Patent Application
20240001308
The invention relates to systems and methods for removing explosives and other coexisting contaminants from water or wastewater.
Ammunition, particularly legacy munitions and insensitive high explosives (IHE), generally contains a variety of nitrated organic compounds: nitroamines [R2N—NO2, such as 1,3,5-Trinitro-1,3,5-triazinane (RDX, or hexagon), 1,3,5,7-Tetranitro-1,3,5,7-tetrazoctane (HMX, or octogen), and hexanitrohexaazaisowurtzitane (HNIW, or CL-20)], nitroaromatics [R—NO2, such as 2,4,6-trinitrotoluene (TNT), dinitrotoluenes (DNT), diazodinitrophenol (DDNP), and 2,4-dinitroanisole (DNAN)], and nitrate esters [R—O—NO2; such as pentaerythritol tetranitrate (PETN), nitroglycerin (NG), and ethylene glycol dinitrate (EGDN)]. These energetics (also referred to herein as “explosive compounds”) are widely used in a variety of munitions. For example, the Picatinny Arsenal Explosive 21 (PAX-21) is composed of RDX and 2,4-dinitroanisole (DNAN). Ammunition wastewater generally contains up to 200-500 mg/L RDX and HMX. Furthermore, these explosives have been introduced to soil and water around ammunition areas because of improper disposal of explosive-containing wastes. The explosives concentrations in the contaminated groundwater are in the thousands of micrograms per liter range.
These explosive compounds have adverse effects on a wide range of organisms, including algae, fish, and humans. For example, the Delaware Health and Social Services (DSS) reported that animal studies show HMX has adverse effects on the nervous system and liver. The United States Environmental Protection Agency (USEPA) has listed RDX, HMX, TNT, 2,4-DNT, and other nitrated explosives as priority pollutants. Additionally, the United States Environmental Protection Agency (EPA) risk assessments indicate that 0.3 μg/L and 30 μg/L RDX in drinking water concentration respectively represents a 10−6 and 10−4 cancer risk level. The recommended limit for the concentration of RDX in aqueous media is 300 μg/L, and a lifetime health advisory guidance level for RDX is 2 μg/L in drinking water. EPA also recommends that the concentration of HMX in an adult's drinking water be less than 0.4 mg/L.
Energetics usually occur in mixtures with oxyanions, such as ClO4−, NO3−, and CrO42−, in ammunition wastewater and explosive-contaminated groundwater. Ammunition wastewater can contain about 190 mg/L (˜2 mmol/L) ClO4−, as the explosives are often combined with perchlorate (ClO4−) to lower the sensitivity to the accidental explosion. ClO4− in the form of ammonium perchlorate (NH4ClO4−) is widely used as an oxidant and energetics booster in solid propellants for rockets, missiles, and fireworks. ClO4− is known to have adverse effects on the thyroid gland and its hormones secretion by interfering with the uptake of iodide (National Research Council 2005). ClO4− causes functional disruption of the thyroid and potentially leads to a reduction in the production of thyroid hormones, especially in infants and young children. The EPA has established an official reference Drinking Water Health Advisory of 15 μg/L and a tap-water screening level of 14 μg/L for perchlorate and its salts.
Munitions wastewater generally contains more than 100 mg/L NO3− (>2 mmol/L). NO3− is a public-health risk for causing cancer for the public and methemoglobinemia in infants below the age of six months. The maximum contaminant level (MCL) for NO3− set by the EPA is 10 mg-N/L to protect against and methemoglobinemia in infants. The World Health Organization has given an admission level for many industrial or human uses as less than 50 mg/L NO3−, which is approximately 11 mg-N/L.
Multiple physical, chemical, and biological techniques have been applied for the treatment of ammunition wastewater, including adsorption using activated carbon, alkaline hydrolysis, photocatalysis, photoelectrocatalysis, electrochemical oxidation, Fenton oxidation, zero-valent iron (ZVI) reduction, Palladium (Pd) catalyzed reduction, microbial reduction, and phytoremediation. Most of these technologies, however, are not successful in practical application due to their limitation in 1) mineralizing the explosives (i.e., complete conversion of the explosives to CO2 with minimal accumulation of harmful intermediates); 2) simultaneously removing all target contaminants (for examples, various explosives plus various oxyanions); and 3) minimizing energy cost caused by aeration and potential secondary contamination caused by adding organic carbon source. For example, none of the existing physiochemical approaches are able to convert the explosives completely to CO2 or remove oxyanions. Among these physiochemical approaches, oxidation-based methods, such as photocatalysis, hydrolysis, and Fenton oxidation, cannot treat oxyanions. Biological methods are able to oxidize the explosives, but reaction rates are extremely slow.
