EP3645132A1 - Stabilization of hazardous materials - Google Patents
Stabilization of hazardous materialsInfo
- Publication number
- EP3645132A1 EP3645132A1 EP18823982.6A EP18823982A EP3645132A1 EP 3645132 A1 EP3645132 A1 EP 3645132A1 EP 18823982 A EP18823982 A EP 18823982A EP 3645132 A1 EP3645132 A1 EP 3645132A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- arsenic
- aluminum
- scorodite
- gel
- carbonate base
- 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.)
- Pending
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
- B09B3/20—Agglomeration, binding or encapsulation of solid waste
- B09B3/25—Agglomeration, binding or encapsulation of solid waste using mineral binders or matrix
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
- B09B3/20—Agglomeration, binding or encapsulation of solid waste
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09C—RECLAMATION OF CONTAMINATED SOIL
- B09C1/00—Reclamation of contaminated soil
- B09C1/08—Reclamation of contaminated soil chemically
Definitions
- This invention relates to stabilization / solidification of hazardous materials and, in particular, arsenical wastes through encapsulation with mineralized products of hydrolyzed aluminum gels.
- Stabilization/solidification is an approach used for the fixation of toxic waste materials of various types and sources.
- An example of such a process involves the mixing of a toxic waste with cement and/or other binder materials to produce a chemically and physically stable solid mass suitable for use in the landfill.
- the most common technologies currently used for the stabilization/solidification of hazardous wastes are those based upon hydraulic cement and/or slaked lime and, less commonly, organic polymers, sulphur polymer cement, and other encapsulation materials.
- a method for the stabilization of hazardous materials comprising:
- carbonate base such as NaHC03 or Na 2 COs
- aluminum gels and their mineralized products in stabilization of hazardous materials.
- a composite comprising scorodite particles and a gel-derived solidified matrix comprising aluminum (oxy)hydroxide mineral phases.
- a composite prepared by the method as defined herein.
- FIG. 1 is a graph of the evolution profiles of pH and Eh with time during stability testing of scorodite-gel blends using either Na 2 S0 3 (top) or Na 2 S (bottom) to adjust Eh;
- FIG. 2 depicts arsenic release from naked scorodite and scorodite encapsulated with aluminum gels derived from reference bases NaOH and Mg(OH) 2 , compared to a carbonate base
- FIG. 3 depicts arsenic release from naked scorodite and scorodite encapsulated with aluminum gels derived from reference bases NaOH and Mg(OH) 2 , compared to a carbonate base
- FIG. 4 is a graph showing the arsenic release from naked scorodite and scorodite encapsulated with Al-gels prepared from NaOH, Na2C03 and NaHC03 under anoxic (Na2S03) condition and pH ⁇ 9;
- FIG. 5. represents the arsenic release from scorodite encapsulated with aluminum gels derived from Na 2 C0 3 and NaHC0 3 under anoxic condition chemically generated with Na 2 S;
- FIG. 6 depicts XRD patterns of Na 2 C0 3 derived aluminum gels after 167 days stability testing under oxic and anoxic conditions;
- FIG. 7 presents the profile of arsenic release from scorodite encapsulated with Al-gels prepared from Na 2 CC>3 or Mg(OH) 2 under oxic (with and without elemental sulfur present) or anoxic (Na 2 S) condition (with or without elemental sulfur present) in water of pH ⁇ 9 compared to release of arsenic under same conditions from naked scorodite; and
- FIG. 8 is a schematic representation of scorodite particle encapsulated with gel-derived mineralized aluminum (oxy)hydroxides phases.
- the inventors have discovered hydrolyzed aluminum gels derived from aluminum sulfate solutions by neutralization with carbonate bases to be highly effective in encapsulating hazardous materials like scorodite particles.
- the said aluminum gels form a mineralized matrix protecting the scorodite particles from decomposition in alkaline or anoxic waters, hence minimizing release of arsenic.
- the encapsulation process involves blending scorodite particles with gels prepared with carbonate bases from aluminum sulphate solution and storing the resultant composite that provides protection via the in situ formation of a mineralized aluminum (oxy)hydroxide matrix.
- the carbonate base is comprising a carbonate anion (formula: CO3 2" ) or bicarbonate anion (formula: HCO 3 " - also referred to as hydrogen-carbonate ion in the IUPAC system).
