WO1997030757A1 - Treatment process for contaminated waste - Google Patents

Treatment process for contaminated waste Download PDF

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Publication number
WO1997030757A1
WO1997030757A1 PCT/CA1997/000114 CA9700114W WO9730757A1 WO 1997030757 A1 WO1997030757 A1 WO 1997030757A1 CA 9700114 W CA9700114 W CA 9700114W WO 9730757 A1 WO9730757 A1 WO 9730757A1
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WO
WIPO (PCT)
Prior art keywords
carbon dioxide
waste material
added
waste
ash
Prior art date
Application number
PCT/CA1997/000114
Other languages
French (fr)
Inventor
Rikkert J. Vos
Original Assignee
B.C. Research, Inc.
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 B.C. Research, Inc. filed Critical B.C. Research, Inc.
Priority to AU17152/97A priority Critical patent/AU1715297A/en
Publication of WO1997030757A1 publication Critical patent/WO1997030757A1/en

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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
    • A62D3/33Processes for making harmful chemical substances harmless or less harmful, by effecting a chemical change in the substances by reacting with chemical agents by chemical fixing the harmful substance, e.g. by chelation or complexation
    • 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
    • A62D2101/08Toxic combustion residues, e.g. toxic substances contained in fly ash from waste incineration
    • 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
    • A62D2101/40Inorganic substances
    • A62D2101/43Inorganic substances containing heavy metals, in the bonded or free state

Definitions

  • This invention relates to a process for stabilizing leachable heavy metals in waste material.
  • the invention finds particular application in the stabilization of lead in incinerator ash so that the lead cannot be leached into the environment .
  • the present invention addresses one particular problem, namely the leaching of heavy metals, especially lead, from the ash produced in the incineration of solid wastes.
  • the invention is such that the treated ash does not contain lead that is leachable. This means that the ash can be disposed as a non- hazardous waste or used in, for example, the production of cement and concrete.
  • the present invention provides a process for stabilizing leachable heavy metals contained in a waste material that comprises contacting the waste material with carbon dioxide.
  • the reaction may be carried out in the presence of water.
  • the heavy metal is lead.
  • the waste material is ash, particularly ash produced from a municipal incinerator.
  • the carbon dioxide may be added in gaseous or solid form, the latter as dry ice.
  • the carbon dioxide might also be the carbon dioxide in the air, that is air may be used as a source of carbon dioxide.
  • the process may be carried out at atmospheric pressure but it is desirably carried out in a closed vessel. This permits the use of pressure greater than atmospheric pressure which reduces the reaction time. Pressures up to about 90 pounds per square inch gauge (psig) have been used. Higher pressure may be used to speed the reaction rate.
  • psig pounds per square inch gauge
  • the process may be controlled by monitoring the pH during the addition of the carbon dioxide. Typically, the process results in a decrease in pH from approximately 12 to 11.5 or lower.
  • Figure 1 is a flow diagram showing the stabilizing of fly ash with carbon dioxide.
  • FIG. 1 shows a closed reactor 10 having an inlet 12 for ash and a mixer 14.
  • the reactor 10 may be a batch or continuous reactor.
  • Water is added through an inlet 20. Typically water is added in an amount of about 40 to 65% moisture content.
  • the stabilized ash slurry from the reactor 10 leaves through an outlet 22 and passes to a dewatering unit 24. Water from the dewatering unit 24 is fed back to the reactor 10 via inlet 20.
  • Make-up water is added as desired, through a conduit 26.
  • Sludge from the dewatering unit 24 leaves the unit 24 through outlet 28. This sludge typically contains about 30% moisture and is sent for disposal or use. For example, it may be used as an inert filler in the production of concrete or cement.
  • effluent from the reactor 10 may be fed to a dryer 30.
  • the slurry from the dryer is disposed of in the same way as the effluent from the dewatering unit 24.
  • Carbon dioxide was added at 90 psig in a pressure vessel for tests 1, 2 and 3 and at atmospheric pressure for test 4. The period of reaction was about 0.5 hrs.
  • the quantity of carbon dioxide added ranged from about 8.00% to 14.03% based on the volume of the wet ash. In general the amount of carbon dioxide can be determined by routine experiment as the amount needed to stabilize the lead.

