WO2004013050A2 - Solid materials for removing metals and fabrication - Google Patents

Solid materials for removing metals and fabrication Download PDF

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Publication number
WO2004013050A2
WO2004013050A2 PCT/US2002/035221 US0235221W WO2004013050A2 WO 2004013050 A2 WO2004013050 A2 WO 2004013050A2 US 0235221 W US0235221 W US 0235221W WO 2004013050 A2 WO2004013050 A2 WO 2004013050A2
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Prior art keywords
hydrophobic
gac
aerogel
hydrophobic aerogel
mixture
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PCT/US2002/035221
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WO2004013050A3 (en
Inventor
Paul R. Coronado
John G. Reynolds
Sabre J. Coleman
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University of California Berkeley
University of California San Diego UCSD
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University of California Berkeley
University of California San Diego UCSD
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Priority to CA2466169A priority Critical patent/CA2466169C/en
Priority to EP02807656A priority patent/EP1441987A2/en
Priority to JP2004525949A priority patent/JP2005526615A/en
Priority to AU2002368148A priority patent/AU2002368148A1/en
Publication of WO2004013050A2 publication Critical patent/WO2004013050A2/en
Publication of WO2004013050A3 publication Critical patent/WO2004013050A3/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28014—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
    • B01J20/28047—Gels
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/04—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of alkali metals, alkaline earth metals or magnesium
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/10—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
    • B01J20/103—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate comprising silica
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/20—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28014—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
    • B01J20/28016—Particle form
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30—Processes for preparing, regenerating, or reactivating
    • B01J20/3078—Thermal treatment, e.g. calcining or pyrolizing
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30—Processes for preparing, regenerating, or reactivating
    • B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3202—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the carrier, support or substrate used for impregnation or coating
    • B01J20/3204—Inorganic carriers, supports or substrates
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30—Processes for preparing, regenerating, or reactivating
    • B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3231—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
    • B01J20/3242—Layers with a functional group, e.g. an affinity material, a ligand, a reactant or a complexing group
    • B01J20/3244—Non-macromolecular compounds
    • B01J20/3246—Non-macromolecular compounds having a well defined chemical structure
    • B01J20/3257—Non-macromolecular compounds having a well defined chemical structure the functional group or the linking, spacer or anchoring group as a whole comprising at least one of the heteroatoms nitrogen, oxygen or sulfur together with at least one silicon atom, these atoms not being part of the carrier as such
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2220/00—Aspects relating to sorbent materials
    • B01J2220/50—Aspects relating to the use of sorbent or filter aid materials
    • B01J2220/58—Use in a single column

Definitions

  • the present invention relates to the removal of contaminants, particularly to the removal of contaminants from an aqueous media, and more particularly to the removal of contaminating metals and organic compouncis from an aqueous media using solid material, which may be in the form of sol-gel and /or sol-gel and with solid support mixtures, which maybe in the form of granulated activated carbon (GAC).
  • solid material which may be in the form of sol-gel and /or sol-gel and with solid support mixtures, which maybe in the form of granulated activated carbon (GAC).
  • GAC granular activated carbon
  • ion-exchanged resins ion-exchanged resins
  • air-strippers ion-exchanged resins
  • bioremediation are used for contaminate removal.
  • GAC has been commercially used as an adsorbent for contaminants in water. It is cheap and treatment technology hardware is readily available commercially for its use. Even though GAC is a good adsorbent medium for many contaminants, such as VOCs, it is not efficient for certain metals, particularly uranium. Thus, there has been a need for a material " by which contaminating metals and certain organic compounds may be removed from aqueous media.
  • the present invention provides a solution to this need by providing a material that can be used alone or with GAC to make it a good adsorbent for uranium, for example, without loosing the affinity for other contaminants.
  • the material is a sol-gel and /or sol-gel and GAC mixture.
  • a further object of the invention is to provide solid materials for removal of contaminating metals and organic compounds from aqueous media.
