EP0679411A1 - Procédé de décontamination de matières solides contaminées par des dibenzodioxines et dibenzofuranes polychlorés - Google Patents

Procédé de décontamination de matières solides contaminées par des dibenzodioxines et dibenzofuranes polychlorés Download PDF

Info

Publication number
EP0679411A1
EP0679411A1 EP95102847A EP95102847A EP0679411A1 EP 0679411 A1 EP0679411 A1 EP 0679411A1 EP 95102847 A EP95102847 A EP 95102847A EP 95102847 A EP95102847 A EP 95102847A EP 0679411 A1 EP0679411 A1 EP 0679411A1
Authority
EP
European Patent Office
Prior art keywords
contaminated
hydrogen peroxide
pcdd
pcdf
decontamination
Prior art date
Legal status (The legal status 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 status listed.)
Withdrawn
Application number
EP95102847A
Other languages
German (de)
English (en)
Inventor
Alexander Dr. Möller
Ulrich Schelbert
Manfred Dr. Weck
Hubertus Eickhoff
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Evonik Operations GmbH
Original Assignee
Degussa GmbH
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 Degussa GmbH filed Critical Degussa GmbH
Publication of EP0679411A1 publication Critical patent/EP0679411A1/fr
Withdrawn legal-status Critical Current

Links

Classifications

    • AHUMAN NECESSITIES
    • A62LIFE-SAVING; FIRE-FIGHTING
    • A62DCHEMICAL MEANS FOR EXTINGUISHING FIRES OR FOR COMBATING OR PROTECTING AGAINST HARMFUL CHEMICAL AGENTS; CHEMICAL MATERIALS FOR USE IN BREATHING APPARATUS
    • A62D3/00Processes for making harmful chemical substances harmless or less harmful, by effecting a chemical change in the substances
    • A62D3/30Processes for making harmful chemical substances harmless or less harmful, by effecting a chemical change in the substances by reacting with chemical agents
    • A62D3/38Processes for making harmful chemical substances harmless or less harmful, by effecting a chemical change in the substances by reacting with chemical agents by oxidation; by combustion
    • AHUMAN NECESSITIES
    • A62LIFE-SAVING; FIRE-FIGHTING
    • A62DCHEMICAL MEANS FOR EXTINGUISHING FIRES OR FOR COMBATING OR PROTECTING AGAINST HARMFUL CHEMICAL AGENTS; CHEMICAL MATERIALS FOR USE IN BREATHING APPARATUS
    • A62D2101/00Harmful chemical substances made harmless, or less harmful, by effecting chemical change
    • A62D2101/20Organic substances
    • A62D2101/22Organic substances containing halogen
    • AHUMAN NECESSITIES
    • A62LIFE-SAVING; FIRE-FIGHTING
    • A62DCHEMICAL MEANS FOR EXTINGUISHING FIRES OR FOR COMBATING OR PROTECTING AGAINST HARMFUL CHEMICAL AGENTS; CHEMICAL MATERIALS FOR USE IN BREATHING APPARATUS
    • A62D2101/00Harmful chemical substances made harmless, or less harmful, by effecting chemical change
    • A62D2101/20Organic substances
    • A62D2101/28Organic substances containing oxygen, sulfur, selenium or tellurium, i.e. chalcogen