- Suitable carbonates include:
- the carbonate base is NaHC0 3 or Na 2 C0 3 .
- the molar ratio of Al:As is ranging from about 1.5 to 0.05; preferably less than about 1, or from about 1.0 to 0.1, or less than about 0.2, or more preferably from about 0.2 to 0.1, and most preferably about 0.1.
- the concentration of Al(S0 4 ) l 5 in the aqueous medium for preparing the Al gel is ranging from about 0.5 to 3.0M (mol/L) of 1.0 to 3.0 mol/L; preferably, about 1.0 to 2.0, more preferably about 1.5 to 2.0, and most preferably about 2.0.
- the carbonate bases can be used as powders or suspension/solution.
- Na 2 C0 3 from about 0.5M to dry powder and preferably about 1.0M to 6M, more preferably about 2M to 4M and most preferably about 2.5 to 3M.
- NaHC0 3 one can double these numbers, i.e. from about 1M to powder, or about 2M to 12M or about 4M to 8M or most preferably about 5 to 6M.
- the amount will suitably vary depending on the concentration of Al sulfate solution.
- the skilled person understands that it may not be desirable to use very dilute solutions of base or AI-SO 4 as this would lead to very liquid-like gel. On the other hand, it may not be desirable to use too concentrated a medium as this leads to immediate solidification (in the form of crushed ice) of the gel, and making more difficult its handling, such as its transportation to the storage site.
- the temperature range for forming the gel or blending it with the hazardous material is from about 0 to 80°C, or preferably about 10 to 40°C, or more preferably about 15 to 30°C or about 20°C.
- hazardous materials subjected to stabilization with hydrolyzed aluminum gels as defined herein is not especially limited. Examples include ferric arsenate/scorodite, but however may as well be other arsenical compounds, residues, precipitates or flue dusts such as arsenic sulfides, calcium arsenates or arsenites, mixed calcium arsenates- phosphates, ferrous arsenate, ferric arsenite, arsenic trioxide and so on. Further, the carbonate- derived aluminum gels could be used to provide additional protection to arsenical residues previously stabilized (partially) with conventional cement based methods.
- the gels could be used for other types of hazardous materials, as is the case for example of antimony, mercury or selenium-containing wastes generated by smelting and other industrial operations.
- "blending" may involve aging following mixing of the gel and the hazardous arsenical material or not before permanent disposal.
- Non-limiting examples of aging time may be about one day or from 1 day to 30 days before permanent disposal (storing) of the blended material.
- aqueous medium can be essentially water, optionally comprising conventional additional components present in the "hazardous materials" subjected to stabilization with hydrolyzed aluminum gels as defined herein.
- the scorodite substrate material was synthesized by atmospheric precipitation via the use of a seed and supersaturation control method previously developed by the inventors.
- 0.5 L As(V) - Fe(III) - H 2 S0 4 solutions containing 40 g/L arsenic(V) and iron(III) to arsenic molar ratio of one were placed in a reactor and heated to 95°C.
- 5 g of hydrothermally produced scorodite were added to the reactor as seed.
- precipitation started and was allowed to proceed for 24 hours, after which the slurry was filtered using a pressure filter with 0.22 ⁇ pore size membrane filter.
- TCLP Toxicity Characterization Leachability Procedure-method developed by the Environmental Protection Agency-EPA- of the USA.
- the freshly washed scorodite particles were subsequently used in aging with aluminum hydroxyl gels. All the reagents and chemicals used were of analytical grade.
- Preferred gels were prepared using sodium bicarbonate (NaHCOs) and sodium carbonate (Na 2 CC>3) by partial neutralization of aluminum(III) sulfate solution.
- magnesium hydroxide also as reference gel
- sodium carbonate and sodium bicarbonate powders or previously dissolved or suspended in water (as reported in the specific examples given) were introduced to the prepared Al(S0 4 ) l 5 (typical concentration: 2 mol/L) solutions.
- Mild stirring had to be applied during mixing as excessive force was found to be counter-productive, causing gel thinning.
- the freshly prepared aluminum gels were used to stabilize scorodite particles.
