Classifications

• • C—CHEMISTRY; METALLURGY
  • C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
  • C22C—ALLOYS
  • C22C38/00—Ferrous alloys, e.g. steel alloys
  • C22C38/002—Ferrous alloys, e.g. steel alloys containing In, Mg, or other elements not provided for in one single group C22C38/001 - C22C38/60
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
  • B09C—RECLAMATION OF CONTAMINATED SOIL
  • B09C1/00—Reclamation of contaminated soil
  • B09C1/002—Reclamation of contaminated soil involving in-situ ground water treatment
• • 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
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F1/00—Treatment of water, waste water, or sewage
  • C02F1/70—Treatment of water, waste water, or sewage by reduction
  • C02F1/705—Reduction by metals
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F2101/00—Nature of the contaminant
  • C02F2101/30—Organic compounds
  • C02F2101/36—Organic compounds containing halogen
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
  • C02F2103/06—Contaminated groundwater or leachate
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
  • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
  • Y10T428/00—Stock material or miscellaneous articles
  • Y10T428/12—All metal or with adjacent metals

Definitions

• the present invention relates to a new material and the use of the new material for remediation of polluted soil, water or groundwater as well as a method for remediation of polluted soil, water or ground water.
• halogenated hydrocarbons for instance chlorinated compounds
• halogenated hydrocarbons have been accumulated in the soil and ground water and can constitute a long term threat against health and environment. It is therefore of outmost importance to find methods and materials suitable for reducing the content of halogenated hydrocarbons in polluted soil, water and ground water.
• pollutants may be contained in large volumes of e.g. soils at various concentration levels
• materials to be used for decomposing and reducing contents of pollutants should preferably be fairly inexpensive and have an ability to be effective at various concentration levels and varying overall conditions.
• Remediation technologies are many and varied but can be categorized into ex-situ and in-situ methods.
• Ex-situ methods involve excavation of effected soils and subsequent treatment at the surface. In-situ methods seek to treat the contamination without removing the soils.
• the more traditional remediation approaches (used almost exclusively on contaminated sites from the 1970s to the 1990s) consists primarily of soil excavation and disposal to landfill (“dig and dump”) and groundwater (“pump and treat”).
• In situ technologies include solidification and stabilization and have been used extensively in the USA.
• One interesting in-situ remediation technology for treating halogenated/chlorinated hydrocarbon contaminated soil, water or ground water is based on decomposition of the substances into less harmful species of which one end product being chloride-ions.
• ZVI zero-valent iron
• Patent application WO2004/007379 describes support catalysts for in situ remediation of soil and/or groundwater contaminated with chlorinated hydrocarbons, comprising activated carbon as an absorbent and impregnated with ZVI.
• suitable shape of ZVI are powder, turnings or chips.
• the application also discloses support catalysts made by pyrolizing a mixture of activated carbon and iron salt followed by reducing the formed iron oxide to ZVI.
• a method for preparing highly stabilized and dispersible ZVI nanoparticles and using the nanoparticles in a remediation technology against inorganic chemical toxins in contaminated sites.
• the patented method comprises: providing a composition of ZVI nanoparticles dispersed in an aqueous carrier and stabilizer comprising carboxymethyl cellulose and delivering said composition to the contaminated site.
• US patent application 2009/0191084 (Liskowitz) teaches ZVI in the form of particles or iron wool enriched with graphite carbon and sulphur which is supposed to create catalytic sites on the surface of the ZVI, promoting atomic hydrogen formation in a aqueous oxygen containing environment polluted with e.g. trichloroethylene.
• the formed atomic hydrogen will promote reduction of trichloroethylene to ethylene and ethane.
• Pure ZVI on the other hand tends to promote a reaction chain involving direct electron transfer from the corroding iron to the dissolved contaminating compound.
• US patent application 2010/0126944 discloses degradation of organic nitro compounds, especially nitro aromatic compounds and nitroamines, with bimetallic particles comprising ZVI having discontinuous coatings of metallic copper on the surface thereof. Higher rates of degradation are achieved when the water has a pH of 3.5-4.4 and especially when acetic acid is present in the water.
• Patent application US 201 1/0130575 describes a clay comprising a 2:1 aluminosilicate having negative charged sites; the 2:1 aluminosilicate clay containing sub-nano-sized ZVI particles distributed on the clay surface. Methods of synthesizing the novel clay is also described as well as its use in remediation applications e.g. dechlorination reductions.