Definitions

  • the invention is directed to a process for the decontamination of solids contaminated with polychlorinated dibenzodioxins (PCDD) and / or polychlorinated dibenzofurans (PCDF).
  • PCDD polychlorinated dibenzodioxins
  • PCDF polychlorinated dibenzofurans
  • PCDD / PCDF-containing gases are cleaned by passing them over a fixed bed or fluidized bed made of incombustible materials such as silicas, zeolites, silicates, TiO2 or Al2O3 and with Caro's acid or a their salts are brought into contact, whereby the PCDD and PCDF pollutants are oxidatively destroyed.
  • incombustible materials such as silicas, zeolites, silicates, TiO2 or Al2O3
  • Caro's acid or a their salts are brought into contact, whereby the PCDD and PCDF pollutants are oxidatively destroyed.
  • this document gives no suggestion to decontaminate solids contaminated with PCDD / PCDF with oxidizing agents other than Caro's acid.
  • U.S. Patent 4,632,742 teaches a process for decontaminating mineral oils and soils contaminated with polychlorodiphenyls, polychlorodibenzodioxins, and polychlorodibenzofurans. Decontamination is carried out by treating the contaminated material with a reagent composed of (a) a polyalcohol or polyethylene glycol, (b) a base, such as alkali or alkaline earth carbonate, and (c) an oxidizing agent or a free radical source, such as alkali or alkaline earth peroxide. wherein organically bound halogen is converted into inorganic halide.
  • a reagent composed of (a) a polyalcohol or polyethylene glycol, (b) a base, such as alkali or alkaline earth carbonate, and (c) an oxidizing agent or a free radical source, such as alkali or alkaline earth peroxide. wherein organically bound halogen is converted into inorganic
  • the treatment can be carried out at room temperature or elevated temperature and good decontamination can be achieved, it should be regarded as a disadvantage that, in addition to a peroxide, a base and additionally an alcoholic compound must also be present during the decontamination. This makes the decontamination of particulate materials more difficult because the actual decontamination treatment requires an expensive separation of the alcohols and salts.
  • the aforementioned reagent can also be used in such a way that it is applied as a film to a particulate solid support and the liquid to be decontaminated is coated over the coated support is directed.
  • the document does not teach the decontamination of a particulate solid.
  • the object of the present invention is accordingly to provide a process for the direct decontamination of PCDD / PCDF-contaminated solids which can be carried out in a simple manner, the pollutants being oxidatively destroyed under mild conditions.
  • the process should avoid the disadvantages of the previously known processes, such as the use of a number of auxiliaries and their elaborate removal and disposal after the actual decontamination.
  • PCDD polychlorinated dibenzodioxins
  • PCDF polychlorinated dibenzofurans
  • PCDD polychlorinated dibenzodioxins
  • PCDF polychlorinated dibenzofurans
  • the decontamination according to the invention it is possible to largely reduce the content of the polychlorinated dibenzodioxins / dibenzofurans adsorbed on the solid by oxidative degradation thereof; Degradation rates of at least 70%, mostly more than 80% and often more than 90% are generally achieved.
  • PCDD / PCDF residual contents of less than 5 ng / g solids can usually be achieved in accordance with the Hazardous Substances Ordinance (GefStoffV) applicable in the FRG.
  • the initial contents of the contaminated solids can range between a few ng / g solid and a few micrograms / g solid, depending on their origin.
  • PCDD / PCDF contents of the contaminated solids are calculated from the sum of the contents of the following PCDD or PCDF isomers: 2,3,7,8-tetrachlorodibenzodioxin (TCDD); 1,2,3,7,8-penta-CDD; 1,2,3,6,7,8-hexa-CDD; 1,2,3,7,8,9-hexa-CDD; 1,2,3,4,7,8-hexa-CDD; 2,3,7,8-tetrachlorodibenzofuran (TCDF); 2,3,4,7,8-penta-CDF and 1,2,3,6,7,8-hexa-CDF.
  • TCDD 2,3,7,8-tetrachlorodibenzodioxin
  • TCDF 2,3,7,8-penta-CDD
  • 1,2,3,6,7,8-hexa-CDF 1,2,3,6,7,8-hexa-CDF.
  • the decontamination can be carried out either using an aqueous solution containing hydrogen peroxide or using gaseous hydrogen peroxide.
  • the concentration of the aqueous hydrogen peroxide solution can be in a wide range. A 10 to 50% by weight hydrogen peroxide solution is usually preferred.
  • the contacting is usually carried out at a temperature in the range between 10 and 95 ° C., preferably at room temperature to 60 ° C.
  • the treatment can be carried out by pumping the aqueous hydrogen peroxide solution through a bed containing the contaminated solid until the desired degree of decontamination is reached. In many cases it is also sufficient to leave a mixture of the contaminated solid and the aqueous hydrogen peroxide solution in a container and to stir it only if necessary. After draining off the aqueous hydrogen peroxide solution, the solid is washed with water.
  • the solution containing hydrogen peroxide used in the process according to the invention can, in addition to an essentially pure hydrogen peroxide solution, also be an aqueous solution of sodium percarbonate, since sodium percarbonate releases hydrogen peroxide as an H2O2 addition compound immediately after being dissolved in water.
  • an aqueous sodium percarbonate solution if the resulting alkalinity within the scope of Decontamination process does not interfere or even serves for neutralization or in the decontamination of acidic components.
  • this gas mixture is passed through a bed containing the contaminated solid.
  • air containing 0.01 to 1% by volume of hydrogen peroxide is passed through the solid bed.
  • This treatment is usually carried out over a period of several hours. The treatment can be carried out at room temperature or at an elevated temperature.
  • the process according to the invention can be used to decontaminate different solids which contain adsorbed PCDD's and PCDF's without the pollutants being converted from the solid phase into a gaseous phase, but rather being directly oxidatively destroyed almost quantitatively.
  • the process is characterized by extraordinary simplicity, which was not to be expected in view of the usually very difficult to destroy polychlorinated dibenzodioxins and dibenzofurans.
  • apart from hydrogen peroxide or sodium percarbonate no further auxiliaries for decontamination are required.