  • Another object of the invention is to provide for the removal of uranium from aqueous media.
  • Another object of the invention is to provide a material composed of a sol-gel and/or a sol-gel and a solid support mixtures for removing contaminating metals and organic compounds from aqueous media.
  • Another object of the invention is to provide a material composed of a sol-gel and/or a sol-gel and granulated activated carbon mixtures for removing contaminating metals and organic compounds from aqueous media.
  • the invention involves the removal of contaminating metals, such as uranium, and organic compounds from aqueous media.
  • the invention involves a solid material that may be in molded, granular, or powder form, and the solid material adsorbs the metal and the organics leaving a purified aqueous stream.
  • the solid materials are sol-gel and /or sol-gel and granulated activated carbon (GAC) mixtures. After adsorbing the contaminants, the contaminated solid material can be disposed of or the contaminant can be removed and the solid materials recycled.
  • the species- specific adsorption occurs through specific chemical modifications of the solid materials tailored towards the contaminant(s).
  • Figure 1 shows a Freundlich isotherm plot for baseline granulated activated carbon (GAC).
  • Figure 2 shows a Freundlich isotherm plot for a 1% phosphoric acid and hydrophobic aerogel/GAC composite.
  • Figure 3 shows a Freundlich isotherm plot for a 17% phosphoric acid and hydrophobic aerogel/GAC composite.
  • Figure 4 shows a Freundlich isotherm plot for a phosphoric acid exchanged hydrophobic aerogel/GAC composite.
  • Figure 5 shows a Freundlich isotherm plot for a functionalized phosphonate hydrophobic aerogel/GAC composite.
  • Figure 6 shows a column test for a functionalized phosphate hydrophobic aerogel.
  • the present invention involves removing contaminating metals, such as uranium, and organic compounds from aqueous media use a solid material and fabrication method therefor.
  • the invention utilizes solid materials and the contaminants are removed by passing the aqueous phase through the solid materials, which materials may be in molded, granular, or powder form.
  • the solid materials adsorb the metals and the organics leaving a purified aqueous stream.
  • the solid materials are comprised of sol-gel and /or sol-gel and a solid support such as granulated activated carbon (GAC) mixtures.
  • GAC granulated activated carbon
  • the species-specific adsorption occurs through specific chemical modifications of the solid materials tailored towards the contaminant of choice, such as uranium.
  • the contaminated solid materials can then be disposed of or the contaminant can be removed and the solid materials recycled.
  • the solid materials can be used to cleanup any aqueous stream with environmentally damaging material, such as caused by commercial interests or military activities. For example, but not limited to, ground water with uranium or heavy metal contamination, volatile organic compounds (VOCs) contamination, ground water with gasoline or other fuel spills, waste storage tanks with uranium or heavy metals, and ground water or surface waters "with petroleum product contamination or fuel spills.
  • environmentally damaging material such as caused by commercial interests or military activities.
  • VOCs volatile organic compounds
  • the solid material of this invention may, for example, be composed of a silica sol-gel (aerogel) that has been modified to be hydrophobic and is activated by supercritical drying, and possible further modification is used separately or mixed with a solid support such as GAC, to remove contaminants, particularly uranium, from aqueous streams.
  • a silica aerogel by itself in the past has not been cost-effective.
  • GAC solid support
  • Aerogel/GAC composite is the preferred utilization being superior to previous treatment technologies, including GAC alone.
  • GAC is a widely available commercial material that comes in many forms and from many sources. GAC by itself has been commercially used as an adsorbent for contaminants in water. It is inexpensive and the treatment technology hardware is readily available commercially for its use. It is a good media for adsorption of many other contaminants, such as VOCs, but without modification, it is not an efficient adsorbent of uranium.
  • Aerogels are nano-structured materials having high surface areas (around 5O0 m 2 /g), low densities, and large meso pore structure.