Accordingly, systems and methods that can overcome such roadblocks are needed for the removal of ammunition-related contaminants in water or wastewater.
The disclosure relates to systems and methods for synthesizing bio-metal composite catalysts, also referred to herein as a metal-biofilm. Also described herein are system and methods for treating water and wastewater using the bio-metal composite catalyst to ammunition-related contaminants. The systems and methods described herein offers a cost-effective, efficient, reliable, and sustainable option that satisfactorily treats IHE and legacy ammunition constituents with bio-metal composite catalysts. The targeted contaminants include, but are not limited to, oxyanions (such as nitrate, nitrite, perchlorate, chlorate, chromate, and selenate), explosives (such as RDX, HMX, CL-20, TNAZ, TNT, DNT, DNP, DDNP, DNB, DUNNITE, DNAN, TATB, PETN, NG, and EGDN), and other miscellaneous organic contaminants (such as trichloroethane (TCA), trichloroethene (TCE), and other halogenated compounds).
The technology also enables one-pot simultaneous removal of explosives and oxyanions, which solely physical-chemical or biological treatment technologies cannot accomplish on their own.
The system for establishing a metal-biofilm for removing ammunition-related contaminants comprise a gas-transfer membrane, a hydrogen-gas source, an inoculant comprising a biofilm-forming population of microorganisms, a growth medium comprising at least one nitrate salt and at least one perchlorate salt, and a catalyst precursor medium comprising at least one soluble autocatalytic metal precursor and having a basic pH. The growth medium feeds biofilm-forming population of microorganisms to establish a biofilm anchored on the gas-transfer membrane. The catalyst precursor medium feeds the biofilm, whereby the biofilm converts the soluble autocatalytic metal precursor to autocatalytic metal nanoparticles. The resulting autocatalytic metal nanoparticles are embedded in the biofilm matrices to produce a metal-biofilm that is anchored on the gas-transfer membrane.
Also described is a system for removing ammunitions contaminants from a fluid comprises a gas-transfer membrane, a hydrogen-gas source, autocatalytic metal nanoparticles; and a biofilm, wherein the autocatalytic metal nanoparticles are embedded in the matrices of the biofilm. The biofilm comprises a H2-utilizing autotroph capable of reducing oxyanions, a H2-utilizing autotroph capable of reducing precious metals, and a heterotroph capable of degrading organics.
Methods of establishing a bio-metal composite catalyst for removing ammunition-related contaminants are disclosed. In one embodiment, the method comprises providing an aqueous system, wherein the aqueous system comprises a gas-transfer membrane and a hydrogen-gas source and inoculating the gas-transfer membrane with an inoculant to establish a biofilm anchored to the gas-transfer membrane. The inoculated aqueous system is provided with a growth medium comprising at least one nitrate salt and at least one perchlorate salt to establishes a biofilm on the gas-transfer membrane. The method further comprises providing the aqueous system with a catalyst precursor medium comprising at least one soluble autocatalytic metal precursor and having a basic pH. The catalyst precursor medium feeds the biofilm, and the biofilm converts the soluble autocatalytic metal precursor to autocatalytic metal nanoparticles, which are embedded in the biofilm matrices to produce a metal-biofilm that is anchored on the gas-transfer membrane.
In another embodiment, the method for establishing a bio-metal composite catalyst for removing ammunition-related contaminants comprises providing an aqueous system, wherein the aqueous system comprises a gas-transfer membrane; a biofilm, wherein the biofilm is anchored to the gas-transfer membrane and comprises a H2-utilizing autotroph capable of reducing oxyanions, a H2-utilizing autotroph capable of reducing precious metals, and a heterotroph capable of degrading organics; and a hydrogen-gas source. The method further comprises providing the aqueous system with a catalyst precursor medium comprising at least one soluble autocatalytic metal precursor and having a basic pH. The catalyst precursor medium feeds the biofilm, and the biofilm converts the soluble autocatalytic metal precursor to autocatalytic metal nanoparticles, which are embedded in the biofilm matrices to produce a metal-biofilm that is anchored on the gas-transfer membrane.
