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US4642397A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for separating isomers of dinitrotoluene

Assignee: Honeywell UOP LLC
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Filing: 1985-10-01
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Granted: 1987-02-10
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Expires: 2005-10-01
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Abstract

Abstract This invention comprises a process for separating 2,4-dinitrotoluene from a feed mixture comprising 2,4-dinitrotoluene and at least one isomer thereof, which process comprises contacting the mixture at adsorption conditions with an adsorbent comprising an X or Y type zeolite cation exchanged with a cation in the group K, Na, Ca, Ba, Li or Mg, thereby selectively adsorbing the 2,4-dinitrotoluene. The remainder of the feed mixture is removed from the adsorbent and the 2,4-dinitrotoluene is recovered by desorption at desorption conditions with a desorbent material comprising a C3to C5 alcohol, a ketone, toluene, an ester or a nitrocompound.

Inventors

  • 👤 Hermann A. Zinnen
  • 👤 Thad S. Franczyk

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 11:14
CPC Classifications
C; C07; C07C; C07C201/00; C07C201/06; C07C201/16

Claims Analysis

Total Claims: 13
Claim 1
Independent Claim 166 words
A process for separating 2,4-dinitrotoluene from a feed mixture comprising 2,4-dinitrotoluene and 2,6-dinitrotoluene, said process comprising contacting said mixture at a temperature within the range from about 20° C. to about 200° C. and at a pressure to maintain liquid phase with an adsorbent comprising an L type zeolite whose cations have been exchanged with K, an X type zeolite whose cations have been exchanged with a cation selected from the group consisting of Na, Ca, Ba and K, or a Y type zeolite whose cations have been exchanged with a cation selected from the group consisting of Ca, Ba, K, Na, Li and Mg thereby selectively adsorbing said 2,4-dinitrotoluene, removing the remainder of said mixture from said adsorbent, and then recovering said 2,4-dinitrotoluene by desorption at a temperature within the range from about 20° C. to about 200° C. and at a pressure to maintain liquid phase with a desorbent material comprising a C 3 to C 5 alcohol, a ketone, an ester, or nitrobenzene.
Claim 2
Dependent Claim 166 words
A process for separating 2,4-dinitrotoluene from a feed mixture comprising 2,4-dinitrotoluene and 2,6-dinitrotoluene, said process comprising contacting said mixture at a temperature within the range from about 20° C. to about 200° C. and at a pressure to maintain liquid phase with an adsorbent comprising an L type zeolite whose cations have been exchanged with K, an X type zeolite whose cations have been exchanged with a cation selected from the group consisting of Na, Ca, Ba and K, or a Y type zeolite whose cations have been exchanged with a cation selected from the group consisting of Ca, Ba, K, Na, Li and Mg thereby selectively adsorbing said 2,4-dinitrotoluene, removing the remainder of said mixture from said adsorbent, and then recovering said 2,4-dinitrotoluene by desorption at a temperature within the range from about 20° C. to about 200° C. and at a pressure to maintain liquid phase with a desorbent material comprising a C 3 to C 5 alcohol, a ketone, an ester, or nitrobenzene.
Claim 3
Dependent Claim 17 words
The process of claim 1 wherein said process is effected with a simulated moving bed flow system.
Claim 4
Dependent Claim 15 words
The process of claim 1 wherein said process is effected with a static bed system.
Claim 5
Dependent Claim 47 words
The process of claim 1 wherein said absorbent is selected from the group consisting of X type zeolites whose cations have been exchanged with Ba and Y type zeolites whose cations have been exchanged with a cation from the group consisting of K, Na, Li and Mg.
Claim 6
Dependent Claim 55 words
The process of claim 1 wherein said adsorbent is selected from the group of X type zeolites whose cations have been exchanged with a cation from the group consisting of Ba and Na and Y type zeolites whose cations have been exchanged with a cation from the group consisting of Ba, Na, Li and K.
Claim 7
Dependent Claim 16 words
The process of claim 1 wherein said desorbent comprises a C 3 to C 5 alcohol.
Claim 8
Dependent Claim 11 words
The process of claim 6 wherein said desorbent additionally contains toluene.
Claim 9
Dependent Claim 27 words
The process of claim 1 wherein said absorbent is an L type zeolite and said desorbent is selected from the group consisting of n-butanol and ethyl acetate.
Claim 10
Dependent Claim 11 words
The process of claim 8 wherein said desorbent additionally contains toluene.
Claim 11
Dependent Claim 18 words
The process of claim 1 wherein said absorbent is an X type zeolite and said desorbent comprises pentanol.
Claim 12
Dependent Claim 11 words
The process of claim 10 wherein said desorbent additionally contains toluene.
Claim 13
Dependent Claim 24 words
The process of claim 1 wherein said absorbent is a Y type zeolite and said desorbent comprises a C 3 to C 5 alcohol.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1990-02-09 1990-08-11 1991-02-10 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1994-02-09 1994-08-11 1995-02-10 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1998-02-09 1998-08-11 1999-02-10 $7700.00 Window Closed / Lapsed

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