  • nano-structured properties are configured in a three-dimensional structure giving ideal physical properties for adsorption. Through chemical modification, they can be designed to have species-specific binding, as well as discriminating bulk properties. Combining these properties, with the known adsorption properties of GAC as delineated by Tchobanoglous et al, Water Quality, Characteristics, Modeling and Modification, ISBN: 0-201- 05433-7 (1985), makes the aerogel/GAC composite ideal for treating environmentally important systems such as ground water.
  • the key to the superior performance of the aerogel/GAC composite is being able to tailor the aerogel to be specific for the particular target clean-up stream.
  • This stream can be aqueous with metal ions, aqueous with organic compounds, aqueous with metal ions and organic compounds, non-aqueous with the above contaminants.
  • the aerogel/GAC composite design will depend upon the all the components of the stream. This invention is not limited to aqueous streams with uranium in them, but simply uses that as an example of the design of the aerogel/GAC composite for the specific application.
  • the aerogel is tailored to be hydrophobic and specific for adsorbing uranium.
  • the backbone of the aerogel is formed by the hydrolysis condensation of tetra methoxy silane, or tetra ethoxy silane more commonly known as silica sol-gel chemistry. This serves as an example of a method to make the backbone.
  • Other commonly used methods found in the literature such as taught by Brinker and Scherer, Sol-Gel Science, The Physics and Chemistry of Sol-Gel Processing, ISBN: 0-12-134970-5 (1989), are also viable.
  • the hydrophobic component is formed by the addition of, but not limited to, a fluorinated substituent through co-condensation reaction for an example.
  • the trifluoropropyl group is used only to demonstrate the effect of making the hydrophobic character, not to limit the method of production.
  • Reynolds Recent Research Developments in Non-Crystalline Solids, ISBN: 81-7895- 028-6 (2001), teaches such common methods to make the material hydrophobic and other substituents found in the literature can also be used.
  • the uranium adsorption site is formed by the incorporation of a uranium specific binding material into or onto the aerogel and/or the aerogel/GAC composite.
  • Phosphoric acid, exchanged calcium nitrate, and diethyl phosphato ethylene triethoxy silane are used to demonstrate the viability of the approach.
  • Other materials that have affinity for uranium can be used, preferably those materials that have affinity for other species in the cases where other metals and/or organics are targets for clean-up or separation.
  • Other materials such as hydroxyapatite, calcium phosphate, and others can be used.
  • the formation of the aerogel/GAC composite is made by combining the backbone, hydrophobic, and uranium binding components with the GAC. Co-gellation followed by supercritical extraction is an example, but not limited to, how this can be accomplished. 023] The following are examples of the solid material (aerogel) formulation of the invention in practice.
  • Example 2 [0025] 1% phosphoric acid and hydrophobic aerogel was prepared by the following method: 14.7 g (CHsO) 4 Si and 3.14 g (CHsO) 3 SiCH 2 CH 2 CF 3 were mixed together and to this mixture, 18.0 g CH3OH were added and stirred. In a separate vessel, 36.0 g CH3OH, 0.147 g H3PO4, 1.5 g HBF were mixed together and stirred. After about 1 min., both solutions were poured into a supercritical-drying reactor containing 13.4 g of GAC. A vacuum was pulled, and the mixture gelled in less than 1 hour. The gelled mixture was then supercritically dried at 300°C.
  • Example 3 [0026] 17% phosphoric acid and hydrophobic aerogel was prepared by the same method as in Example 2 except 2.5 g H3PO4 was used.
  • Phosphoric acid exchanged hydrophobic aerogel was prepared by the following method: 35.0 g (CH 3 0) 4 Si and 7.55 g (CH 3 0) 3 SiCH 2 CH 2 CF 3 were mixed together and to this mixture, 44.1 g acetone were added and stirred. In a separate vessel, 30.9 g H 2 0, 85.7 g acetone, 7.46 g Ca(N0 3 )2, O.lg HBF 4 were mixed together and stirred. After about 1 min., both solutions were poured into a supercritical-drying reactor containing 96.2 g of GAC. A vacuum was pulled, and the mixture gelled in less than 1 hour. The gelled mixture was then supercritically dried at 300°C.