Methods of removing ammunition-related contaminants in a fluid are also disclosed. In one embodiment, the method comprises providing an aqueous system, wherein the aqueous system comprises a gas-transfer membrane and a hydrogen-gas source; and inoculating the gas-transfer membrane with an inoculant to establish a biofilm anchored to the gas-transfer membrane. The method further comprises providing the inoculated aqueous system with a growth medium comprising at least one nitrate salt and at least one perchlorate salt, wherein growth medium establishes a biofilm on the gas-transfer membrane; and providing to the metal-biofilm the fluid with ammunition-related contaminants, wherein the metal-biofilm reduces the ammunition-related contaminants. In some aspects, the pH of the fluid with ammunition-related contaminants is a neutral pH. In other aspects, the method further comprises adjusting the pH of the fluid with ammunition-related contaminants to a neutral pH.
In another embodiment, the method comprises providing an aqueous system comprising a gas-transfer membrane, a hydrogen-gas source, and a bio-metal composite catalyst and providing to the aqueous system the fluid with ammunition-related contaminants, wherein the bio-metal composite catalyst reduces the ammunition-related contaminants. The bio-metal composite catalyst comprises autocatalytic metal nanoparticles embedded in the matrices of a biofilm. The biofilm is anchored to the gas-transfer membrane, and the biofilm comprises a H2-utilizing autotroph capable of reducing oxyanions, a H2-utilizing autotroph capable of reducing precious metals, and a heterotroph capable of degrading organics. In some aspects, the pH of the fluid with ammunition-related contaminants is a neutral pH. In other aspects, the method further comprises adjusting the pH of the fluid with ammunition-related contaminants to a neutral pH.
For the above-described methods and systems, the inoculant comprises a biofilm-forming population of microorganisms comprising a H2-utilizing autotroph capable of reducing oxyanions, a H2-utilizing autotroph capable of reducing precious metals, and a heterotroph capable of degrading organics. In some aspects, the inoculant comprises bacteria from the classes Betaproteobacteria, Alphaproteobacterial, and Saprospirae. In some embodiments, the inoculant comprises bacteria from at least one class selected from the group consisting of: Clostridia, Flavobacteria, Bacteroidia, and Methanobacteria. In other aspects, the inoculant comprises a member from Rhodocyclus, Rhizobiales, and Chitinophagaceae. In some embodiments, the inoculant comprises a member of Azospira, Rhodocyclaceae, Dysgonomonas, and Bacteroidales.
In some aspects of the above-described methods and systems, the concentration of the at least one soluble autocatalytic metal precursor in the catalyst precursor medium is 0.1-5 mM. In certain embodiments, the least one soluble autocatalytic metal precursor of the catalyst precursor membrane is selected from platinum group metals. For example, the autocatalytic metal nanoparticles are nanoparticles of elemental palladium (Pd0). In particular embodiments, the concentration of platinum group metal in the catalyst precursor medium is 2 mM.
In some aspects of the above-described methods and systems, the at least one nitrate salt in the growth medium provide a concentration of nitrate of at least 14 mg-N/L and the at least one perchlorate salt provides a concentration of ClO4− of at least 10 mg/L. for example, the at least one nitrate salt in the growth medium provides a concentration of nitrate of 14-48 mg-N/L and the at least one perchlorate salt provides a concentration of ClO4− of 10-200 mg/L. In particular embodiments, the growth medium comprises 300-350 mg/L NaNO3 and 240-245 mg/L NaClO4.
In some aspects of the above-described methods and systems, the hydrogen-gas source provides H2 gas mixed with CO2 gas at a mole ratio of 99:1 to 1:99. In some embodiments, the hydrogen-gas source provides H2 gas mixed with CO2 gas at a mole ratio of 95:5 to 50:50.
Detailed aspects and applications of the invention are described below in the drawings and detailed description of the invention. Unless specifically noted, it is intended that the words and phrases in the specification and the claims be given their plain, ordinary, and accustomed meaning to those of ordinary skill in the applicable arts.
In the following description, and for the purposes of explanation, numerous specific details are set forth to provide a thorough understanding of the various aspects of the invention. It will be understood, however, by those skilled in the relevant arts, that the present invention may be practiced without these specific details. It should be noted that there are many different and alternative configurations, devices, and technologies to which the disclosed inventions may be applied. The full scope of the inventions is not limited to the examples that are described below.
The singular forms “a,” “an,” and “the” include plural referents unless the context clearly dictates otherwise. Thus, for example, reference to “a step” includes reference to one or more of such steps.