• Korean patent KR1076765B1 discloses nitrate reduction of water using ZVI combined with nickel, palladium or copper.
• EP0506684 to Gilham discloses a procedure for cleaning a halogenated organic contaminant from groundwater in an aquifer by contacting the polluted ground water with a metal body, e.g. ZVI in the form of filings, particulates, fibers etc. under anaerobic conditions.
• a metal body e.g. ZVI in the form of filings, particulates, fibers etc. under anaerobic conditions.
• the present invention relates to an iron- boron alloy powder or an iron-boron alloy powder composition suitable for remediation of halogenated hydrocarbon polluted soil, water or groundwater as well as the use of the powder or powder composition. Further, the present invention provides a method for remediation of halogenated hydrocarbon polluted soil, water groundwater. It has been shown that the new material has a similar or higher activity for decomposition of halogenated hydrocarbon compared to commercially available much finer zero valent iron powders.
• the present invention provides a solution to the above mentioned problems and is based on the unexpected finding that ZVI particles, alloyed with boron (B), exhibit a surprisingly high efficiency in terms of decomposing halogenated/chlorinated hydrocarbon polluted water and soil. It has also been shown that ZVI, alloyed with B, having a relatively coarse particle size, well above so called nano-sized scale, have the same or higher efficiency for decomposing halogenated/chlorinated hydrocarbon polluted water and soil compared to finer ZVI and/or nano-scale ZVI.
• the materials according to the invention exhibit a relatively long life-time making them suitable for remediation purposes, especially remediation of polluted soil/groundwater.
• a B-iron alloy powder also denominated as B-ZVI alloy powder
• B-ZVI alloy powder having a B-content of 0.1-40% by weight, preferably 0.1-30 % by weight, preferably 0.1-20% by weight, preferably 0.1-10 % by weight, preferably 0.1-5% by weight or preferably 0.3-4% by weight.
• intervals of boron contents according to the first aspect of the present invention are 0.5-15% by weight, 0.5-10% by weight, 0.5-7% by weight, 0.5-5% by weight, 0.5-4% by weight, 0.7-4% by weight, 0.7-3.5% by weight or 0.8-3% by weight.
• a content of B above 40% by weight does not contribute to improved properties in terms of reaction efficiency and will also considerably increase the cost of the material.
• B-content below 0.1 % by weight will not render the alloy powder the desired properties.
• B- content above 20% by weight, or above 10%, or even above 7% by weight may increase the risk that excessive amounts of B are released to the recipient, thus constituent a potential environmental problem.
• the optimal B-content is depending of e.g. type and concentration of chemicals (for instance chlorinated hydrocarbons) to be decomposed and type of polluted soil, water or groundwater.
• the B-ZVI alloy powder has a content of Fe of more than 60% iron, preferably more than 80% by weight, preferably more than 85%, preferably more than 90% by weight, preferably more than 93% by weight, preferably more than 95% by weight, preferably more than 96% by weight, preferably more than 96.5% by weight.
• the amount of inevitable impurities such as carbon, oxygen, sulphur, manganese and phosphorus should be less than 10%, preferably less than 7%, preferably less than 5% by weight, preferably less than 3 % by weight.
• Carbon and sulphur may in some embodiments contribute to the remediation and thus the contents of these elements can be controlled to desired levels. Such levels may be up to 5 % by weight.
• the particle size may be in the interval of 20 mm and 1 ⁇ .
• the optimal particle size range is depending of e.g. type and concentration of halogenated hydrocarbons to be decomposed and type of polluted soil or groundwater.
• the B-ZVI alloy powder particles according to the present invention may have a particle size between 20 mm and 0.5 mm, preferably between 10 mm and 1 mm.
• the particle size may be defined by the weight average particle size, X 50 , as measured by standard sieving according to SS EN 24497 or by laser diffraction according to SS-ISO 13320-1 , being between 8 and 3 mm.
• a particle size between 0.5 mm and 10 ⁇ , preferably 250 ⁇ and 10 ⁇ may be used.
• the particle size may be defined by the weight average particle size, X 50 , as measured by standard sieving according to SS EN 24497 or by laser diffraction according to SS-ISO 13320-1 , being between 150 ⁇ and 20 ⁇ .