  • Example 6 [0029] 50 g of the aerogel/GAC composite from Example 3 was tested in a column reactor. A 101 pCi/L uranium solution at pH 7 was treated in a up- flow configuration. Figure 6 shows the concentration of uranium in the effluent as a function of time on stream. The concentration was immediately reduced to 4 pCi/L and remained at that level through the entire run. [0030] It has thus been shown that the aerogel (sol-gel) and granulated activated carbon (GAC) mixtures or composites provide a significant increase in adsorption of metals (uranium) over that of GAC alone, or over aerogel material alone. Thus, this invention enables contamination cleanup of materials such as uranium in addition to contaminants that can be adsorbed by GAC alone, thereby enabling multiple contaminant removal with the same material.
  • GAC granulated activated carbon

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  • Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Dispersion Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Water Treatment By Sorption (AREA)

Abstract

Solid materials have been developed to remove contaminating metals and organic compounds from aqueous media. The contaminants are removed by passing the aqueous phase through the solid materials which can be in molded, granular, or powder form. The solid materials adsorb the metals and the organics leaving a purified aqueous stream. The materials are sol-gel and or sol-gel and granulated activated carbon (GAC) mixtures. The species-specific adsorption occurs through specific chemical modifications of the solids tailored towards the contaminant(s). The contaminated solid materials can then be disposed of or the contaminant can be removed and the solids recycled.

Description

SOLID MATERIALS FOR REMOVING METALS AND FABRICATION
METHOD
[0001] The United States Government has rights in this invention pursuant to Contract No. W-7405-ENG-48 between the United States Department of Energy and the University of California for the operation of Lawrence Livermore National Laboratory.
RELATED APPLICATION [0002] This application relates to U.S. Provisional Application No. 60/337,361 filed November 5, 2001, and claims priority thereof.
BACKGROUND OF THE I1SJVENTION [0003] The present invention relates to the removal of contaminants, particularly to the removal of contaminants from an aqueous media, and more particularly to the removal of contaminating metals and organic compouncis from an aqueous media using solid material, which may be in the form of sol-gel and /or sol-gel and with solid support mixtures, which maybe in the form of granulated activated carbon (GAC).
[0004] In recent years, substantial effort has been directed to the removal of contaminants from an aqueous media, such as ground water. Numerous "Superfund" sites have been established because of contamination of ground water by various materials. The main contaminants are metals, particularly uranium and hexavalent chromium, volatile organic compounds (VOCs), high explosive compounds, nitrates, perchlorates, and tritium, as well as various commercial and manufacturing waste contaminants.
[0005] Presently, granular activated carbon (GAC), ion-exchanged resins, air-strippers, and bioremediation are used for contaminate removal. These work on many contaminants. However, there is not an readily available cost-effective remedy for uranium.
[0006] GAC has been commercially used as an adsorbent for contaminants in water. It is cheap and treatment technology hardware is readily available commercially for its use. Even though GAC is a good adsorbent medium for many contaminants, such as VOCs, it is not efficient for certain metals, particularly uranium. Thus, there has been a need for a material "by which contaminating metals and certain organic compounds may be removed from aqueous media.
[0007] The present invention provides a solution to this need by providing a material that can be used alone or with GAC to make it a good adsorbent for uranium, for example, without loosing the affinity for other contaminants. The material is a sol-gel and /or sol-gel and GAC mixture.
[0008] Sol-gels or aerogels, as commonly known, by themselves have not in the past been cost-effective to use. However, in an example of a composite, made in accordance with the invention, only 20% or less is an aerogel and the composite is a much better adsorbent for uranium than the aforementioned treatment technologies.