- This anoxic stability test was conducted at adjusted reducing potential (Eh) conditions ( 200 + 20 mV ) via the addition of sodium sulfite (0.15mol/L Na 2 SOs) solution. The pH of the solution was monitored and periodically adjusted to pH 9 ⁇ 0.2 with 0.5 mol/L Ca(OH)2 slurry. Refer to FIG. 1.
- This anoxic stability test was conducted at adjusted reducing potential (E h ) of 50mV via addition of sodium sulfide solution (0.125M Na 2 S). The pH of the solution was monitored and periodically adjusted to pH 9 ⁇ 0.2 with 0.5 mol/L Ca(OH) 2 slurry. Refer to FIG. 1.
- ICP-AES Inductively Coupled Plasma- Atomic Emission Spectrometer
- an aluminum gel of acceptable quality for ageing tests is one that has a sufficiently high initial viscosity (at least 300 cP) to enable solid particles to be blended with the gel without subsequently settling. It is also preferable that the aluminum gel maintains a sufficiently high viscosity for enough time (e.g. 1 to 24 hours) for ease of transportation to storage site before it becomes solidified.
- Tables 1-4 below summarizes some of the viscosity measurements. The measurements were made with a Brookfield LVDV-E Viscometer apparatus. [0037] Table 1 - NaOH pellets, Na 2 C0 3 , NaHC0 3 powders were introduced to a 2M Al(S0 4 )i.s solution.
- NaHCC>3 and Na 2 CC>3 provided satisfactory initial viscosities under various reaction conditions except for very dilute (0.5M-Table 3) Al(S04)i.s solution.
- tests showed gels made with NaOH suffered breakage with time, i.e. water/gel separation (Table 4).
- scorodite encapsulated with the gel deriving from Na2C03 exhibited a negligible amount of arsenic release after 167 days, and was below the detection limit of the ICP-AES for arsenic (i.e. ⁇ 0.1 mg/L) at a final pH of -7.6. This is significantly lower than the permitted amount of released arsenic in leachate from industrial/mining waste ranging from 1.0 mg/L in certain countries like Japan to 5.0 mg/L in USA. Therefore, these gels display a superior performance for industrial usage. It was also observed that the arsenic released from the two types of hydroxide ions (i.e. NaOH and Mg(OH) 2 ) varied broadly and in an unexpected manner relative to each other.
- FIG. 3 shows the arsenic release versus time for various aluminum gel/scorodite materials in comparison with scorodite substrate under anoxic environment (chemically generated under Na 2 SOs). It can be seen that the dissolution of scorodite (-137 mg/L in the case of naked mineral) was effectively suppressed with the aid of these aluminum gels encapsulations. The concentration of arsenic released from scorodite encapsulated with particular aluminum gels was reduced by at least one order of magnitude. The scorodite encapsulated with the sodium hydroxide -derived gels had a significantly higher arsenic release.
- the arsenic released from the scorodite encapsulated with Al-gel derived from NaHC0 3 is no more than 0.1 mg/L and lower than that from Al-gel derived from Na 2 C0 3 .
- the in-situ mineralization of the hydrolyzed aluminum gel into inert aluminum (oxy)hydroxide crystalline phases as schematically depicted in FIG. 8 provides a protective layer to the scorodite particles, thus preventing their dissolution/decomposition.
- the mineralized aluminum (oxy)hydroxide matrix is immune to pH and redox potential swings compared to those caused by the addition of chemical reducing agents, hence greatly enhancing the stabilization of the toxic material.
Landscapes
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Processing Of Solid Wastes (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Removal Of Specific Substances (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Abstract
La présente invention concerne la stabilisation et/ou la solidification de matières dangereuses qui peuvent être générées par des activités telles que des opérations industrielles d'extraction minière, de broyage ou de fusion, par exemple de déchets arsénifères (tels que la scorodite, les sulfures d'arsenic, les arséniates ou les arsenites de calcium, les d'arséniates-phosphates de calcium mixtes, l'arséniate ferreux, l'arsénite ferrique ou le trioxyde d'arsenic), d'antimoine, de déchets contenant du mercure ou du sélénium par l'encapsulation desdits déchets arsénifères dans les produits minéralisés de gels d'aluminium hydrolysés créés par la neutralisation partielle d'Al(SO4)1, 5 par un carbonate.The present invention relates to the stabilization and / or solidification of hazardous materials that can be generated by activities such as industrial mining, milling or melting operations, for example arsenic waste (such as scorodite, sulphides). arsenates or calcium arsenates, mixed calcium arsenate phosphates, ferrous arsenate, ferric arsenite or arsenic trioxide), antimony, mercury-containing wastes or selenium by encapsulating said arsenic waste in the mineralized hydrolysed aluminum gel products created by the partial neutralization of Al (SO4) 1, 5 with a carbonate.