• a particle size between 50 ⁇ to 1 ⁇ , preferably 30 ⁇ to 1 ⁇ may be used.
• the particle size may be defined by the weight average particle size, X 50 , as measured according to SS-ISO 13320-1 , by laser diffractometry, being between 20 ⁇ and 5 ⁇ .
• coarser particle sizes which may be produced from finer particles and turned into coarser porous or non-porous particles, thereby forming aggregate(s), by known methods such as agglomeration, compaction and milling, heat treatment and milling, or compaction, heat treatment and milling. Examples of such known methods may be found in Metals Handbook, Ninth Edition, Volume 7, Powder Metallurgy, American Society for Metals, 1984, page 293-492, Consolidation of Metal Powders. Depending on the application, i.e.
• B-ZVI alloy powder with known substances may be chosen in order to obtain optimal efficiency, forming a ZVI-B-alloy powder composition (also denominated as B-iron alloy powder composition or B-ZVI alloy powder composition).
• the particle size being determined by standard sieving according to SS EN 24497 or by laser diffraction according to SS-ISO 13320- 1.
• the particle size intervals shall be interpreted as 80% or more, by weight of the particles being within the intervals.
• the B-ZVI alloy powder used may originate directly from atomization a molten-iron-boron alloy, e.g. from gas atomization or water atomization as described in Metals Handbook, Ninth Edition, Volume 7, Powder Metallurgy, American Society for Metals, 1984, page 25-30, Atomization.
• the B-ZVI alloy powder may be produced through milling of an atomized iron-boron alloy or through milling solidified pieces of various size of an iron-boron alloy melt. Examples of milling operations are described in Metals Handbook, Ninth Edition, Volume 7, Powder Metallurgy, American Society for Metals, 1984, page 56-70, Milling of Brittle and Ductile Materials.
• the B-ZVI alloy powder particles are dispersed in a carrier or thickener such as guar gum or carboxymethyl cellulose thus avoiding sedimentation of the particles and facilitating handling of the material, e.g. facilitating injection of a water dispersion containing B-ZVI alloy powder into polluted soil or aquifer.
• the thickener is guar gum solution at a concentration 0.1-10% by weight, preferably 0.1-6% by weight, in which the B-ZVI alloy powder composition is dispersed. It has also been shown that the presence of boron increases the viscosity of a guar gum based dispersion compared to a dispersion with similar material but without boron. This enables additions of lower amount of guar gum, thus decreasing the cost.
• a method for remediation of polluted soil, water or groundwater may be due to the presence of hydrocarbons (e.g. halogenated hydrocarbons such as e.g. chlorinated or boronated compounds, dyes, etc.), other organics, or metals.
• hydrocarbons e.g. halogenated hydrocarbons such as e.g. chlorinated or boronated compounds, dyes, etc.
• the method comprising the steps of providing a B-ZVI alloy powder or B- ZVI alloy powder composition according to the first aspect, contacting the B-ZVI alloy powder or B-ZVI alloy powder composition with the polluted soil water or groundwater by placing the B-ZVI alloy powder or B-ZVI alloy powder composition in a trench or in an aquifer in the polluted area, alternatively injecting the B-ZVI alloy powder or B-ZVI alloy powder composition into the polluted soil or aquifer, for a time sufficient to decompose the pollutants.
• the B-ZVI alloy powder or B-ZVI alloy powder composition will be allowed to remain in the soil or aquifer after the decomposition reactions have diminished or ceased.
• the B-ZVI alloy powder or B-ZVI alloy powder composition according to the invention may also be applied in material reactor type recipients, above ground or below ground level.
• the B-ZVI alloy powder or B-ZVI alloy powder composition according to the invention may also be applied in soilmixing.
• halogenated hydrocarbons such as Chlorinated Aliphatic Hydrocarbon (CAH
• pollutants may be chlorinated ethenes comprising tetrachloroethylene (PCE), trichloroethylene (TCE) and cis-dichloroethylene (cDCE); the group of chloroethanes comprising 1 , 1 ,1 ,2 tetrachloroethane (1 1 1 1 TeCE), 1 ,1 ,2,2 tetrachloroethenes (1 122 TeCE), 1 ,1 ,1 trichloroethane (1 1 1-TCA), 1 , 1 ,2 trichloroethane and 1 ,1 Dichloroethane (1 1-DCA); the group of chloromethanes comprising chloroform, dichlorobromomethane
• Particle size distributions X10, X50 and X90 were measured according to SS-ISO 13320-1 by laser diffractometry with a HELOS laser diffraction sensor together with RODOS dispersing unit diffraction.