SUMMARY OF THE INVENTION [0009] It is an object of the present invention to provide for the removal of contaminant metals and organic compounds from aqueous media. [0010] A further object of the invention is to provide solid materials for removal of contaminating metals and organic compounds from aqueous media.
[0011] Another object of the invention is to provide for the removal of uranium from aqueous media.
[0012] Another object of the invention is to provide a material composed of a sol-gel and/or a sol-gel and a solid support mixtures for removing contaminating metals and organic compounds from aqueous media.
[0013] Another object of the invention is to provide a material composed of a sol-gel and/or a sol-gel and granulated activated carbon mixtures for removing contaminating metals and organic compounds from aqueous media.
[0014] Other objects and advantages of the invention will become apparent from the following description and accompanying drawings. The invention involves the removal of contaminating metals, such as uranium, and organic compounds from aqueous media. The invention involves a solid material that may be in molded, granular, or powder form, and the solid material adsorbs the metal and the organics leaving a purified aqueous stream. The solid materials are sol-gel and /or sol-gel and granulated activated carbon (GAC) mixtures. After adsorbing the contaminants, the contaminated solid material can be disposed of or the contaminant can be removed and the solid materials recycled. The species- specific adsorption occurs through specific chemical modifications of the solid materials tailored towards the contaminant(s).
BRIEF DESCRIPTION OF THE DRAWINGS [0015] The accompanying drawings, which are incorporated into and form a part of the disclosure, illustrate an embodiment of the invention and, together with the description, serve to explain the principles of the invention.
Figure 1 shows a Freundlich isotherm plot for baseline granulated activated carbon (GAC).
Figure 2 shows a Freundlich isotherm plot for a 1% phosphoric acid and hydrophobic aerogel/GAC composite.
Figure 3 shows a Freundlich isotherm plot for a 17% phosphoric acid and hydrophobic aerogel/GAC composite.
Figure 4 shows a Freundlich isotherm plot for a phosphoric acid exchanged hydrophobic aerogel/GAC composite.
Figure 5 shows a Freundlich isotherm plot for a functionalized phosphonate hydrophobic aerogel/GAC composite.
Figure 6 shows a column test for a functionalized phosphate hydrophobic aerogel.
DETAILED DESCRIPTION OF THE INVENTION 016] The present invention involves removing contaminating metals, such as uranium, and organic compounds from aqueous media use a solid material and fabrication method therefor. The invention utilizes solid materials and the contaminants are removed by passing the aqueous phase through the solid materials, which materials may be in molded, granular, or powder form. The solid materials adsorb the metals and the organics leaving a purified aqueous stream. The solid materials are comprised of sol-gel and /or sol-gel and a solid support such as granulated activated carbon (GAC) mixtures. The species-specific adsorption occurs through specific chemical modifications of the solid materials tailored towards the contaminant of choice, such as uranium. The contaminated solid materials can then be disposed of or the contaminant can be removed and the solid materials recycled.
[0017] The solid materials can be used to cleanup any aqueous stream with environmentally damaging material, such as caused by commercial interests or military activities. For example, but not limited to, ground water with uranium or heavy metal contamination, volatile organic compounds (VOCs) contamination, ground water with gasoline or other fuel spills, waste storage tanks with uranium or heavy metals, and ground water or surface waters "with petroleum product contamination or fuel spills.
[0018] The solid material of this invention may, for example, be composed of a silica sol-gel (aerogel) that has been modified to be hydrophobic and is activated by supercritical drying, and possible further modification is used separately or mixed with a solid support such as GAC, to remove contaminants, particularly uranium, from aqueous streams. The silica aerogel by itself in the past has not been cost-effective. However, in the composite with GAC, less than 20% of it is aerogel and the composite is a much better adsorbent for uranium of the afore-mentioned treatment technologies.