Description
Claims
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US201762526511P | 2017-06-29 | 2017-06-29 | |
| PCT/CA2018/050790 WO2019000091A1 (en) | 2017-06-29 | 2018-06-27 | Stabilization of hazardous materials |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EP3645132A1 true EP3645132A1 (en) | 2020-05-06 |
| EP3645132A4 EP3645132A4 (en) | 2021-03-03 |
Family
ID=64740780
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP18823982.6A Pending EP3645132A4 (en) | 2017-06-29 | 2018-06-27 | STABILIZATION OF HAZARDOUS MATERIALS |
Country Status (9)
| Country | Link |
|---|---|
| EP (1) | EP3645132A4 (en) |
| JP (1) | JP7265267B6 (en) |
| CN (1) | CN110944724B (en) |
| AU (1) | AU2018292424B2 (en) |
| CA (1) | CA3096126A1 (en) |
| CL (1) | CL2019003807A1 (en) |
| MX (1) | MX2020000165A (en) |
| PE (1) | PE20200766A1 (en) |
| WO (1) | WO2019000091A1 (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2020237361A1 (en) | 2019-05-28 | 2020-12-03 | The Royal Institution For The Advancement Of Learning / Mcgill University | Method for producing scorodite |
| CN111069228A (en) * | 2019-11-22 | 2020-04-28 | 昆明理工大学 | Method for wrapping stabilized scorodite by copper slag gel |
| CN112718793B (en) * | 2020-12-15 | 2022-03-11 | 紫金矿业集团股份有限公司 | Method for directly vitrifying arsenic-fixing material containing arsenite |
| CN119301077A (en) * | 2023-04-06 | 2025-01-10 | 埃科美泰尔斯公司 | Method for stabilizing arsenic by precipitating ferric arsenate by blending with aluminum gel |
| CN120943485B (en) * | 2025-10-15 | 2026-02-27 | 中铝山东新材料有限公司 | Treatment method of carbonate-containing alkaline washing liquid |
Family Cites Families (25)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS53144872A (en) * | 1977-05-25 | 1978-12-16 | Takenaka Komuten Co | Solidification method* solidifying agent and additive aid for wastes |
| JPS5496250A (en) * | 1978-08-25 | 1979-07-30 | Takenaka Komuten Co Ltd | Solidification of waste, solidifier agent, and additives |
| WO1996037264A1 (en) * | 1995-05-26 | 1996-11-28 | Rmt, Inc. | Method of treating arsenic-contaminated matter using aluminum compounds |
| IL133161A0 (en) * | 1997-05-29 | 2001-03-19 | Pericalse Pty Ltd | Encapsulation of hazardous waste materials |
| AU736813B2 (en) * | 1997-05-29 | 2001-08-02 | Dolomatrix International Limited | Encapsulation of hazardous waste materials |
| US6254312B1 (en) * | 1998-06-18 | 2001-07-03 | Rmt, Inc. | Stabilization of arsenic-contaminated materials |
| US6843617B2 (en) * | 1998-06-18 | 2005-01-18 | Rmt, Inc. | Stabilization of toxic metals in a waste matrix and pore water |
| CA2481961C (en) * | 2002-04-10 | 2012-07-10 | Manoranjan Misra | Removal of arsenic from drinking and process water |
| AUPS200702A0 (en) * | 2002-04-29 | 2002-06-06 | Dolomatrix International Limited | Treatment of hazardous waste material |
| JP4718155B2 (en) * | 2004-10-06 | 2011-07-06 | 水澤化学工業株式会社 | Method for producing deodorant composite composition |
| JP5069154B2 (en) * | 2008-03-11 | 2012-11-07 | 電気化学工業株式会社 | Porous purification material and purification method using porous filter using the same |