• the units X10, X50 and X90 represent the particles sizes - a percentage (10%, 50%, 90%) of the particles of the material is smaller than the indicated size.
• the focal lengths were R3 and R5.
• the trigger thresholds for start/stop conditions were 2%, respectively.
• the light scattering model was according to Fraunhofer. Dry dispersion was used, with an injection diameter of 4 mm, primary pressure was 3 bar. The dispersion unit was set up to reach an optical concentration between 5 to 15%.
• the specific surface areas were analyzed by single point measurement with a Micromeritics Flowsorb III instrument according to the BET method (Brunauer-Emmett-Teller method) using adsorption of N 2 at the temperature of liquid N 2 . All the samples were degassed at 1 10°C for 30 minutes before analysis.
• CAHs used were tetrachloroethylene (PCE), trichloroethylene (TCE), cis-dichloroethylene (cDCE) and 1 ,1 , 1 trichloroethane (1 1 1-TCA).
• the experiments were set up under anaerobic conditions and in triplicates. The vials were then placed for continuously gently mixing at 12 C. H 2 , CAHs, acetylene, ethane and methane were measured as start up (only blank) and after 14, 28, 49, and 105 days. CAH concentrations (including breakdown products) were measured using a GC-FID instrument (VARIAN).
• concentrations of PCE, TCE and c-DCE with respect to time are shown in Tables 2 to 4.
• Tables 5 and 6 show concentrations with respect to time of the breakdown products ethene and ethane.
• the boron containing materials according to the invention nos. 4 to 7 show a superior reactivity rate for reducing the contaminants TCE and c- DCE compared to the reference materials nos 1 to 3.
• the commercially available material no 2 shows a comparable reactivity rate related to decomposition of the contaminant PCE, when compared to the materials according to the invention.
• Tables 5 and 6 above show the concentration of the less harmful reaction products of the decomposition reactions, ethene and ethane. It can be noticed that the concentrations of ethene and ethane increase more rapidly for the materials according to the invention compared to the reference materials.
• Example 7 shows the corrosion rate and life time for some of the ZVI materials in Example 1.

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• Engineering & Computer Science (AREA)
• Life Sciences & Earth Sciences (AREA)
• Environmental & Geological Engineering (AREA)
• Chemical & Material Sciences (AREA)
• Soil Sciences (AREA)
• Organic Chemistry (AREA)
• Hydrology & Water Resources (AREA)
• Water Supply & Treatment (AREA)
• Metallurgy (AREA)
• Mechanical Engineering (AREA)
• Materials Engineering (AREA)
• Processing Of Solid Wastes (AREA)
• Treatment Of Water By Oxidation Or Reduction (AREA)
• Manufacture Of Metal Powder And Suspensions Thereof (AREA)
• Powder Metallurgy (AREA)

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• 2013
  • 2013-09-18 IN IN2446DEN2015 patent/IN2015DN02446A/en unknown
  • 2013-09-18 CA CA2885252A patent/CA2885252A1/en not_active Abandoned
  • 2013-09-18 KR KR1020157010033A patent/KR20150056640A/ko not_active Abandoned
  • 2013-09-18 DK DK13765349.9T patent/DK2897911T3/da active
  • 2013-09-18 WO PCT/EP2013/069326 patent/WO2014044692A1/en not_active Ceased
  • 2013-09-18 AU AU2013320366A patent/AU2013320366B2/en not_active Ceased
  • 2013-09-18 ES ES13765349.9T patent/ES2643509T3/es active Active
  • 2013-09-18 BR BR112015006277A patent/BR112015006277A2/pt not_active Application Discontinuation
  • 2013-09-18 PL PL13765349T patent/PL2897911T3/pl unknown
  • 2013-09-18 EP EP13765349.9A patent/EP2897911B1/en not_active Not-in-force
  • 2013-09-18 TW TW102134043A patent/TWI626092B/zh not_active IP Right Cessation
  • 2013-09-18 JP JP2015532389A patent/JP6235596B2/ja not_active Expired - Fee Related
  • 2013-09-18 US US14/429,688 patent/US9816164B2/en not_active Expired - Fee Related
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