Perchlorate: Health Effects and Technologies for Its Removal from Water Resources
Abstract
:1. Introduction
1.1. Properties of Perchlorate
2. Uses of Perchlorate
3. Environmental Fate and Transport
4. Perchlorate in the Environment
4.1. Presence of Naturally Occurring Perchlorate
4.2. Theory of Origin of Natural Perchlorate
4.3. Presence of Perchlorate in Natural Waters
4.4. Perchlorate in Food Supplies
5. Analytical Methodologies
6. Regulatory Limits
7. Toxicity and Risk
7.1. Thyroid Function
7.2. Perchlorate Toxicity
7.3. Animal Toxicity Studies
7.4. Human Toxicity Studies
7.5. Ecotoxicity Studies
8. Natural Biodegradation
9. Treatment Technologies
9.1. Ion Exchange (IX)
9.2. Bioreactors
9.3. In situ Biodegradation
9.4. Other Processes
- Adsorption: Adsorption involves the use of adsorbent media such as granular activated carbon (GAC) or activated alumina to remove perchlorate. For sites that have groundwater containing contaminants other than perchlorate, previous experience shows the potential for the use of treatment trains consisting of standard GAC/ion exchange resins or tailored GAC [97]. Cationic surfactant-tailored activated carbon has been studied to remove perchlorate in a laboratory scale column test; perchlorate was removed to below detection levels and increased the breakthrough time up to 30 times longer than standard activated carbon [98].
- Membrane filtration: Membrane filtration treatment includes reverse osmosis (RO), nanofiltration (NF), ultrafiltration (UF) and electrodialysis (ED). Three main types of semi-permeable membranes have been evaluated for the treatment of perchlorate in groundwater which includes high pressure RO membrane, nanofiltration membrane and low pressure RO membrane. High pressure RO membranes (> 150 psi) have been observed to remove about 99.9% of perchlorate [99]. NF membranes have a nominal pore size of approximately 0.001 micron and require an operating pressure in the range of 80 to 150 psi. NF membranes have been found to allow particles such as salts to pass through them. UF membranes have a pore size of approximately 0.002 to 0.1 microns and operate at a lower pressure (30 to 100 psi). Tight UF membranes, having smaller pores than UF but larger than NF, have been found to be ineffective in treating perchlorate [2]. Liang et al. [100] conducted pilot scale studies to evaluate the performance of perchlorate removal by production sized RO, NF and UF membranes. RO and NF membranes were observed to consistently remove more than 86.7% of perchlorate while tight UF membranes proved to be ineffective. Addition of cationic surfactant to UF membrane did not prove to be effective; this resulted in plugging the membrane.
- Electrochemical reduction: Electrochemical reduction of perchlorate anion has been studied in a cell with a nickel working electrode and a platinum counter electrode in concentrated solutions of hypochlorous acid [102]. Lee and Kramer [103] examined titanium metal as a chemical reductant to remove perchlorate in water. The activation of titanium was achieved by eliminating the localized surface oxide film using electrochemically induced pitting corrosion. It was observed that a higher current increases the activity of pitting corrosion. This dissolves a higher concentration of transitory titanium metal ions in the vicinity of the pits, which results in a higher rate of perchlorate reduction. The surface of the bare Ti(0) inside the pits induces further electrochemical reactions and causes faster rate of chloride oxidation to chlorine by increasing the current.
- Phytoremediation: Phytoremediation is an in situ mechanism by which vegetation is used to treat perchlorate. The most successful plants in perchlorate degradation include French terragon, cottonwood, and willow. Under hydroponic conditions willows were observed to degrade perchlorate from 10,000 μg/L to below detection in about 53 days [9]. Other plants that have been successfully tested include salt cedar trees, bulbrushes, cattails and sedges. Perchlorate concentrations have decreased from 20 μg/L to less than 4 μg/L using constructed wetlands [2].