| US20100155330A1 (en) * | 2008-11-11 | 2010-06-24 | Molycorp Minerals, Llc | Target material removal using rare earth metals |
| JP2011184266A (en) * | 2010-03-10 | 2011-09-22 | Dowa Metals & Mining Co Ltd | Method for treating iron arsenate particle |
| CN101863565B (en) * | 2010-03-23 | 2012-07-25 | 中国地质大学(武汉) | Earth surface depth treatment method of high-arsenic underground water and system thereof |
| CN102336461A (en) * | 2010-07-27 | 2012-02-01 | 中国科学院过程工程研究所 | Method for removing metal ions from aqueous solution by use of hydrotalcite |
| JP5599061B2 (en) * | 2010-10-25 | 2014-10-01 | 太平洋セメント株式会社 | Neutral solidifying material additive, neutral solidifying material and method for suppressing elution of heavy metals |
| CN102249609B (en) * | 2011-04-29 | 2013-06-12 | 昆明理工大学 | Arsenic-containing waste slag solidified body and preparation method thereof |
| JP5905669B2 (en) * | 2011-05-23 | 2016-04-20 | 日鉄住金環境株式会社 | Hazardous material treatment material and method |
| JP6226235B2 (en) * | 2013-03-29 | 2017-11-08 | 三菱マテリアル株式会社 | Method for producing scorodite |
| CN103316904A (en) * | 2013-04-10 | 2013-09-25 | 天津市环境保护科学研究院 | Repairing method of chromium polluted soil |
| AU2014341297B2 (en) * | 2013-10-28 | 2017-05-25 | Yoshino Gypsum Co., Ltd. | Insolubilizing material for specific hazardous substance and method for insolubilizing specific hazardous substance with same |
| CN103553197B (en) * | 2013-11-05 | 2014-12-31 | 红河学院 | Method for removing arsenic and antimony in industrial wastewater by using smelting furnace slag |
| CN103952207B (en) * | 2014-04-08 | 2015-07-15 | 重庆大学 | Arsenic-fixing agent and preparation method thereof, and method utilizing arsenic-fixing agent to fix arsenic |
| CN104774619B (en) * | 2015-02-13 | 2017-12-26 | 湖南永清环保研究院有限责任公司 | It is a kind of for the solidification stabilizer of As polluted soil and its application |
| CN106242121A (en) * | 2016-09-05 | 2016-12-21 | 吉林市润成膜科技有限公司 | A kind of composite drug preparation method removing arsenic in water |
-
2018
- 2018-06-27 WO PCT/CA2018/050790 patent/WO2019000091A1/en not_active Ceased
- 2018-06-27 PE PE2019002680A patent/PE20200766A1/en unknown
- 2018-06-27 CA CA3096126A patent/CA3096126A1/en active Pending
- 2018-06-27 CN CN201880049403.1A patent/CN110944724B/en active Active
- 2018-06-27 AU AU2018292424A patent/AU2018292424B2/en active Active
- 2018-06-27 EP EP18823982.6A patent/EP3645132A4/en active Pending
- 2018-06-27 JP JP2019571443A patent/JP7265267B6/en active Active
- 2018-06-27 MX MX2020000165A patent/MX2020000165A/en unknown
-
2019
- 2019-12-23 CL CL2019003807A patent/CL2019003807A1/en unknown
Also Published As
| Publication number | Publication date |
|---|---|
| CA3096126A1 (en) | 2019-01-03 |
| MX2020000165A (en) | 2020-07-22 |
| CN110944724A (en) | 2020-03-31 |
| AU2018292424B2 (en) | 2023-09-28 |
| PE20200766A1 (en) | 2020-07-30 |
| CN110944724B (en) | 2022-08-26 |
| CL2019003807A1 (en) | 2020-08-14 |
| AU2018292424A1 (en) | 2020-02-13 |
| JP7265267B2 (en) | 2023-04-26 |
| WO2019000091A1 (en) | 2019-01-03 |
| EP3645132A4 (en) | 2021-03-03 |
| JP7265267B6 (en) | 2023-05-19 |
| JP2020525121A (en) | 2020-08-27 |
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