[0019] The aerogel/GAC composite is the preferred utilization being superior to previous treatment technologies, including GAC alone. GAC is a widely available commercial material that comes in many forms and from many sources. GAC by itself has been commercially used as an adsorbent for contaminants in water. It is inexpensive and the treatment technology hardware is readily available commercially for its use. It is a good media for adsorption of many other contaminants, such as VOCs, but without modification, it is not an efficient adsorbent of uranium. [0020] Aerogels are nano-structured materials having high surface areas (around 5O0 m2/g), low densities, and large meso pore structure. These nano-structured properties are configured in a three-dimensional structure giving ideal physical properties for adsorption. Through chemical modification, they can be designed to have species-specific binding, as well as discriminating bulk properties. Combining these properties, with the known adsorption properties of GAC as delineated by Tchobanoglous et al, Water Quality, Characteristics, Modeling and Modification, ISBN: 0-201- 05433-7 (1985), makes the aerogel/GAC composite ideal for treating environmentally important systems such as ground water.
[0021] The key to the superior performance of the aerogel/GAC composite is being able to tailor the aerogel to be specific for the particular target clean-up stream. This stream can be aqueous with metal ions, aqueous with organic compounds, aqueous with metal ions and organic compounds, non-aqueous with the above contaminants. The aerogel/GAC composite design will depend upon the all the components of the stream. This invention is not limited to aqueous streams with uranium in them, but simply uses that as an example of the design of the aerogel/GAC composite for the specific application.
[0022] In the design of this aerogel/GAC composite, the aerogel is tailored to be hydrophobic and specific for adsorbing uranium. The backbone of the aerogel is formed by the hydrolysis condensation of tetra methoxy silane, or tetra ethoxy silane more commonly known as silica sol-gel chemistry. This serves as an example of a method to make the backbone. Other commonly used methods found in the literature such as taught by Brinker and Scherer, Sol-Gel Science, The Physics and Chemistry of Sol-Gel Processing, ISBN: 0-12-134970-5 (1989), are also viable. The hydrophobic component is formed by the addition of, but not limited to, a fluorinated substituent through co-condensation reaction for an example. The trifluoropropyl group is used only to demonstrate the effect of making the hydrophobic character, not to limit the method of production. Reynolds, Recent Research Developments in Non-Crystalline Solids, ISBN: 81-7895- 028-6 (2001), teaches such common methods to make the material hydrophobic and other substituents found in the literature can also be used. The uranium adsorption site is formed by the incorporation of a uranium specific binding material into or onto the aerogel and/or the aerogel/GAC composite. Phosphoric acid, exchanged calcium nitrate, and diethyl phosphato ethylene triethoxy silane are used to demonstrate the viability of the approach. Other materials that have affinity for uranium can be used, preferably those materials that have affinity for other species in the cases where other metals and/or organics are targets for clean-up or separation. Other materials such as hydroxyapatite, calcium phosphate, and others can be used. The formation of the aerogel/GAC composite is made by combining the backbone, hydrophobic, and uranium binding components with the GAC. Co-gellation followed by supercritical extraction is an example, but not limited to, how this can be accomplished. 023] The following are examples of the solid material (aerogel) formulation of the invention in practice. These examples are not intended to be limiting nor necessarily optimum formulations. All samples were tested using a modified ASTM D 3860-98 method (Standard Practice for Determination of Adsorptive Capacity of Activated Carbon by Aqueous Phase Isotherm Technique). Stock solutions of uranium were prepared at either approximately 25, 50, or 100 ppb at pH 7 for sorption testing. Example 1: [0024] Baseline granulated activated carbon (GAC) was tested to establish the behavior of the adsorption industry standard for comparison. Figure 1 shows the Freundlich isotherm plot, and derived parameters are: n = 1.001, and _ = 20.05.