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  • 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)

Abstract

A process for stabilizing leachable heavy metals contained in a waste material. The waste material is contacted with carbon dioxide. The invention is of particular application in the stabilizing of lead, particularly in waste material produced by the combustion of solid waste.

Description

TREATMENT PROCESS FOR CONTAMI ATED WASTE
FIELD OF THE INVENTION
This invention relates to a process for stabilizing leachable heavy metals in waste material. The invention finds particular application in the stabilization of lead in incinerator ash so that the lead cannot be leached into the environment .
DESCRIPTION OF RELATED ART
The incineration of solid wastes, particularly municipal garbage, is finding increasing application worldwide. It has the advantage of reducing the cost of landfill disposal and, of course, saving landfill space. However, incineration has its own problems. It results in air emissions and the production of ash. The ash is a problem in that it contains heavy metals, particularly lead, which can be leached out from any disposal site. There are a number of tests to determine leachability, for example, the United State Environmental Protection Agency has published the Federal Registry, Volume 40, Part 261, Appendix II, Method 1311 entitled Toxicity
Characteristic Leaching Procedure (TCLP) 1993, p.p. 66 to 82. As an example of the Canadian regulations the Province of British Columbia has published Regulation 63/88, O.C. 268/88, Waste Management Act, Special Waste Regulations, February, 1988 (S.W.E.P.) .
Thus, although the use of incineration has undoubtedly been an advantage, there are still problems to be solved and the present invention addresses one particular problem, namely the leaching of heavy metals, especially lead, from the ash produced in the incineration of solid wastes. The invention is such that the treated ash does not contain lead that is leachable. This means that the ash can be disposed as a non- hazardous waste or used in, for example, the production of cement and concrete. SUMMARY OF THE INVENTION
Accordingly, the present invention provides a process for stabilizing leachable heavy metals contained in a waste material that comprises contacting the waste material with carbon dioxide. The reaction may be carried out in the presence of water.
In a preferred embodiment, the heavy metal is lead. In a further preferred embodiment, the waste material is ash, particularly ash produced from a municipal incinerator.
The carbon dioxide may be added in gaseous or solid form, the latter as dry ice. The carbon dioxide might also be the carbon dioxide in the air, that is air may be used as a source of carbon dioxide.
The process may be carried out at atmospheric pressure but it is desirably carried out in a closed vessel. This permits the use of pressure greater than atmospheric pressure which reduces the reaction time. Pressures up to about 90 pounds per square inch gauge (psig) have been used. Higher pressure may be used to speed the reaction rate.
The process may be controlled by monitoring the pH during the addition of the carbon dioxide. Typically, the process results in a decrease in pH from approximately 12 to 11.5 or lower.
BRIEF DESCRIPTION OF THE DRAWINGS
A preferred embodiment of the invention is illustrated in Figure 1, which is a flow diagram showing the stabilizing of fly ash with carbon dioxide. DESCRIPTION OF THE PREFERRED EMBODIMENT
Figure 1 shows a closed reactor 10 having an inlet 12 for ash and a mixer 14. The reactor 10 may be a batch or continuous reactor. There is an inlet 16 to receive carbon dioxide from a carbon dioxide storage tank 18. Water is added through an inlet 20. Typically water is added in an amount of about 40 to 65% moisture content. The stabilized ash slurry from the reactor 10 leaves through an outlet 22 and passes to a dewatering unit 24. Water from the dewatering unit 24 is fed back to the reactor 10 via inlet 20. Make-up water is added as desired, through a conduit 26. Sludge from the dewatering unit 24 leaves the unit 24 through outlet 28. This sludge typically contains about 30% moisture and is sent for disposal or use. For example, it may be used as an inert filler in the production of concrete or cement.
In an alternative, illustrated to the right of Figure 1, effluent from the reactor 10 may be fed to a dryer 30. The slurry from the dryer is disposed of in the same way as the effluent from the dewatering unit 24.
The following example illustrates the invention:
Fly ash obtained from the Greater Vancouver Regional District (GVRD) in Vancouver, British Columbia, failed to pass the British Columbia SWEP test or the USTCLP test.
It was treated with water and carbon dioxide in apparatus as schematically illustrated in Figure 1. Carbon dioxide was added at 90 psig in a pressure vessel for tests 1, 2 and 3 and at atmospheric pressure for test 4. The period of reaction was about 0.5 hrs. The quantity of carbon dioxide added ranged from about 8.00% to 14.03% based on the volume of the wet ash. In general the amount of carbon dioxide can be determined by routine experiment as the amount needed to stabilize the lead.
The following results were achieved:
Figure imgf000006_0001
It is clear from the above results that the process of the present invention has taken an ash unacceptable under the known tests and produced a solid product that easily passes the known tests. Furthermore, the pronounced alkalinity of the untreated ash has changed in the treated ash to about neutral.
Although the present invention has been described in some detail by way of example for purposes of clarity and understanding, it will be apparent that certain changes and modifications may be practised within the scope of the appended claims.

