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US3760065A Expired / Lapsed US ⏱️ 0.0 years remaining

Production of chlorine dioxide

Assignee: Erco Industries Ltd
•
Filing: 1971-05-28
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Granted: 1973-09-18
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Expires: 1991-05-28
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Abstract

Abstract Chlorine dioxide is produced from two reactors, the first reacting sodium chlorate, sodium chloride and/or hydrogen chloride, and sulphuric acid at an acidity in excess of 4.8N to deposit sodium acid sulphate, and the second reacting sodium chlorate, sodium chloride and/or hydrogen chloride, and a sulphate-ion material which is constituted at least in part by the sodium acid sulphate deposited in the first reaction, at an acidity less than 4.8N to deposit sodium sulphate. In an alternative embodiment, the reaction is carried out in three vessels, the first producing sodium acid sulphate which is used as at least part of the source of acid for a second reactor producing sodium sesquisulfate which in turn is used as at least part of the acid source of the third reactor.

Inventors

  • 👤 W Rapson

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-02 02:07
CPC Classifications
C; C01; C01B; C01B11/00; C01B11/02; C01B11/022; C01B11/023; C01B11/025

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 32 words
The process of claim 1 wherein said first reaction medium and said second reaction medium are maintained at a boiling temperature, and said first and second zones are maintained under reduced pressure.
Claim 2
Dependent Claim 19 words
The process of claim 1 wherein said sulphate ion-containing acidic material in said first reaction medium is sulphuric acid.
Claim 3
Dependent Claim 252 words
A continuous process for the production of chlorine dioxide which comprises continuously feeding sodium chlorate and sodium chloride to a first reaction vessel containing a first aqueous reaction medium having an acidity from 6 to 12 N and comprising sodium chlorate, sodium chloride and sulphuric acid, continuously feeding sulphuric acid to said first reaction vessel, continuously generating chlorine dioxide and chlorine from said first reaction medium, continuously evaporting sufficient water from said first reaction medium to precipitate continuously sodium acid sulphate from said first reaction medium in said first vessel, continuously recovering from said first vessel a gaseous mixture comprising chlorine dioxide, chlorine and evaporated water, continuously recovering said precipitated sodium acid sulphate from said first vessel, feeding at least part of said recovered sodium acid sulphate to a second reaction vessel, said second reaction vessel containing a second aqueous reaction medium comprising sodium chlorate and sodium chloride, said second reaction medium having an acidity of from 2 to 4.8 N, at least a major proportion of said latter acidity being provided by said fed sodium acid sulphate, continuously feeding sodium chlorate and sodium chloride to said second vessel, continuously generating chlorine dioxide and chlorine from said second reaction medium, continuously evaporating sufficient water from said second reaction medium to precipitate continuously anhydrous sodium sulphate from said second reaction medium in said second vessel, continuously removing from said second vessel a gaseous mixture comprising chlorine dioxide, chlorine and evaporated water, and continuously recovering said precipitated anhydrous sodium sulphate from said second vessel.
Claim 4
Dependent Claim 32 words
The process of claim 4 wherein said first reaction medium and said second reaction medium are maintained at a boiling temperature and said first and second vessels are maintained under reduced pressure.
Claim 5
Dependent Claim 22 words
The process of claim 4 wherein an aqueous solution containing sodium chlorate and sodium chloride is fed to said second reaction vessel.
Claim 6
Dependent Claim 26 words
The process of claim 4 wherein an aqueous solution of sodium chlorate and an aqueous solution of sodium chloride are fed separately to said first vessel.
Claim 7
Dependent Claim 26 words
The process of claim 4 wherein an aqueous solution of sodium chlorate and an aqueous solution of sodium chloride are fed separately to said second vessel.
Claim 8
Dependent Claim 20 words
The process of claim 4 wherein dry sodium chlorate and dry sodium chloride are fed to said first reaction vessel.
Claim 9
Dependent Claim 179 words
A process for the production of chlorine dioxide which comprises generating chlorine dioxide and chlorine from a first aqueous reaction medium contained in a first reaction zone, said first aqueous reaction medium comprising sodium chlorate, a chloride selected from sodium chloride, hydrogen chloride and mixtures thereof, and a sulphate ion-containing acidic material, evaporating sufficient water from said first reaction medium and providing an acidity in said first reaction medium to precipitate a sodium acid sulphate from said first reaction zone, recovering said sodium acid sulphate from said first reaction zone, forming a second aqueous reaction medium having an acidity less than 4.8 N in a second reaction zone by feeding said recovered sodium acid sulphate to an aqueous solution containing sodium chlorate and a chloride selected from sodium chloride, hydrogen chloride and mixtures thereof, generating chlorine dioxide and chlorine from said second reaction medium in said second zone, evaporating sufficient water from said second reaction medium to precipitate anhydrous sodium sulphate in said second zone and recovering chlorine dioxide and chlorine generated in said first and second reaction zones.

References Cited (Backward Citations)

CA543589A Cited
US3341288A Cited
GB1056790A Cited
GB1077306A Cited
US3347628A Cited
US3563702A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1976-09-17 1977-03-19 1977-09-18 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1980-09-17 1981-03-19 1981-09-18 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1984-09-17 1985-03-19 1985-09-18 $7700.00 Window Closed / Lapsed

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