As used herein, the term “explosives”, “explosive contaminants”, or “ammunitions-related contaminants” include 1,3,5-Trinitro-1,3,5-triazinane (RDX or hexagon), 1,3,5,7-Tetranitro-1,3,5,7-tetrazoctane (HMX or octogen), 2,4,6-trinitrotoluene (TNT), dinitrotoluenes (DNT), hexanitrohexaazaisowurtzitane (HNIW or CL-20), 2,4-dinitroanisole (DNAN), pentaerythritol tetranitrate (PETN), nitroglycerin (NG), 2,4-dinitrophenol (DNP), diazodinitrophenol (DDNP), 1,3-dinitrobenzene (DNB), ethylene glycol dinitrate (EGDN), triaminotrinitrobenzene (TATB), 1,3,3-trinitroazetidine (TNAZ), dunnite.
Disclosed herein are cost-effective, efficient, reliable, and sustainable methods of removing ammunitions-related contaminants from a liquid that satisfactorily treats insensitive high explosives (IHE) and legacy ammunition constituents with bio-metal composite catalysts. The targeted contaminants include, but are not limited to, oxyanions (such as nitrate, nitrite, perchlorate, chlorate, chromate, and selenate), explosives (such as RDX, HMX, CL-20, TNAZ, TNT, DNT, DNP, DDNP, DNB, dunnite, DNAN, TATB, PETN, NG, and EGDN), and other miscellaneous organic contaminants (such as TCA, TCE, and halogenated compounds). In some aspects, the fluid containing the contaminants is water or wastewater. Accordingly, also described are systems for treating water and wastewater using the bio-metal composite catalyst to remove ammunition-related contaminants. The methods and systems catalytically convert the explosives into less harm and more biodegradable intermediates. In some aspects, the methods and systems also biologically mineralize the intermediates into CO2 and converting the co-existing oxyanions into harmless forms. Unlike solely physical-chemical or biological treatment technologies, the described methods and systems enable one-pot simultaneous removal of explosives and oxyanions. The disclosure also describes system and methods for synthesizing bio-metal composite catalysts, referred to herein as a metal-biofilm. The disclosure is also directed to the metal-biofilm.
Compared to other physical-chemical treatment technologies such as advanced oxidation and photocatalysis processes, the methods and systems disclosed herein are capable of simultaneously removing in a single module organic explosives and inorganic oxyanions that co-exist in ammunition-contaminated water and ammunition wastewater. Additionally, the only reagent that needs to be continuously supplied is hydrogen gas (H2), which is inexpensive, nontoxic and can be generated on-site and on-demand. No input of energy-consumable or environmental-unfriendly reagents, such as UV light, ozone, hydrogen peroxide, or peroxysulfates, are required. Thus, the methods and systems described herein provide substantial saving of energy and cost in catalyst synthesis compared to conventional abiotic synthesis approaches with high energy input yet low catalyst yield.
Table 1 summarizes the improvements of described methods and systems over the existing technologies for removing ammunition-related contaminants.
The method for removing ammunition-related contaminants comprises establishing a metal-biofilm and thus for synthesizing bio-metal composite catalysts. To establish the metal-biofilm, a biofilm must first be established. Accordingly, the method utilizes a system comprising a gas-transfer membrane and a hydrogen-gas source. The system is provided with an inoculant comprising a biofilm-forming population of microorganisms and a growth medium so that the gas-transfer membrane is submerged with a solution containing the growth medium and the inoculant. The method further comprises feeding the inoculated system with the growth medium, wherein a biofilm is formed on the gas-transfer membrane from the inoculant. In some implementations, the inoculated system is fed with the growth medium at a hydraulic retention time (HRT) of 0.1-48 hours, preferably between 4 and 20 hours. In some preferred embodiments, the system was continuously fed with the growth medium for 2 to 8 weeks to ensure a robust biofilm is formed on the gas-transfer membrane.