Claims

I CLAIM :
I. A process for stabilizing leachable heavy metals contained in a waste material that comprises contacting the waste material with carbon dioxide.
2. A process as claimed in claim 1 in which the heavy metal is lead.
3. A process as claimed in claim 1 in which the waste material is produced by the combustion of solid waste .
4. A process as claimed in claim 1 in which the carbon dioxide is added as a gas, liquid or solid.
5. A process as claimed in claim 1 in which the carbon dioxide is added diluted with air or supplied from the air.
6. A process as claimed in claim 1 in which water is added.
7. A process as claimed in claim 6 that includes monitoring the pH during the addition of carbon dioxide.
8. A process as claimed in claim 6 including dewatering the treated waste.
9. A process as claimed in claim 8 in which dewatering is carried out by evaporation or filtration.
10. A process as claimed in claim 9 in which the effluent from the dewatering is recycled to be added to the untreated waste material.
II. A process as claimed in claim 1 carried out in an enclosed vessel .
12. A process as claimed in claim 1 in which water is absent from the process.
13. A process as claimed in claim 12 in which pressure and/or heat is applied to increase the stabilization rate.
PCT/CA1997/000114 1996-02-23 1997-02-19 Treatment process for contaminated waste WO1997030757A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AU17152/97A AU1715297A (en) 1996-02-23 1997-02-19 Treatment process for contaminated waste

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US60636996A 1996-02-23 1996-02-23
US08/606,369 1996-02-23

Publications (1)

Publication Number Publication Date
WO1997030757A1 true WO1997030757A1 (en) 1997-08-28

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Country Status (2)

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AU (1) AU1715297A (en)
WO (1) WO1997030757A1 (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2770159A1 (en) * 1997-10-24 1999-04-30 Recupyl Sa Treatment with waste incinerator residues
EP0913172A1 (en) * 1997-10-28 1999-05-06 Deutsche Babcock Anlagen Gmbh Method for treating incineration residues
ES2137071A1 (en) * 1996-03-18 1999-12-01 Vicent Claverie Martin Procedure for the inertization of solid alkaline waste.
WO2002018069A1 (en) * 2000-09-01 2002-03-07 Tech-Wise A/S Process for the treatment of bottom ash from waste incineration plants
JP2015054313A (en) * 2013-09-13 2015-03-23 大阪瓦斯株式会社 Processing method of incineration ash and incineration apparatus

