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US4018819A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the manufacture of 2-chloroethane-phosphonic acid

Assignee: Hoechst AG
•
Filing: 1975-08-19
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Granted: 1977-04-19
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Expires: 1995-08-19
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Abstract

Abstract An improved process for the manufacture of 2-chloroethane phosphonic acid in which 2-chloroethane phosphonic acid bis(2-chloroethyl)-ester is heated with excess hydrogen chloride in the presence of 0.1 to 31% by weight of water at temperatures above 100° C under pressure, the 1,2-dichloroethane formed during the reaction is continuously or discontinuously distilled off and the decrease in pressure is compensated by adding gaseous hydrogen chloride.

Inventors

  • 👤 Karl Rehn
  • 👤 Otto Schaffner
  • 👤 Gerhard Stahler

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 20:16
CPC Classifications
C; C07; C07F; C07F9/00; C07F9/02; C07F9/28; C07F9/38; C07F9/3804; C07F9/3808

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 78 words
In a process for the manufacture of 2-chloroethane-phosphonic acid by the hydrolytic cleavage of 2-chloroethane-phosphonic acid-bis(2-chloroethyl) ester by contacting said ester with hydrogen chloride in the presence of 0.1 to 31 percent of water, by weight of said ester, at a temperature above 100° C. and under an elevated pressure and maintaining an elevated pressure during the reaction by adding gaseous hydrogen chloride, the improvement which comprises distilling off during the reaction the 1,2-dichloroethane formed by the reaction.
Claim 2
Dependent Claim 78 words
In a process for the manufacture of 2-chloroethane-phosphonic acid by the hydrolytic cleavage of 2-chloroethane-phosphonic acid-bis(2-chloroethyl) ester by contacting said ester with hydrogen chloride in the presence of 0.1 to 31 percent of water, by weight of said ester, at a temperature above 100° C. and under an elevated pressure and maintaining an elevated pressure during the reaction by adding gaseous hydrogen chloride, the improvement which comprises distilling off during the reaction the 1,2-dichloroethane formed by the reaction.
Claim 3
Dependent Claim 23 words
The process of claim 1, wherein hydrochloric acid having a concentration of from 30 to 38% by weight is used for the cleavage.
Claim 4
Dependent Claim 19 words
The process of claim 1, wherein a pressure of from 1 to 10 atmospheres gauge is maintained during hydrolysis.
Claim 5
Dependent Claim 14 words
The process of claim 3, wherein the pressure is 3 to 6 atmospheres gauge.
Claim 6
Dependent Claim 20 words
The process of claim 1, wherein the hydrolysis is carried out at a temperature of from 110° to 190° C.
Claim 7
Dependent Claim 12 words
The process as in claim 1, wherein 1,2-dichloroethane is distilled off discontinuously.
Claim 8
Dependent Claim 12 words
The process as in claim 1, wherein 1,2-dichloroethane is distilled off continuously.

References Cited (Backward Citations)

FR1565742A Cited
US3787486A Cited
US3808265A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-04-18 1980-10-18 1981-04-19 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-04-18 1984-10-18 1985-04-19 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-04-18 1988-10-18 1989-04-19 $7700.00 Window Closed / Lapsed

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