Once the biofilm is formed, the system is provided with a catalyst precursor medium so that the gas-transfer membrane coated with the biofilm is submerged in the catalyst precursor medium. Feeding the system with the catalyst precursor medium results in the conversion of soluble autocatalytic metal precursors to autocatalytic metal nanoparticles, which are embedded into the biofilm matrices and serve as the catalyst for contaminant removal reactions. The resulting bio-metal composite catalyst film (“metal-biofilm”) on the membrane surfaces can treat explosive-contaminated water and wastewater. In some embodiments, the biofilm is in directly contacted with the catalyst precursor medium for 0.5-24 hours, preferably between 2-10 hours, to form the metal-biofilm. In a particular embodiment, the catalyst precursor medium comprises palladium (Pd(II)), for example, in the form of Na2PdCl4. In some aspects, the concentration of palladium in the catalyst precursor medium is 2 mM, and the pH of the palladium-containing catalyst precursor medium is around 9. In such embodiments, soluble Pd(II) was immobilized into the biofilm via adsorption, and the adsorbed Pd(II) was reduced to Pd0 nanoparticles. The Pd0 nanoparticles are embedded in the biofilm matrices. In certain embodiments, the Pd0 nanoparticles are 2-5 nm in major dimension, which provides high reaction area.
In view of the above, the system for establishing a metal-biofilm, which could be used to remove ammunition-related contaminants, comprises a gas-transfer membrane, a hydrogen-gas source, an inoculant comprising a biofilm-forming population of microorganisms, a growth medium, and a catalyst precursor medium. Accordingly, a system for removing ammunitions-related contaminants from a fluid comprises a metal-biofilm, a gas-transfer membrane, and a hydrogen-gas source. The meta-biofilm is anchored on the liquid-phase of the gas-transfer membrane, while the hydrogen-gas source provides H2 to the gas-phase of the gas-transfer membrane.
The methods for removing ammunition-related contaminants from a fluid further comprise providing a fluid comprising ammunition-related contaminants to the metal-biofilm, where the metal-biofilm reduces the ammunition-related contaminant. Thus, the systems for removing ammunition-related contaminants from water or wastewater comprise a gas-transfer membrane, a hydrogen-gas source, autocatalytic metal nanoparticles, and a biofilm, where the autocatalytic metal nanoparticles are embedded in the matrices of the biofilm. The running conditions for the method of removing ammunition-related contaminants from a fluid and the disclosed system may be optimized by adjusting the partial pressure of H2 provided to the metal-biofilm by the hydrogen-gas source and the HRT of system in relation to the concentration of the contaminants in the fluid, in particular the ammunition-related contaminants. For example, the higher contaminants concentration in the fluid, the higher the partial pressure of H2 or the longer HRT will be needed. In certain implementations the pH of the fluid is buffered to be around neutral pH to ensure the biofilm of the metal-biofilm is operating in an optimized environment.
The gas-transfer membrane does not have pores in its wall (e.g., a nonporous membrane). The lack of pores in the membrane enables transferring gas (e.g., hydrogen or oxygen) in a bubble-free form at controllable rates. In some embodiments, the membrane is a hollow-fiber membrane. In such embodiments, gas is supplied to the lumen of the hollow-fiber membrane (the gas-phase side). Accordingly, the biofilm and autocatalytic metal nanoparticles would be anchored to the outer surface of the hollow-fiber membrane (the liquid-phase side). In other embodiments, the membrane is a flat- or curled-sheet membrane. In such embodiments, H2 is supplied to one side of the sheet membrane (the gas-phase side), while biofilm and autocatalytic metal nanoparticles are anchored to the other surface of the sheet membrane (the liquid-phase side).
The membrane may be made of a variety of polymeric materials, for example polypropylene, polyurethane, polysulfone, or composite forms. In some embodiments, the membrane comprises polypropylene fibers and has a permeability of 1.8×107 m3 H2⋅m membrane thickness/m2 hollow fiber surface area⋅d⋅bar at standard temperature and pressure. In some aspects, the membrane of the system is nonporous, for example, the membrane lacks pores in its walls. In some embodiments, the outer diameter of the hollow fiber membrane is about 200 μm; the inner diameter of the hollow fiber membrane is about 100-110 μm; and the wall thickness of the hollow fiber membrane is about 50-55 μm.
In particular embodiments, the gas-transfer membrane is a nonporous polypropylene hollow-fiber membrane (200 μm OD, 100-110 μm ID, wall thickness 50-55 μm).
The hydrogen-gas source can be any reliable source of H2 gas, for examples, a gas storage tank having pressurized H2 gas, a H2 generator via water electrolysis, or a methane reformer. In other embodiments, the hydrogen-gas source include a built-in or external gas pressure regulator. The gas pressure regulator regulates the pressure of H2 gas from the gas storage tank to the gas-phase side of the membrane. In certain preferred embodiments, H2 gas is mixed with CO2 gas to balance pH and provide autotrophs in the biofilm with inorganic carbon sources. The H2 to CO2 mole ratio is set at a certain value in a range from 99:1 to 1:99. In some embodiments, H2 and CO2 are premixed at a certain mole ratio in a range of 95:5 to 50:50.