- Use of iron particles: Stabilized elemental iron nanoparticles have been studied to remove perchlorate [104]. The results showed that temperature played a critical role in perchlorate degradation process. Approximately 100% of perchlorate was transformed to chloride during the reaction without any detectable intermediate products. Kinetics of perchlorate reduction by elemental iron was examined at elevated temperatures using microwave heating and conventional block heating [105]. Results from microwave heating study showed that 98% of perchlorate was removed in one hour at 200 deg C. Similar results observed with block heater indicated that enhancement in the rate of perchlorate removal by elemental iron was mostly due to heat energy at a higher temperature. Gurol and Kim [106] investigated chemical reduction of perchlorate using iron and iron oxide under various conditions. The main result of their investigation was that the addition of metallic iron (100 g/L) combined with exposing the solutions to ultraviolet light at wavelengths < 185 nm achieved 77% reduction in perchlorate.
- Catalytic reactors: A preliminary study using a catalyst that efficiently uses hydrogen gas to reduce perchlorate completely to chloride has been reported [107]. The catalyst has been prepared by the addition of methylthrioxorhenium to a combination of 5% Pd-carbon powder. Initial batch studies have indicated complete reduction of perchlorate to chloride.
10. Conclusions
References
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Compound | Formula | Molecular weight (g/mol) | Density (g/cm3) | Physical appearance | Aqueous solubility at 20° C (103 mg/L) | Decomposition temperature (°C) / Reaction | Uses |
---|---|---|---|---|---|---|---|
Ammonium perchlorate | NH4ClO4 | 117.488 | 1.952 | Colourless or white orthorombhic and regular crystals | 217–220 | 150 | Energetic booster in rocket fuel. |
Sodium perchlorate | NaClO4 | 122.439 | 2.02–2.499 | Hygroscopic/deliquescent, white orthorombhic crystals | 2010 | 492 | Strong oxidizing agent used in explosive and chemical industries |
Potassium perchlorate | KClO4 | 138.547 | 2.5298 | Colourless crystal to white crystalline powder, hygroscopic | 7.5 to 16.8 | 440 | Solid oxidant for rocket production. |
Litium perchlorate | LiclO4 | 106.3906 | 2.428–2.429 | Deliquescent, white crystal | 375 | < 250–400 | Electrolyte in voltaic cells, synthesis of organic chemicals |
Perchloric acid | HClO4.2H2O | 223.21 | 2.21 | White, hygroscopic powder | Very soluble | 250 | Analytical, oxidizing and dehydrating agent. |
Application
| Potential release
| Remarks
|
---|---|---|
Agricultural uses | Chilean nitrates and potash ores | App. 75,000 tons fertilizer containing 0.01 wt% perchlorate used annually between 2002 and 2004. |
Solid propellants | Disposal of solid propellants, untreated liquid waste from hog out process, space shuttle and other solid fuel launch vehicles. | Perchlorate containing debris, scraps of solid propellants, rejected rocket motors not burned to completion. |
Munitions | Hydraulic washout of equipment in munition manufacturing, corrosion and subsequent degradation of casings. Expended munitions and simulators. | Systems containing perchlorate include fuses, flares, illumination rounds, simulators, grenades, etc.
Improper functioning/ incomplete propellant consumption and subsequent leaching. |
Fireworks | Firework based perchlorate residue | Contain up to 70 wt% potassium or ammonium perchlorate. |
Safety and hazard flares | Precipitation from flame manufacturing sites | Preliminary research suggests unburned and burned flares lead to 3.6 g and 1.9 g, respectively of perchlorate. Residue from burned flare containing leachable amount of 2000 μg/flare perchlorate [25]. |
Matches Commercial explosives | Release likely to be at production facility Use of unlined ponds to collect production derived wastewater in explosive manufacturing and accumulation of perchlorate containing sludge. Disposal of perchlorate containing wastes at open burn/open detonation resulting in perchlorate residue generation. Black powder manufacturing, storage leakage and disposal of bags and containers of perchlorate in landfill. At blasting site if detonation is incomplete. | -
Contain up to 30 wt% sodium/ammonium/potassium perchlorate as chemical sensitizing agent. |