Example 2: [0025] 1% phosphoric acid and hydrophobic aerogel was prepared by the following method: 14.7 g (CHsO)4Si and 3.14 g (CHsO) 3SiCH2CH2CF3 were mixed together and to this mixture, 18.0 g CH3OH were added and stirred. In a separate vessel, 36.0 g CH3OH, 0.147 g H3PO4, 1.5 g HBF were mixed together and stirred. After about 1 min., both solutions were poured into a supercritical-drying reactor containing 13.4 g of GAC. A vacuum was pulled, and the mixture gelled in less than 1 hour. The gelled mixture was then supercritically dried at 300°C. Figure 2 shows the Freundlich isotherms and the derived parameters are: n = 1.685, Kf = 303.
Example 3: [0026] 17% phosphoric acid and hydrophobic aerogel was prepared by the same method as in Example 2 except 2.5 g H3PO4 was used. Figure 3 shows the Freundlich isotherms and the derived parameters are: n = 2.87, Kf = 1169.
Example 4:
[0027] Phosphoric acid exchanged hydrophobic aerogel was prepared by the following method: 35.0 g (CH30)4Si and 7.55 g (CH30)3SiCH2CH2CF3 were mixed together and to this mixture, 44.1 g acetone were added and stirred. In a separate vessel, 30.9 g H20, 85.7 g acetone, 7.46 g Ca(N03)2, O.lg HBF4 were mixed together and stirred. After about 1 min., both solutions were poured into a supercritical-drying reactor containing 96.2 g of GAC. A vacuum was pulled, and the mixture gelled in less than 1 hour. The gelled mixture was then supercritically dried at 300°C. The dry sample was removed from the supercritical reactor, sieved to remove fines, and mixed with a 5% H3PO4 in acetone solution for 5 to 10 min. The solvent was decanted off, and the solid was washed with pure acetone and dried under vacuum. Figure 4 shows the Freundlich isotherms and the derived parameters are: n = 1.666, Kf = 313.
Example 5: [0028] Functionalized phosphonate hydrophobic aerogel was prepared by the following method: 29.5 g (CH30)4Si, 6.3 g (CH3O) 3SiCH2CH2CF3, and 6.3 g (C2H50)3SiCH2CH2P(0)(OC2H5)2 were mixed together, and to this mixture, 36.0 g CH3OH were added and stirred. In a separate vessel, 17.5 g H20, 90.0 g CH3OH, 0.0175 g NH4OH were mixed together and stirred. After about 1 min., both solutions were poured into a supercritical-drying reactor that contained 8.49 g of GAC. The mixture was then supercritically dried at 300°C. Figure 5 shows the Freundlich isotherms and the derived parameters are: n = 0.715, Kf = 98.4.
Example 6: [0029] 50 g of the aerogel/GAC composite from Example 3 was tested in a column reactor. A 101 pCi/L uranium solution at pH 7 was treated in a up- flow configuration. Figure 6 shows the concentration of uranium in the effluent as a function of time on stream. The concentration was immediately reduced to 4 pCi/L and remained at that level through the entire run. [0030] It has thus been shown that the aerogel (sol-gel) and granulated activated carbon (GAC) mixtures or composites provide a significant increase in adsorption of metals (uranium) over that of GAC alone, or over aerogel material alone. Thus, this invention enables contamination cleanup of materials such as uranium in addition to contaminants that can be adsorbed by GAC alone, thereby enabling multiple contaminant removal with the same material.
[0031] While particular examples have been set forth with particular materials, times, etc. to exemplify and teach the prindples of the invention, such are not intended to be limiting. Modifications and changes may become apparent to those skilled in the art, and it is intended that the invention be limited only by the scope of the appended claims.

Claims

WHAT IS CLAIMED IS:
1. A material for removing contaminating metals and organic compounds from aqueous media, said material comprising a sol-gel and a solid support.
2. The material of claim 1, wherein the sol-gel and the solid support is a composite.
3. The material of claim 1, wherein said sol-gel and a solid support form a solid material selected from the group consisting of molded, granular, and powder form.