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5462654A (en) * 1977-10-27 1979-05-19 Nippon Kokan Kk <Nkk> Method of treating waste water containing heavy metal
JPS5667572A (en) * 1979-11-07 1981-06-06 Yokohamashi Treatment for solidifying of electric collected dust ash
JPS5730594A (en) * 1980-07-30 1982-02-18 Takuma Co Ltd Disposal of ash sludge from dust incinerator
JPS6365988A (en) * 1986-09-08 1988-03-24 Hitachi Zosen Corp Harmless treatment of ash collected in electrostatic precipitator by utilizing co2 contained in exhaust gas
JPH01284382A (en) * 1988-05-11 1989-11-15 Nkk Corp Treatment of fly ash
EP0538598A1 (en) * 1991-10-25 1993-04-28 AUSTRIAN ENERGY &amp; ENVIRONMENT SGP/WAAGNER-BIRO GmbH Process for converting water soluble heavy metal compounds into water insoluble, or sparingly soluble, compounds
FR2732910A1 (en) * 1995-04-13 1996-10-18 Viafrance Sa Treating cinders from incineration of domestic waste with carbon di:oxide

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5462654A (en) * 1977-10-27 1979-05-19 Nippon Kokan Kk <Nkk> Method of treating waste water containing heavy metal
JPS5667572A (en) * 1979-11-07 1981-06-06 Yokohamashi Treatment for solidifying of electric collected dust ash
JPS5730594A (en) * 1980-07-30 1982-02-18 Takuma Co Ltd Disposal of ash sludge from dust incinerator
JPS6365988A (en) * 1986-09-08 1988-03-24 Hitachi Zosen Corp Harmless treatment of ash collected in electrostatic precipitator by utilizing co2 contained in exhaust gas
JPH01284382A (en) * 1988-05-11 1989-11-15 Nkk Corp Treatment of fly ash
EP0538598A1 (en) * 1991-10-25 1993-04-28 AUSTRIAN ENERGY &amp; ENVIRONMENT SGP/WAAGNER-BIRO GmbH Process for converting water soluble heavy metal compounds into water insoluble, or sparingly soluble, compounds
FR2732910A1 (en) * 1995-04-13 1996-10-18 Viafrance Sa Treating cinders from incineration of domestic waste with carbon di:oxide

Non-Patent Citations (6)

* Cited by examiner, † Cited by third party
Title
DATABASE WPI Section Ch Week 7926, Derwent World Patents Index; Class D15, AN 79-48066B, XP002029441 *
DATABASE WPI Section Ch Week 8213, Derwent World Patents Index; Class D15, AN 82-24882E, XP002029440 *
DATABASE WPI Section Ch Week 8818, Derwent World Patents Index; Class D15, AN 88-122585, XP002029439 *
DATABASE WPI Section Ch Week 9001, Derwent World Patents Index; Class J01, AN 90-002902, XP002029438 *
PATENT ABSTRACTS OF JAPAN vol. 005, no. 132 (C - 068) 22 August 1981 (1981-08-22) *
REDDY K J ET AL: "REACTION OF CO2 WITH ALKALINE SOLID WASTES TO REDUCE CONTAMINANT MOBILITY", WATER RESEARCH, vol. 28, no. 6, 1 June 1994 (1994-06-01), pages 1377 - 1382, XP000435988 *

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2137071A1 (en) * 1996-03-18 1999-12-01 Vicent Claverie Martin Procedure for the inertization of solid alkaline waste.
FR2770159A1 (en) * 1997-10-24 1999-04-30 Recupyl Sa Treatment with waste incinerator residues
EP0913172A1 (en) * 1997-10-28 1999-05-06 Deutsche Babcock Anlagen Gmbh Method for treating incineration residues
WO2002018069A1 (en) * 2000-09-01 2002-03-07 Tech-Wise A/S Process for the treatment of bottom ash from waste incineration plants
JP2015054313A (en) * 2013-09-13 2015-03-23 大阪瓦斯株式会社 Processing method of incineration ash and incineration apparatus

Also Published As

Publication number Publication date
AU1715297A (en) 1997-09-10

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