CO5700809A2 - PROCESS FOR THE PRODUCTION OF CHLORINE DIOXIDE - Google Patents

PROCESS FOR THE PRODUCTION OF CHLORINE DIOXIDE

Info

Publication number
CO5700809A2
CO5700809A2 CO06081217A CO06081217A CO5700809A2 CO 5700809 A2 CO5700809 A2 CO 5700809A2 CO 06081217 A CO06081217 A CO 06081217A CO 06081217 A CO06081217 A CO 06081217A CO 5700809 A2 CO5700809 A2 CO 5700809A2
Authority
CO
Colombia
Prior art keywords
chlorine dioxide
reactor
absorption tower
acid
alkali metal
Prior art date
Application number
CO06081217A
Other languages
Spanish (es)
Inventor
Gary Charles
Michael Burke
Original Assignee
Akzo Nobel Nv
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Akzo Nobel Nv filed Critical Akzo Nobel Nv
Publication of CO5700809A2 publication Critical patent/CO5700809A2/en

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J3/00Processes of utilising sub-atmospheric or super-atmospheric pressure to effect chemical or physical change of matter; Apparatus therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24Stationary reactors without moving elements inside
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B11/00Oxides or oxyacids of halogens; Salts thereof
    • C01B11/02Oxides of chlorine

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Treating Waste Gases (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

1.- Un proceso para producir continuamente dióxido de cloro comprende las etapas de:alimentar continuamente un reactor con ácido, un agente reductor y un clorato de metal álcali; hacer reaccionar el clorato de metal álcali con el ácido y el agente de reducción para formar un vapor de producto que contiene dióxido de cloro y la sal de metal álcali de ácido.; y, llevar dicho vapor de producto del reactor a una torre de absorción, en donde esta se conecta con un flujo de agua para formar una solución acuosa que contiene dióxido de cloro .2.- Un proceso como se reivindicó en la reivindicación 1, en donde la solución acuosa que contiene dióxido de cloro tiene una concentración de este de aproximadamente 4 a aproximadamente 12 g/l.3.- Un proceso como se reivindica en cualquiera de las reivindicaciones 1 a 2, en donde la concentración de CIO2 en la solución acuosa se mantiene independiente y substancialmente constante de el índice de producción de dióxido de cloro al ajustar el flujo de agua a la torre de absorción.4.- Un proceso como se reivindica en cualquiera de las reivindicaciones 1 a 3, en donde el gas no absorbido de la torre de absorción se retira mediante una tobera, creando una presión subatmosférica en el reactor y la torre de absorción.5.- Un proceso como se reivindica en cualquiera de las reivindicaciones 1 a 4, en donde el reactor se opera en una presión de aproximadamente 30 a aproximadamente 100 kPa.1. A process for continuously producing chlorine dioxide comprises the steps of: continuously feeding a reactor with acid, a reducing agent and an alkali metal chlorate; react the alkali metal chlorate with the acid and the reducing agent to form a product vapor containing chlorine dioxide and the alkali metal salt of acid .; and, taking said product vapor from the reactor to an absorption tower, where it is connected to a water flow to form an aqueous solution containing chlorine dioxide. 2. A process as claimed in claim 1, in wherein the aqueous solution containing chlorine dioxide has a concentration of this from about 4 to about 12 g / l.3.- A process as claimed in any one of claims 1 to 2, wherein the concentration of CIO2 in the solution The water remains independent and substantially constant of the index of production of chlorine dioxide by adjusting the flow of water to the absorption tower. 4. A process as claimed in any one of claims 1 to 3, wherein the gas does not absorbed from the absorption tower is removed by a nozzle, creating a subatmospheric pressure in the reactor and the absorption tower. 5. A process as claimed in any one of claims 1 to 4, in where the reactor is operated at a pressure of about 30 to about 100 kPa.

CO06081217A 2004-02-23 2006-08-16 PROCESS FOR THE PRODUCTION OF CHLORINE DIOXIDE CO5700809A2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US54619904P 2004-02-23 2004-02-23
EP04445030 2004-03-12

Publications (1)

Publication Number Publication Date
CO5700809A2 true CO5700809A2 (en) 2006-11-30

Family

ID=34889042

Family Applications (1)

Application Number Title Priority Date Filing Date
CO06081217A CO5700809A2 (en) 2004-02-23 2006-08-16 PROCESS FOR THE PRODUCTION OF CHLORINE DIOXIDE

Country Status (4)

Country Link
CO (1) CO5700809A2 (en)
MY (1) MY140635A (en)
PE (1) PE20060034A1 (en)
TW (1) TWI342865B (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11535541B2 (en) * 2017-02-27 2022-12-27 Ecolab Usa Inc. Method for onsite production of chlorine dioxide
TWI750356B (en) 2017-08-17 2021-12-21 美商藝康美國公司 Low risk chlorine dioxide onsite generation system
US11970393B2 (en) 2018-07-05 2024-04-30 Ecolab Usa Inc. Decomposition mediation in chlorine dioxide generation systems through sound detection and control

Also Published As

Publication number Publication date
TW200535088A (en) 2005-11-01
MY140635A (en) 2010-01-15
TWI342865B (en) 2011-06-01
PE20060034A1 (en) 2006-04-12

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Legal Events

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