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US5107040A Expired / Lapsed US ⏱️ 0.0 years remaining

Dehydrohalogenation using magnesium hydroxide

Assignee: Dow Chemical Co
•
Filing: 1991-05-15
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Granted: 1992-04-21
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Expires: 2011-05-15
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Abstract

Abstract A process comprising contacting a solvent, magnesium hydroxide, and a halogenated hydrocarbon at a pressure sufficient to keep the solvent and the halogenated hydrocarbon under liquid conditions, and a temperature greater than 150° C. under conditions suitable to dehydrohalogenate the halogenated hydrocarbon, and recovering the dehydrohalogenated product.

Inventors

  • 👤 Joseph F. Repman
  • 👤 Tarver G. Snedecor, Jr.

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-02 20:22
CPC Classifications
C; C07; C07C; C07C17/00; C07C17/25

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 65 words
A process comprising contacting a solvent, magnesium hydroxide, and a halogenated hydrocarbon selected from the group consisting of chloroethane, 1,1-dichloroethane, 1,2-dichloroethane, 1,1,1-trichloroethane, 1,1,2-trichloroethane, 1,1,1,2-tetrachloroethane, 1,1,2,2-tetrachloroethane, pentachloroethane, and mixtures thereof at a pressure sufficient to keep the solvent and the halogenated hydrocarbon in the liquid phase, and a temperature greater than 150° C. under conditions suitable to dehydrohalogenate the halogenated hydrocarbon, and recovering the dehydrohalogenated product.
Claim 2
Dependent Claim 65 words
A process comprising contacting a solvent, magnesium hydroxide, and a halogenated hydrocarbon selected from the group consisting of chloroethane, 1,1-dichloroethane, 1,2-dichloroethane, 1,1,1-trichloroethane, 1,1,2-trichloroethane, 1,1,1,2-tetrachloroethane, 1,1,2,2-tetrachloroethane, pentachloroethane, and mixtures thereof at a pressure sufficient to keep the solvent and the halogenated hydrocarbon in the liquid phase, and a temperature greater than 150° C. under conditions suitable to dehydrohalogenate the halogenated hydrocarbon, and recovering the dehydrohalogenated product.
Claim 3
Dependent Claim 11 words
The process of claim 1 wherein the halogenated hydrocarbon is 1,1,2-trichloroethane.
Claim 4
Dependent Claim 10 words
The process of claim 1 wherein the solvent is water.
Claim 5
Dependent Claim 16 words
The process of claim 1 wherein the pressure is between about 200 psig and 500 psig.
Claim 6
Dependent Claim 16 words
The process of claim 1 wherein the pressure is between about 250 psig and 400 psig.
Claim 7
Dependent Claim 16 words
The process of claim 1 wherein the temperature is between about 150° C. and 250° C.
Claim 8
Dependent Claim 16 words
The process of claim 1 wherein the temperature is between about 175° C. and 225° C.
Claim 9
Dependent Claim 21 words
The process of claim 1 wherein the molar ratio of magnesium hydroxide to halogenated hydrocarbon is between about 1:1 and 10:1.
Claim 10
Dependent Claim 68 words
A process which comprises contacting water, 1,1,2-trichloroethane, and magnesium hydroxide at a pressure between about 250 psig and 400 psig and a temperature between about 175 ° C. and 225° C., the molar ratio of magnesium hydroxide to 1,1,2-trichloroethane greater than 1:1, the weight percentage of magnesium hydroxide to water between about 10 and 50, under conditions suitable to dehydrohalogenate 1,1,2-trichloroethane, and recovering the vinylidene chloride so formed.
Claim 11
Dependent Claim 68 words
A process which comprises contacting water, 1,1,2-trichloroethane, and magnesium hydroxide at a pressure between about 250 psig and 400 psig and a temperature between about 175 ° C. and 225° C., the molar ratio of magnesium hydroxide to 1,1,2-trichloroethane greater than 1:1, the weight percentage of magnesium hydroxide to water between about 10 and 50, under conditions suitable to dehydrohalogenate 1,1,2-trichloroethane, and recovering the vinylidene chloride so formed.

References Cited (Backward Citations)

US2134102A Cited
US2410541A Cited
US2598646A Cited
US3290398A Cited
US3622641A Cited
US3639493A Cited
US3639492A Cited
US3754044A Cited
US3725486A Cited
US3869520A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1995-04-21 1995-10-21 1996-04-21 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1999-04-21 1999-10-21 2000-04-21 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2003-04-21 2003-10-21 2004-04-21 $7700.00 Window Closed / Lapsed

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