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US4086328A Expired / Lapsed US ⏱️ 0.0 years remaining

Production of chlorine dioxide from buffered reaction media

Assignee: Sterling Canada Inc
•
Filing: 1977-02-22
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Granted: 1978-04-25
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Expires: 1997-02-22
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Abstract

Abstract Chlorine dioxide is produced in a continuous process by reaction of sodium chlorate and hydrochloric acid. The reaction medium is maintained at its boiling point under subatmospheric pressure and the resulting steam is used to dilute the chlorine dioxide and chlorine and remove the same from the reaction zone. Sodium chloride is deposited from the reaction medium in the reaction zone. The reaction medium also contains buffering anions and the actual hydrogen ion concentration of the reaction medium is maintained in the range of about 0.05 to 0.3 normal to maintain an economic production rate for the chlorine dioxide.

Inventors

  • 👤 Richard Swindells

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 11:58
CPC Classifications
C; C01; C01B; C01B11/00; C01B11/02; C01B11/022; C01B11/023; C01B11/025

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 252 words
In a method of producing chlorine dioxide, which comprises: a. establishing in a reaction zone an aqueous reaction medium containing dissolved quantities of sodium chlorate, sodium chloride and hydrochloric acid, said aqueous reaction medium being substantially saturated with sodium chloride, b. continuously feeding hydrochloric acid or hydrogen chloride to said aqueous reaction medium, c. continuously maintaining said reaction medium at its boiling point at the absolute pressure thereon at a temperature below that above which substantial decomposition of chlorine dioxide occurs, d. continuously maintaining said reaction zone under a subatmospheric pressure sufficient to maintain said reaction medium at its boiling point, e. continuously generating chlorine dioxide, chlorine and sodium chloride in said reaction medium, f. continuously removing from said reaction zone a gaseous mixture of chlorine dioxide, chlorine and steam wherein the volume ratio of steam to chlorine dioxide is greater than that below which substantial decomposition of chlorine dioxide occurs, g. continuously depositing said generated sodium chloride from said reaction medium in said reaction zone, h. removing said deposited sodium chloride from said reaction zone, and i. continuously maintaining the volume of liquid in said reaction zone substantially constant, the improvement wherein j. said aqueous reaction medium contains at least one buffering anion selected from the group consisting of divalent and multivalent inorganic anionic species which is introduced to said aqueous reaction medium as a water-soluble salt thereof, and k. the actual hydrogen ion concentration in said reaction medium is maintained in the range of about 0.05 to about 0.03 normal.
Claim 2
Dependent Claim 252 words
In a method of producing chlorine dioxide, which comprises: a. establishing in a reaction zone an aqueous reaction medium containing dissolved quantities of sodium chlorate, sodium chloride and hydrochloric acid, said aqueous reaction medium being substantially saturated with sodium chloride, b. continuously feeding hydrochloric acid or hydrogen chloride to said aqueous reaction medium, c. continuously maintaining said reaction medium at its boiling point at the absolute pressure thereon at a temperature below that above which substantial decomposition of chlorine dioxide occurs, d. continuously maintaining said reaction zone under a subatmospheric pressure sufficient to maintain said reaction medium at its boiling point, e. continuously generating chlorine dioxide, chlorine and sodium chloride in said reaction medium, f. continuously removing from said reaction zone a gaseous mixture of chlorine dioxide, chlorine and steam wherein the volume ratio of steam to chlorine dioxide is greater than that below which substantial decomposition of chlorine dioxide occurs, g. continuously depositing said generated sodium chloride from said reaction medium in said reaction zone, h. removing said deposited sodium chloride from said reaction zone, and i. continuously maintaining the volume of liquid in said reaction zone substantially constant, the improvement wherein j. said aqueous reaction medium contains at least one buffering anion selected from the group consisting of divalent and multivalent inorganic anionic species which is introduced to said aqueous reaction medium as a water-soluble salt thereof, and k. the actual hydrogen ion concentration in said reaction medium is maintained in the range of about 0.05 to about 0.03 normal.
Claim 3
Dependent Claim 20 words
The method of claim 1 wherein said buffering anion is selected from sulphate ions, phosphate ions and monohydrogen phosphate ions.
Claim 4
Dependent Claim 48 words
The method of claim 1 wherein said buffering anion is present in said reaction medium by virtue of an initial charge of a water-soluble salt thereof to said reaction medium in a concentration below the saturation of the reaction medium by said salt at the prevailing reaction conditions.
Claim 5
Dependent Claim 31 words
The method of claim 1 wherein said reaction medium also contains an efficiency improving quantity of at least one catalyst selected from vanadium pentoxide, silver ions, manganese ions and arsenic ions.

References Cited (Backward Citations)

US2863722A Cited
US3101253A Cited
US3563702A Cited
CA913328A Cited
US3929974A Cited
US3829557A Cited
US3793439A Cited
US3895100A Cited
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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-04-24 1981-10-24 1982-04-25 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-04-24 1985-10-24 1986-04-25 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-04-24 1989-10-24 1990-04-25 $7700.00 Window Closed / Lapsed

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