Landscapes

  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Toxicology (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Business, Economics & Management (AREA)
  • Emergency Management (AREA)
  • Processing Of Solid Wastes (AREA)
  • Fire-Extinguishing Compositions (AREA)
  • Treatment Of Sludge (AREA)
EP95102847A 1994-04-30 1995-03-01 Procédé de décontamination de matières solides contaminées par des dibenzodioxines et dibenzofuranes polychlorés Withdrawn EP0679411A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE4415202 1994-04-30
DE4415202 1994-04-30

Publications (1)

Publication Number Publication Date
EP0679411A1 true EP0679411A1 (fr) 1995-11-02

Family

ID=6516912

Family Applications (1)

Application Number Title Priority Date Filing Date
EP95102847A Withdrawn EP0679411A1 (fr) 1994-04-30 1995-03-01 Procédé de décontamination de matières solides contaminées par des dibenzodioxines et dibenzofuranes polychlorés

Country Status (3)

Country Link
EP (1) EP0679411A1 (fr)
JP (1) JPH081131A (fr)
HU (1) HUT70699A (fr)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1043046A1 (fr) * 1997-12-25 2000-10-11 Chiyoda Corporation Procede de type humide pour rendre inoffensives des dioxines
US6483006B1 (en) 1999-02-16 2002-11-19 Hitachi Zosen Corporation Method of decomposing organochlorine compound
CN116966472A (zh) * 2023-07-28 2023-10-31 南京大学 一种基于限域类芬顿的飞灰高效解毒方法

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006167713A (ja) * 2004-11-19 2006-06-29 Dowa Mining Co Ltd 汚染土壌または汚染地下水の浄化方法

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0228086A2 (fr) * 1985-12-30 1987-07-08 Union Carbide Corporation Procédé pour éliminer les matériaux organiques toxiques des solutions aqueuses diluées
WO1992019364A1 (fr) * 1991-05-07 1992-11-12 Lab S.A. Procede d'epuration de fumees contenant des polluants organiques condensables
EP0546314A1 (fr) * 1991-11-27 1993-06-16 Degussa Ag Procédé pour l'élimination des composés organiques halogénés des gas de fumée
US5248395A (en) * 1989-12-26 1993-09-28 Uop Process for purifying aqueous media
DE4305344A1 (de) * 1993-02-20 1994-08-25 Degussa Verfahren zum Abbau von in Gasen enthaltenen hochtoxischen halogenierten organischen Verbindungen

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0228086A2 (fr) * 1985-12-30 1987-07-08 Union Carbide Corporation Procédé pour éliminer les matériaux organiques toxiques des solutions aqueuses diluées
US5248395A (en) * 1989-12-26 1993-09-28 Uop Process for purifying aqueous media
WO1992019364A1 (fr) * 1991-05-07 1992-11-12 Lab S.A. Procede d'epuration de fumees contenant des polluants organiques condensables
EP0546314A1 (fr) * 1991-11-27 1993-06-16 Degussa Ag Procédé pour l'élimination des composés organiques halogénés des gas de fumée
DE4305344A1 (de) * 1993-02-20 1994-08-25 Degussa Verfahren zum Abbau von in Gasen enthaltenen hochtoxischen halogenierten organischen Verbindungen