The hydrogen-gas source supplies the gas at between 18.0-28.0 psi, preferably between 19.0-28.0 psi, between 20.0-28.0 psi, between 19.0-24.0 psi, between 20.0-24.0 psi, between 20.0-23.0 psi, between 19.0-20.0 psi, between 18.0-20.0 psi, between 20.0-21.0 psi, between 21.0-22.0 psi, between 22.0-23.0 psi, between 23.0-24.0 psi, between 24.0-25.0 psi, between 25.0-26.0 psi, between 26.0-27.0 psi, between 27.0-28.0 psi, about 19.8 psi, about 21.8 psi, about 23.0 psi, about 23.8 psi, or about 27.2 psi.
The inoculant comprising a biofilm-forming population of microorganisms enables the formation of a biofilm that is anchored to the gas-transfer membrane. The biofilm-forming population of microorganisms comprises H2-utilizing autotrophs capable of reducing oxyanions, H2-utilizing autotrophs capable of reducing precious metals, and heterotrophs capable of degrading organics. For example, the biofilm-forming population of microorganisms comprises bacteria from the classes Betaproteobacteria, Alphaproteobacterial, and Saprospirae. In some embodiments, the biofilm-forming population of microorganisms further comprises bacteria from at least one class selected from the group consisting of: Clostridia, Flavobacteria, Bacteroidia, and Methanobacteria. In some implementations, the biofilm-forming population of microorganisms comprises Rhodocyclus, Rhizobiales, and Chitinophagaceae. In some aspects, the biofilm-forming population of microorganisms further comprises Azospira, Rhodocyclaceae, Dysgonomonas, and Bacteroidales.
Accordingly, the biofilm comprises bacteria from the classes Betaproteobacteria, Alphaproteobacterial, and Saprospirae. In some embodiments, the biofilm further comprises bacteria from at least one class selected from the group consisting of: Clostridia, Flavobacteria, Bacteroidia, and Methanobacteria. In some implementations, the biofilm comprises Rhodocyclus, Rhizobiales, and Chitinophagaceae. In some aspects, the biofilm further comprises Azospira, Rhodocyclaceae, Dysgonomonas, and Bacteroidales.
The growth medium stimulates sufficient microbial growth to establish and/or maintain the biofilm. The growth medium comprises at least one type of nitrate salts (for example, sodium nitrate) and salts of one or multiple other oxyanions (for example, sodium perchlorate and sodium chromate). The growth medium comprises high concentrations of the nitrate sand the oxyanion. In some aspects, the concentration of nitrate salt is 10-60 mg-N/L (44-266 mg/L NO3−), and the concentration of the oxyanion is 10-300 mg/L. For example, the concentration of nitrate salt is 10-55 mg-N/L, 10-50 mg-N/L, 10-49 mg-N/L, 10-48 mg-N/L, 10-47 mg-N/L, 10-46 mg-N/L, 10-45 mg-N/L, 14-60 mg-N/L, 14-55 mg-N/L, 14-50 mg-N/L, 14-49 mg-N/L, 14-48 mg-N/L, 14-47 mg-N/L, 14-46 mg-N/L, 14-45 mg-N/L, 18-60 mg-N/L, 18-55 mg-N/L, 18-50 mg-N/L, 18-49 mg-N/L, 18-48 mg-N/L, 18-47 mg-N/L, 18-46 mg-N/L, or 18-45 mg-N/L. The concentration of the oxyanion is, for example, 10-250 mg/L, 10-225 mg/L, 10-200 mg/L, 10-175 mg/L, 10-150 mg/L, 15-250 mg/L, 15-225 mg/L, 15-200 mg/L, 15-175 mg/L, 15-150 mg/L, 20-250 mg/l, 20-225 mg/l, 20-200 mg/L, 20-175 mg/l, or 20-150 mg/L.