Industrial uses | Release likely from production facility and handling of perchlorate containing compounds. | Uses include: Bleach activators in detergents, constituent in rust removers, perchloric acid for airbag inflators and processing rare earth element ores. |
Laboratory | Detergent based lab glassware cleaning agents such as Alconox, Liquinox have found to have up to 2.5 mg/kg perchlorate [2]. | Use in labs in industries, academia and defense settings. Groundwater contamination found to be associated with actinide research, high explosive synthesis and testing [26]. |
Sodium chlorate production | - | Electrochemical production of sodium chlorate can generate perchlorate as an impurity. |
Food studied
| Reference
|
---|---|
Drinking water (USA, Japan, China) | [3,23,24] |
Lettuce (concentrations ranging from 0.5 to 129 μg/kg in 116 of 127 samples) | [27] |
Laboratory studies on lettuce, tobacco, soybeans, alfalfa, tomato, cucumber | [28–30] |
Field studies on lettuce, winter wheat crops, alfalafa, watercress, chinaberry and mulberry trees, cucumber, cantaloupe and tomatoes. | [29–31] |
Cow’s milk (average perchlorate concentration 5.76 μg/L) | [27] |
Cow’s milk (concentration ranging from 0.47 to 11 μg/L) | [32] |
Human milk | |
(concentration ranging from 1.4 to 92.2 μg/L in 18 states, USA) | [29] |
(concentration ranging from 1.3 to 411 μg/L in Boston area, USA) | [34] |
Country/State
| PHG/MCLG (μg/L) | Proposed standard (μg/L)
| Action level (μg/L)
| Remarks
| Reference
|
---|---|---|---|---|---|
Canada | 6 | Guidance value | [39] | ||
USEPA | 15 | Interim drinking water health advisory level | [43] | ||
Arizona | 14 | Based on child exposures | [44] | ||
Oregon | 4 | - | [44] | ||
California | 6 | 6 | Notification level | [44] | |
New Jersey | 5 | Health based value | [2] | ||
Maryland | 1 | Advisory level | [44] | ||
Massachusetts | 2 | 1 | Advisory Level for children and other at-risk populations for Bourne | [44] | |
Nevada | 18 | Public notice standard | [44] | ||
New Mexico | 1 | Drinking water screening level | [44] | ||
New York | 5 | Drinking water planning level | [44] | ||
18 | Public notification level | ||||
Texas | 17
51 | Residential protective clean up level (PCL)
Industrial/commercial PCL | [44] |
Source of contamination
| Description | Performance
| Reference
|
---|---|---|---|
Ground water (Presence of nitrates and chlorinated solvents). | A non-regenerable Perchlorate-selective resin is used. The system operating flow rate 400 gpm. | Initial concentration 50 μg/L. Effluent concentration < 4 μg/L | [75] |
Drinking Water | A fixed bed, non-regenerable anion-exchange resin is used. | NA | [76] |
Groundwater (Plant Ion Exchange System (PIES) and Wash Ion Exchange System (WIES)) | The PIES included twelve single-use anion exchange columns in 4 parallel trains. The WIES included three single-use ion exchange columns in series. | Initial concentration 80,000 to 350,000 μg/L. Effluent concentration 500 to 2,000 μg/L. | [75] |
Drinking Water | A fixed bed, non-regenerable anion exchange system is used. The system consists of 10 ion exchange vessels, each loaded with a strong-base, quarternary amine resin, operating at 6,000 gpm. | Initial concentration 20 to 50 μg/L. Effluent concentration < 4 μg/L. | [75] |
Groundwater | A non-regenerable, nitrate- selective anion exchange system is used. Operating flow rate 10,000 gpm. | Initial concentration 15 μg/L. Effluent concentrations < 4 μg/L. | [75] |
Groundwater (other contaminant trichloroethane) | Six fixed bed, non-regenerable anion exchange systems are used. | Initial concentration 20 μg/L. Effluent concentration < μg/L | [75] |
Type of system
| Description
| Concentration (μg/L)
| Reference
|
---|---|---|---|
Upflow fluidized bed reactor | Water contaminated with perchlorate, nitrate and chlorinated solvents. The system consists of bioreactor, an UV oxidation system, an air stripper and a disinfection system. The bioreactor uses ethanol as feed. | Influent: 2,500
Effluent from bioreactor: < 4 | [75] |
Fluidized bed reactor | System consists of four primary and four secondary FBRs, using sand and GAC as media. | Influent: 200,000
Effluent: < 18 | [76] |
Fluidized bed reactor | Water contaminated with perchlorate, metals and volatile organics. FBR is inoculated with pre-conditioned GAC containing biosolids acclimated to perchlorate removal. Acetic acid and inorganic nutrients are added. Excess biomass is removed from media. | Effluent: <4 | [77] |
