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US4081520A Expired / Lapsed US ⏱️ 0.0 years remaining

High efficiency production of chlorine dioxide by solvay process

Assignee: Sterling Canada Inc
•
Filing: 1977-02-22
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Granted: 1978-03-28
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Expires: 1997-02-22
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Abstract

Abstract The efficiency of the Solvay chlorine dioxide producing process is enhanced by the use of a high total acid normality and a single vessel generator-evaporator-crystallizer.

Inventors

  • 👤 Richard Swindells
  • 👤 Maurice C. J. Fredette

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-06 08:57
CPC Classifications
C; C01; C01B; C01B11/00; C01B11/02; C01B11/022; C01B11/023

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 211 words
In a process of producing chlorine dioxide by reducing sodium chlorate with methanol in an aqueous reaction medium containing sulphuric acid in the substantial absence of added chloride ions, the improvement comprises: maintaining a single-chambered generator-evaporator-crystallizer apparatus containing said aqueous reaction medium under a subatmospheric pressure, maintaining said reaction medium at its boiling point at a temperature below that above which substantial decomposition of chlorine dioxide occurs to evaporate water from the reaction medium and provide a gaseous mixture containing steam and chlorine dioxide, removing said gaseous mixture from said single-chambered apparatus, recovering an aqueous solution of chlorine dioxide from said removed mixture, maintaining substantially steady state conditions in said reaction medium by continuously feeding said sodium chlorate, methanol and sulphuric acid into said reaction medium to make up chemicals consumed in said reducing step and to maintain a total acid normality in said reaction medium in excess of about 9 normal, maintaining the liquid level in said single-chambered apparatus substantially constant by balancing water fed to the single-chambered apparatus with water removed therefrom, continuously depositing sodium bisulphate or sesquisulphate from said reaction medium after the reaction medium becomes saturated thereby after the initial start up of the process, and removing said deposited sodium bisulphate or sesquisulphate from said single-chambered apparatus.
Claim 2
Dependent Claim 211 words
In a process of producing chlorine dioxide by reducing sodium chlorate with methanol in an aqueous reaction medium containing sulphuric acid in the substantial absence of added chloride ions, the improvement comprises: maintaining a single-chambered generator-evaporator-crystallizer apparatus containing said aqueous reaction medium under a subatmospheric pressure, maintaining said reaction medium at its boiling point at a temperature below that above which substantial decomposition of chlorine dioxide occurs to evaporate water from the reaction medium and provide a gaseous mixture containing steam and chlorine dioxide, removing said gaseous mixture from said single-chambered apparatus, recovering an aqueous solution of chlorine dioxide from said removed mixture, maintaining substantially steady state conditions in said reaction medium by continuously feeding said sodium chlorate, methanol and sulphuric acid into said reaction medium to make up chemicals consumed in said reducing step and to maintain a total acid normality in said reaction medium in excess of about 9 normal, maintaining the liquid level in said single-chambered apparatus substantially constant by balancing water fed to the single-chambered apparatus with water removed therefrom, continuously depositing sodium bisulphate or sesquisulphate from said reaction medium after the reaction medium becomes saturated thereby after the initial start up of the process, and removing said deposited sodium bisulphate or sesquisulphate from said single-chambered apparatus.

References Cited (Backward Citations)

DE378289C Cited
US2605168A Cited
US2881052A Cited
US3933987A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-03-27 1981-09-26 1982-03-28 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-03-27 1985-09-26 1986-03-28 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-03-27 1989-09-26 1990-03-28 $7700.00 Window Closed / Lapsed

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