In certain preferred aspects, the growth medium comprises salts of a full spectrum of macronutrients, such as calcium (Ca), magnesium (Mg), phosphorus (P), sodium (Na), potassium (K), and iron (Fe). In the preferred aspects, the growth medium also comprises salts of a full spectrum of micronutrients, such as zinc (Zn), manganese (Mn), boron (B), cobalt (Co), copper (Cu), nickel (Ni), molybdenum (Mo), and selenium (Se). In other preferred embodiments, the growth medium comprises mixed phosphate salts (for example, H3PO4, NaH2PO4, Na2HPO4, and Na3PO4) as pH buffers. In a particular embodiment, the growth medium comprises NaNO3, NaClO4, Na2HPO4, NaH2PO4, Ca(NO3)2, Mg(NO3)2, ZnSO4, MnCl2, H3BO3, CoCl2, CuCl2, NiCl2, Na2MoO4, and Na2SeO3.
In a particular embodiment, the concentration of NO3− in the growth medium is 14-48 mg-N/L, and the concentration of ClO4− in the growth medium is between 10˜200 mg/L. For example, the growth medium contains 340 mg/L NaNO3, 244.8 mg/L NaClO4, 994 mg/L Na2HPO4, 840 mg/L NaH2PO4, 1.66 mg/L Ca(NO3)2, 1.48 mg/L Mg(NO3)2, 0.1 mg/L ZnSO4.7H2O, 0.03 mg/L MnCl2.4H2O, 0.3 mg/L H3BO3, 0.2 mg/L CoCl2.6H2O, 0.01 mg/L CuCl2.2H2O, 0.01 mg/L NiCl2.6H2O, 0.03 mg/L Na2MoO4.2H2O, and 0.03 mg/L Na2SeO3.
The catalyst precursor medium comprises at least one autocatalytic metal precursors and a solvent. In some embodiments, the solvent is water, for example, deionized water. Autocatalytic metal precursors include, but are not limited to, gold (Au), silver (Ag), platinum (Pt), palladium (Pd), ruthenium (Ru), rhodium (Rh), osmium (Os), and iridium (Ir). In particular embodiments, the at least one autocatalytic metal precursor is selected from a metal in the platinum group metals. In some aspects, the autocatalytic metal precursors are chemicals that rapidly dissolve in the solvent and release soluble autocatalytic metal ions (for example, Ru3+ released from ruthenium chloride (RuCl3)) or soluble autocatalytic metal complexes of various ligands (for example, (PdCl4)2+ released from sodium tetrachloropalladate (Na2PdCl4)). The concentration of autocatalytic metal precursors in the catalyst precursor medium is between 0.01 mM and 100 mM. In certain preferred embodiments, the concentration of autocatalytic metal precursors in the catalyst precursor medium is 0.1-5 mM.
In particular embodiments, the catalyst precursor medium has a pH of between 4 and 10, for example, between 6 and 8. Accordingly, the autocatalytic metal medium may further comprise an acid (for example, hydrochloric acid), a base (for example, sodium hydroxide), and/or a pH buffer (for example, potassium phosphate species) to adjust the pH to a desired range.
Culturing the biofilm with the catalyst precursor medium converts the biofilm into a metal-biofilm that can remove explosives and oxyanions from a fluid with ammunition-related contaminants. The metal-biofilm is the biofilm with nanoparticles of the at least one autocatalytic metal immobilized within. The nanoparticles of the at least one autocatalytic metal is formed from the biofilm reducing the at least one autocatalytic metal precursor in the catalyst precursor medium. For example, in some implementations where the catalyst precursor medium comprises 2 mM palladium in the form of Na2PdCl4, soluble Pd(II) is immobilized into the biofilm via adsorption. The adsorbed Pd(II) is then reduced to Pd0 nanoparticles, which are retained on the microbial cell surfaces and extracellular polymeric substances (EPS) of the biofilm. The resulting biofilm containing Pd0 functions as the bio-metal composite catalyst.
The disclosure is further illustrated by the following examples that should not be construed as limiting. The contents of all references, patents, and published patent applications cited throughout this application, as well as the Figures, are incorporated herein by reference in their entirety for all purposes.
A bench-scale MPfR featuring bio-metal composite films was established in ambient conditions (23° C. and 1 atm). The system has a dual-tube design as shown in
The system was first inoculated with anoxic sludge from a local wastewater reclamation plant, and then it was filled with the growth medium containing 340 mg/L NaNO3, 244.8 mg/L NaClO4, 994 mg/L Na2HPO4, 840 mg/L NaH2PO4, 1.66 mg/L Ca(NO3)2, 1.48 mg/L Mg(NO3)2, 0.1 mg/L ZnSO4.7H2O, 0.03 mg/L MnCl2.4H2O, 0.3 mg/L H3BO3, 0.2 mg/L CoCl2.6H2O, 0.01 mg/L CuCl2.H2O, 0.01 mg/L NiCl2.6H2O, 0.03 mg/L Na2MoO4.2H2O, and 0.03 mg/L Na2SeO3. The system was left in batch mode overnight and then continuously fed with the growth medium for three months. Thick, mature biofilms had formed on the membrane surfaces after three months.
