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
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 04:40
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.
References Cited (Backward Citations)
US2985589A
Cited
US3114782A
Cited
US3069470A
Cited
US3201491A
Cited
US3265750A
Cited
US3510423A
Cited
US3558730A
Cited
US3626020A
Cited
US3558732A
Cited
US3668267A
Cited
US3663638A
Cited
US3734974A
Cited
US3864416A
Cited
JPS55149230A
Cited
US4270013A
Cited
US4467126A
Cited
US4480129A
Cited
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 |