeolite is essentially completely exchanged with calcium.

Claim 17

The process of claim 12 further characterized in that said zeolite is essentially completely exchanged with cobalt.

Claim 18

The process of claim 12 further characterized in that said feed mixture contains para-chloronitrobenzene, meta-chloronitrobenzene, and ortho-chloronitrobenzene.

Claim 19

The process of claim 12 further characterized in that said feed mixture contains ortho-chloronitrobenzene and one other isomer of chloronitrobenzene.

Claim 20

The process of claim 12 further characterized in that said desorbent material comprises one compound or a mixture of compounds selected from the group consisting of nitrobenzene, toluene and 1-heptanol.

Claim 21

The process of claim 12 further characterized in that said adsorption conditions include a temperature within the range of from about 70° F. to about 450° F. and at a pressure within the range of from about atmospheric to about 500 psig.

Claim 22

The process of claim 19 further characterized in being effected in the liquid phase.

Claim 23

A process for separating ortho-chloronitrobenzene from a feed mixture comprising ortho-chloronitrobenzene and at least one other isomer of chloronitrobenzene which process comprises the steps of: (a) maintaining net fluid flow undirectionally through a column of solid adsorbent comprising type X or type Y zeolite containing at exchangeable cationic sites one or more cations selected from the group consisting of Groups IA, IIA and the transition metals of the Periodic Table of Elements, which column contains at least three zones having separate operational functions occurring therein and being serially interconnected with the terminal zones of said column connected to provide a continuous connection of said zones; (b) maintaining an adsorption zone in said column, said zone defined by the adsorbent located between a feed input stream at an upstream boundary of said zone and a raffinate output stream at a downstream boundary of said zone; (c) maintaining a purification zone immediately upstream from said adsorption zone, said purification zone defined by the adsorbent located between an extract output stream at an upstream boundary of said purification zone and said feed input stream at a downstream boundary of said purification zone; (d) maintaining a desorption zone immediately upstream from said purification zone, said desorption zone defined by the adsorbent located between a desorbent input stream at an upstream boundary of said zone and said extract output stream at a downstream boundary of said zone; (e) passing said feed mixture into said adsorption zone at adsorption conditions to effect the selective adsorption of said ortho-chloronitrobenzene by said adsorbent in said adsorption zone and withdrawing a raffinate output stream from said adsorption zone; (f) passing a desorbent material into said desorption zone at desorption conditions to effect the displacement of said ortho-chloronitrobenzene from the adsorbent in said desorption zone; (g) withdrawing an extract output stream comprising said ortho-chloronitrobenzene and desorbent material from said desorption zone; (h) passing at least a portion of said extract output stream to a separation means and therein separating at separation conditions at least a portion of said desorbent material to produce a ortho-chloronitrobenzene recycle stream having a reduced concentration of desorbent material; and (i) periodically advancing through said column of adsorbent in a downstream direction with respect to fluid flow in said adsorption zone the feed input stream, raffinate output stream, desorbent input stream, and extract output stream to effect the shifting of zones through said adsorbent and the production of extract output and raffinate output streams.

Claim 24

A process for separating ortho-chloronitrobenzene from a feed mixture comprising ortho-chloronitrobenzene and at least one other isomer of chloronitrobenzene which process comprises the steps of: (a) maintaining net fluid flow undirectionally through a column of solid adsorbent comprising type X or type Y zeolite containing at exchangeable cationic sites one or more cations selected from the group consisting of Groups IA, IIA and the transition metals of the Periodic Table of Elements, which column contains at least three zones having separate operational functions occurring therein and being serially interconnected with the terminal zones of said column connected to provide a continuous connection of said zones; (b) maintaining an adsorption zone in said column, said zone defined by the adsorbent located between a feed input stream at an upstream boundary of said zone and a raffinate output stream at a downstream boundary of said zone; (c) maintaining a purification zone immediately upstream from said adsorption zone, said purification zone defined by the adsorbent located between an extract output stream at an upstream boundary of said purification zone and said feed input stream at a downstream boundary of said purification zone; (d) maintaining a desorption zone immediately upstream from said purification zone, said desorption zone defined by the adsorbent located between a desorbent input stream at an upstream boundary of said zone and said extract output stream at a downstream boundary of said zone; (e) passing said feed mixture into said adsorption zone at adsorption conditions to effect the selective adsorption of said ortho-chloronitrobenzene by said adsorbent in said adsorption zone and withdrawing a raffinate output stream from said adsorption zone; (f) passing a desorbent material into said desorption zone at desorption conditions to effect the displacement of said ortho-chloronitrobenzene from the adsorbent in said desorption zone; (g) withdrawing an extract output stream comprising said ortho-chloronitrobenzene and desorbent material from said desorption zone; (h) passing at least a portion of said extract output stream to a separation means and therein separating at separation conditions at least a portion of said desorbent material to produce a ortho-chloronitrobenzene recycle stream having a reduced concentration of desorbent material; and (i) periodically advancing through said column of adsorbent in a downstream direction with respect to fluid flow in said adsorption zone the feed input stream, raffinate output stream, desorbent input stream, and extract output stream to effect the shifting of zones through said adsorbent and the production of extract output and raffinate output streams.

Claim 25

The process of claim 21 further characterized in that said zeolite is essentially completely exchanged with potassium.

Claim 26

The process of claim 21 further characterized in that said zeolite is essentially completely exchanged with calcium.

Claim 27

The process of claim 21 further characterized in that said zeolite is essentially completely exchanged with cobalt.

Claim 28

The process of claim 21 further characterized in that said feed mixture contains para-chloronitrobenzene, meta-chloronitrobenzene, and ortho-chloronitrobenzene.

Claim 29

The process of claim 21 further characterized in that said feed mixture contains ortho-chloronitrobenzene and one other isomer of chloronitrobenzene.

Claim 30

The process of claim 21 further characterized in that said desorbent material comprises one compound or a mixture of compounds selected from the group consisting of nitrobenzene, toluene and 1-heptanol.

Claim 31

The process of claim 21 further characterized in that said adsorption include a temperature within the range of from about 70° F. to about 450° F. and at a pressure within the range of from about atmospheric to about 500 psig.

Claim 32

The process of claim 28 further characterized in being effected in the liquid phase.