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1043046A1 (fr) * 1997-12-25 2000-10-11 Chiyoda Corporation Procede de type humide pour rendre inoffensives des dioxines
EP1043046A4 (fr) * 1997-12-25 2004-11-10 Chiyoda Chem Eng Construct Co Procede de type humide pour rendre inoffensives des dioxines
US6483006B1 (en) 1999-02-16 2002-11-19 Hitachi Zosen Corporation Method of decomposing organochlorine compound
CN116966472A (zh) * 2023-07-28 2023-10-31 南京大学 一种基于限域类芬顿的飞灰高效解毒方法
CN116966472B (zh) * 2023-07-28 2024-03-08 南京大学 一种基于限域类芬顿的飞灰高效解毒方法

Also Published As

Publication number Publication date
HU9501244D0 (en) 1995-06-28
JPH081131A (ja) 1996-01-09
HUT70699A (en) 1995-10-30

Similar Documents

Publication Publication Date Title
EP0666098B1 (fr) Procédé pour la purification de gaz de combustion
EP0169997B1 (fr) Procédé pour la purification de gaz de fumée
EP0447537B1 (fr) Procede de reduction des emissions de produits organiques d'une combustion incomplete
DE4344113A1 (de) Verfahren zur Reinigung von Abgasen der Abfallverbrennung
EP0252521A1 (fr) Procédé pour décomposer les composés polyhalogénés
EP0612555B1 (fr) Procédé pour la dégradation de composés organiques halogénés à haute toxicité contenus dans des gaz
DE4415719A1 (de) Verfahren zur Abgasreinigung
DE4012982A1 (de) Verfahren zur reinigung von gasen und abgasen von anorganischen und organischen schadstoffen
EP0679411A1 (fr) Procédé de décontamination de matières solides contaminées par des dibenzodioxines et dibenzofuranes polychlorés
DE4210055C2 (fr)
DE19801321A1 (de) Verfahren zur Dekontaminierung von mit Quecksilber belasteten Feststoffen
EP0038402B1 (fr) Procédé de préparation de catalyseurs pour l'oxydation de substances organiques au moyen d'ozone
EP1020419B1 (fr) Procédé pour la purification de gaz réducteur
DE4436656C2 (de) Verfahren und Vorrichtung zur Dekontaminierung und Regenerierung von Zeolithen
DE4446375C1 (de) Verfahren zur naßkatalytischen Reinigung von Abwässern
EP0419842B1 (fr) Procédé pour l'élimination de l'eau de contaminants halogénés organiques contenant au moins 5 atomes de carbone
WO1991010499A1 (fr) Procede de suppression des substances organiques en traces dans les gaz de fumee
EP0804271A1 (fr) PROCEDE D'EPURATION DE GAZ DE COMBUSTION AVEC DES CATALYSEURS AU DeNOx A DES TEMPERATURES INFERIEURES A 150o C
DE4414404A1 (de) Verfahren zur Dekontaminierung von mit halogenierten organischen Verbindungen verunreinigten Feststoffen
DE4324085A1 (de) Verfahren zur Zersetzung organischer Halogenverbindungen in staubhaltigen Abgasen
DE10223112A1 (de) Verfahren und Vorrichtung zur Entfernung von organischen Halogenverbindungen aus Wässern
DE4414405C2 (de) Verfahren zur Dekontaminierung von mit halogenierten organischen Verbindungen verunreinigten Kesselaschen und Flugstäuben
EP0919274B1 (fr) Procédé pour la purification de gaz d'échappement des installations de combustion
DE3933480A1 (de) Verfahren zur verringerung der emission von organischen produkten unvollstaendiger verbrennung
DE4327691A1 (de) Verwendung von gebrauchten Katalysatoren der NO¶x¶-Entfernung zur Verringerung der Emission von chlororganischen Produkten unvollständiger Verbrennung

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AT BE CH DE DK ES FR GB IT LI NL PT SE

17P Request for examination filed

Effective date: 19951114

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE APPLICATION HAS BEEN WITHDRAWN

17Q First examination report despatched

Effective date: 19970617

18W Application withdrawn

Withdrawal date: 19970612