Hall bioreactor | System consists of baker tank, deaeration reactor, methanol tank, and patented Hall reactor. Hall reactor contains floating media (poly- urethane based sponge) cut into one-centimeter cubes. Media provides support to bacterial colonies. Methanol fed as carbon source. Temperature ranges from 8 to 35 deg C. | Influent: 300 to 1000
Effluent: non-detectable limits | [86] |
Upflow packed bed reactor | Use of a packed bed anaerobic bioreactor containing sand or plastic media. Acetic acid was constantly fed. Biological reactions initiated by bioaugmentation of the columns with perchlorate respiring bacterial strain Dechlorosoma sp. | Influent: 75
Effluent: < 4 | [90] |
Hollow fiber membrane bioreactor | The bioreactor consists of a bundle of hydrophobic hollow fiber membranes (polyurethane encased within microporous polyethylene) where hydrogen gas diffuses through and autotrophic biofilm is developed outside the membrane, where bacteria (dichloromonas sp. PCI) reduce perchlorate. | Influent: 55
Effluent: 2 | [91] |
Packed bed bioreactor | Laboratory scale treatment of groundwater contaminated with perchlorate and nitrate. The reactor was fed with a gas mixture of H2 and CO2 and inoculated with hydrogen oxidizing perchlorate degrading bacterium. | Influent: 75
Effluent: 25–30% reduction. | [89] |
Packed bed bioreactor | A pure perchlorate respiring isolate (KJ) and mixed culture was used. Acetate required by mixed culture was observed to be twice more than that required by pure culture. Detention time observed to reduce using pure isolate. | Influent: 20
Effluent: < 4 | [83] |
Anaerobic treatment | Domesticated sludge was used. Acetate was fed as carbon source. Bacteria exposed to DO were incapable of reducing perchlorate. Addition of little Fe(0) accelerated while Fe(II) inhibited perchlorate removal. | Reduced to non-detectable limits. | [92] |
Type of system | Material injected | Description | Perchlorate concentration | Reference |
---|---|---|---|---|
Injection | Corn syrup, ethanol | Substrates were used to flood the vadose zone and drive it anaerobic. | Reduction from 5000 to 500 μg/kg | [75] |
Injection | Emulsified Soy bean oil | A portion of the oil is trapped within the soil pores leaving a residual oil phase to support anaerobic biodegradation. | Initial: 10,000 μg/L
Final: 4 μg/L | [101] |
Barrier | Mushroom compost, soybean oil, wood chips | A series of trenches containing the substrates mixture. Shallow trenches are cut into limestone and designed to capture ground water and run off. | Initial 13,000 μg/L
Final: below detection limits | [76] |
Passive Injection | Lactate | Buffer added to the aquifer to increase ground water pH. | Over 95% reductions. | [76] |
Ground water recirculation | Citric acid | Recirculation design consists of single groundwater extraction well and rejection well. Chlorine dioxide used to reduce biofouling. | Initial: 530000 μg/L
Final: < 4 μg/L | [75] |
© 2009 by the authors; licensee Molecular Diversity Preservation International, Basel, Switzerland. This article is an open-access article distributed under the terms and conditions of the Creative Commons Attribution license (http://creativecommons.org/licenses/by/3.0/).
Share and Cite
Srinivasan, A.; Viraraghavan, T. Perchlorate: Health Effects and Technologies for Its Removal from Water Resources. Int. J. Environ. Res. Public Health 2009, 6, 1418-1442. https://doi.org/10.3390/ijerph6041418
Srinivasan A, Viraraghavan T. Perchlorate: Health Effects and Technologies for Its Removal from Water Resources. International Journal of Environmental Research and Public Health. 2009; 6(4):1418-1442. https://doi.org/10.3390/ijerph6041418
Chicago/Turabian StyleSrinivasan, Asha, and Thiruvenkatachari Viraraghavan. 2009. "Perchlorate: Health Effects and Technologies for Its Removal from Water Resources" International Journal of Environmental Research and Public Health 6, no. 4: 1418-1442. https://doi.org/10.3390/ijerph6041418
APA StyleSrinivasan, A., & Viraraghavan, T. (2009). Perchlorate: Health Effects and Technologies for Its Removal from Water Resources. International Journal of Environmental Research and Public Health, 6(4), 1418-1442. https://doi.org/10.3390/ijerph6041418