4. The material of claim 1, wherein the sol-gel comprises a hydrophobic sol-gel or aerogel.
5. The material of claim 1, wherein the solid support is granulated activated carbon (GAC).
6. The material of claim 4, wherein the hydrophobic aerogel includes a quantity of phosphoric acid.
7. The material of claim 4, wherein the phosphoric acid of the hydrophobic aerogel is in a range of < 1% to over 34 %.
8. The material of claim 4, wherein the hydrophobic aerogel includes a quantity of phosphonate.
9. The material of claim 8, wherein the phosphonate of the hydrophobic aerogel is in the form (C2H50)3SiCH2CH2P(0)(OC2H5)2.
10. The material of claim 4, wherein the phosphonate of the hydrophobic aerogel is in the range of < 1% to 50 %.
11. The material of claim 4, 'wherein the hydrophobic aerogel includes a quantity of phosphate exchangeable metal salt.
12. The material of claim 11, wherein the phosphate exchangeable salt is calcium nitrate.
13. The material of claim 11, wherein the phosphate exchangeable metal salt is in the range of < 1% to 50 %.
14. The material of claim 1, wherein the sol-gel is formed from a mixture which includes a quantity of (CH3θ)4Si and a quantity of hydrophobic component.
15. The material of claim 14, wherein the hydrophobic component of the mixture is a fluorinated material.
16. The material of claim 14, wherein the hydrophobic component of the mixture is (CH3θ)3SiCH2CH2CF3.
17. The material of claim 14, wherein the hydrophobic component is in the range of < 1% to 50%.
18. The material of claim 14, wherein the mixture additionally includes a quantity of one of CH3OH, acetone, and (C2H5θ)3SiCH2CH2P(0)(OC2H5)2.
19. A solid material for removing contaminants from aqueous media, comprising: a quantity of hydrophobic aerogel, and a quantity of GAC.
20. The solid material of claim 19, wherein the hydrophobic aerogel and the GAC comprises a composite material.
21. The solid material of claim 19, wherein the hydrophobic aerogel includes material selected from the group consisting of phosphoric acid, phosphonate, and phosphate exchangeable metal salts.
22. A method for producing a solid material for removing contaminants from an aqueous media comprising: providing a quantity of granulated activated carbon (GAC), providing material for producing a hydrophobic aerogel, and forming the solid material from the GAC and the hydrophobic aerogel producing material.
23. The method of claim 22, wherein the material for producing the hydrophobic aerogel includes material selected from the group consisting of phosphoric acid, phosphonate, and phosphate exchangeable metal salts.
24. The method of claim 23, wherein the forming includes preparing a first mixture containing at least (CH3θ) Si and
Figure imgf000015_0001
25. The method of claim 24, additionally including adding to the thus formed first mixture, a quantity of one of CH3OH, acetone, and (C2FT5θ)3SiCH2CH2P(0)(OC2H2)2.
26. The method of claim 25, additionally including forming a second mixture containing one of a quantity of CH3OH, H3PO4, and HBF4, a quantity of H2O, acetone, Ca(N03)2, and HBF4, and a quantity H20, CH3OH, and NH4OH.
27. The method of claim 26, additionally including mixing the first mixture and the second mixture together and stirred, followed by pouring into a supercritical-drying reactor containing a quantity of GAC, pulling a vacuum and gelling the mixed mixtures.
28. The method of claim 26, wherein the gelled mixed mixture is dried at 300°C under supercritical conditions.
29. The method of claim 26, additionally including removing the dried solid material from the supercritical reactor, sieving to remove fines, mixing with a quantity of H3PO4 in acetone solution for a time period, decanting off the solvent, washing the solid material, and drying under vacuum.
30. The method of claim 23, wherein the solid material is selected from the group consisting of phosphoric acid and hydrophobic aerogel, phosphoric acid exchanged hydrophobic aerogel, and functionalized phosphonate hydrophobic aerogel.
31. The method of claim 28, wherein the solid material consisting of phosphoric acid and hydrophobic aerogel contains phosphoric acid in a range of < 1% to about 34 %.
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