Denitrifying microorganisms had the dominant presence in the biofilm (
Perchlorates are usually utilized co-metabolically by denitrifiers, such as Dechloromonas, Azospira, and Clostridium spp. that are abundant in the biofilm. In addition, some non-denitrifying microorganisms like Dysgonomonas spp. in the biofilm are found capable of perchlorate reduction. The total abundance of these identified perchlorate-reducing genera was 19% in the biofilm.
The Dechloromonas genus have potential ability to respire other metals and previous study verified that it was a leading palladium-reducer in a H2-fed biofilm. The family Comamonadaceae (3%) and the order Rhizobiales (22%) are abundant in natural acidic environments contaminated by heavy metals [42, 43]. In addition, they were found to be enriched after exposure to precious metals and probably responsible for precious metal reduction. These groups, totally consisting of 25% of the biofilm, are potentially responsible for palladium catalyst synthesis and stabilization during the following stage of synthesizing bio-metal composite catalysts.
Bacteroidales (15%) are well reported anaerobic fermenters, and they likely survived in the biofilm by consuming byproducts from microbial metabolism. They are potential contributors to explosive mineralization via complete breakdown of the intermediates to CO2.
Once the biofilm matures, the bio-metal composite catalyst (also referred to herein as the metal-biofilm) could be synthesized. To form the bio-metal composite catalyst, a catalyst precursor medium was added into the system so that the biofilm would be fully immersed in the catalyst precursor medium. The catalyst precursor medium contains 2 mM palladium in the form of Na2PdCl4. The medium pH was set at around 9 using phosphate buffer. Soluble Pd(II) was immobilized into the biofilm via adsorption, and the adsorbed Pd(II) was reduced to Pd0 nanoparticles. The Pd0 nanoparticles are retained on the microbial cell surfaces and extracellular polymeric substances (EPS) of the biofilm. After 12 hours, over 99% of the Pd(II) was converted to nanoparticulate Pd0 stabilized in the biofilm matrix. The resulting biofilm containing Pd0 is subsequently referred to herein as Pd-biofilm, which functions as the bio-metal composite catalyst.
A series of batch tests were conducted to profile destruction of RDX, TNT, and PETN catalyzed by the Pd-biofilm. All the batch tests were conducted at pH of 7 and 25° C. in anaerobic conditions. The H2 pressure was set constantly at 20 psig (2.36 atm).
Further analyses of the organic intermediates reveal a map of all possible pathways for Pd-catalyzed RDX decomposition illustrated in
The NO2− decomposed from the RDX was sequentially reduced with Pd to create N2 or NH4+.
A series of batch tests of separated RDX, HMX, perchlorate, and nitrate removals were conducted in the biofilm before and after palladium addition (“biofilm” as the biocatalyst and “Pd-biofilm” as the bio-metal composite catalyst), and an abiotic bare fiber supporting Pd0NP film synthesized via autocatalytic reduction of Pd(II) in the same catalyst precursor medium (“Pd-film” as the metal catalyst). Pd-catalysis by Pd-film was only able to rapidly destroy explosives and could not reduce nitrate and perchlorate (
In a further test, a synthetic ammunition wastewater featuring RDX, HMX, nitrate, and perchlorate was successfully treated in a Pd-biofilm system within four hours (
4. Metal Catalysts Other than Pd for the Removal of Ammunitions-Related Contaminants
Similar to Pd, other platinum group metals (Pt, Rh, and Ru) can be autocatalytically reduced and embedded in the biofilm.
Bimetal catalysts, such as Pd/Pt, Pd/Ru, Pd/Rh, and Pd/Au, also can catalyze the reduction of energetics, with 10 mg/L energetics completely removed in 60 minutes. However, the catalysts with two metals had lower reduction rates than a catalyst film comprising Pd alone (5% ˜40% lower).
This application claims the benefit of U.S. Provisional Patent Application No. 63/115,017, filed Nov. 17, 2020, and incorporates the disclosure of the provisional application by reference thereto.
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/US21/59789 | 11/17/2021 | WO |
| Number | Date | Country | |
|---|---|---|---|
| 63115017 | Nov 2020 | US |
