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PE20060034A1 - PROCESS FOR THE PRODUCTION OF CHLORINE DIOXIDE - Google Patents

PROCESS FOR THE PRODUCTION OF CHLORINE DIOXIDE

Info

Publication number
PE20060034A1
PE20060034A1 PE2005000185A PE2005000185A PE20060034A1 PE 20060034 A1 PE20060034 A1 PE 20060034A1 PE 2005000185 A PE2005000185 A PE 2005000185A PE 2005000185 A PE2005000185 A PE 2005000185A PE 20060034 A1 PE20060034 A1 PE 20060034A1
Authority
PE
Peru
Prior art keywords
acid
reactor
tower
chlorine dioxide
flow
Prior art date
Application number
PE2005000185A
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 PE20060034A1 publication Critical patent/PE20060034A1/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

DONDE EL PROCESO COMPRENDE CONTINUAMENTE: a) ALIMENTAR A UN REACTOR UN ACIDO, UN AGENTE DE REDUCCION Y UN CLORATO DE METAL ALCALINO; b) HACER REACCIONAR EL CLORATO CON EL ACIDO Y EL AGENTE PARA FORMAR UN FLUJO DE PRODUCTOS QUE CONTIENE DIOXIDO DE CLORO Y SAL DE METAL ALCALINO DEL ACIDO; Y, c) LLEVAR DICHO FLUJO DESDE EL REACTOR A UNA TORRE DE ABSORCION, DONDE ES CONTACTADO CON UN FLUJO DE AGUA PARA FORMAR UNA SOLUCION ACUOSA QUE CONTIENE DIOXIDO DE CLORO EN UNA CONCENTRACION DE 4 A 12 g/L QUE SE MANTIENE CONSTANTE POR AJUSTE DEL FLUJO DE AGUA A LA TORRE, SIENDO RETIRADO DE LA TORRE EL GAS NO ABSORBIDO POR UN EDUCTOR, CREANDO UNA PRESION SUB-ATMOSFERICA EN EL REACTOR Y EN LA TORRE. EL REACTOR OPERA A UNA PRESION ENTRE 30 Y 100 KPa. EL pH DE LA SOLUCION ACUOSA ES DE 0,1 A 1. EL ACIDO ES ACIDO SULFURICO Y EL AGENTE DE REDUCCION ES PEROXIDO DE HIDROGENOWHERE THE PROCESS CONTINUOUSLY INCLUDES: a) FEEDING AN ACID, A REDUCING AGENT AND AN ALKALINE METAL CHLORATE TO A REACTOR; b) MAKE THE CHLORATE REACT WITH THE ACID AND THE AGENT TO FORM A FLOW OF PRODUCTS CONTAINING CHLORINE DIOXIDE AND ALKALINE METAL SALT OF THE ACID; AND, c) BRING SAID FLOW FROM THE REACTOR TO AN ABSORPTION TOWER, WHERE IT IS CONTACTED WITH A WATER FLOW TO FORM AN AQUEOUS SOLUTION CONTAINING CHLORINE DIOXIDE IN A CONCENTRATION OF 4 TO 12 g / L THAT IS KEPT CONSTANT BY ADJUSTMENT FROM THE WATER FLOW TO THE TOWER, THE GAS NOT ABSORBED BY AN EDUCATOR BEING REMOVED FROM THE TOWER, CREATING A SUB-ATMOSPHERIC PRESSURE IN THE REACTOR AND IN THE TOWER. THE REACTOR OPERATES AT A PRESSURE BETWEEN 30 AND 100 KPa. THE pH OF THE AQUEOUS SOLUTION IS 0.1 TO 1. THE ACID IS SULFURIC ACID AND THE REDUCING AGENT IS HYDROGEN PEROXIDE

PE2005000185A 2004-02-23 2005-02-17 PROCESS FOR THE PRODUCTION OF CHLORINE DIOXIDE PE20060034A1 (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
PE20060034A1 true PE20060034A1 (en) 2006-04-12

Family

ID=34889042

Family Applications (1)

Application Number Title Priority Date Filing Date
PE2005000185A PE20060034A1 (en) 2004-02-23 2005-02-17 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
CN110291047A (en) * 2017-02-27 2019-09-27 埃科莱布美国股份有限公司 The method of produced on-site chlorine dioxide
AR111541A1 (en) 2017-08-17 2019-07-24 Ecolab Usa Inc IN SITU GENERATION SYSTEM FOR LOW RISK CHLORINE DIOXIDE
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
TWI342865B (en) 2011-06-01
MY140635A (en) 2010-01-15
CO5700809A2 (en) 2006-11-30

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