Chlorate, Perchlorate, and Bromate in Sodium Hypochlorite Disinfection System - A summary of formation, regulations and solutions By Jeny Shah and Naeem Qureshi (Progressive Consulting Engineers, Inc.) 30 MRWA TODAY Spring 2012 Almost all water systems in the United States that disinfect drinking water use some type of chlorine-based process, either alone or in combination with other disinfectants. With the prospect of a terrorist attack and the passage of the Public Health Security and Bioterrorism Response Act of 2002, many utilities have started using sodium hypochlorite in place of chlorine gas. These utilities are now finding that they have elevated levels of chlorate, perchlorate and bromate when they had none when they were using chlorine gas. Proposed federal regulation (i.e. the Drinking Water System Security Act of 2009, HR 3258) may impose significant burdens on the continued use of chlorine gas at drinking water utilities. This development could potentially result in the increase in the use of hypochlorite for disinfection. This will lead to introduction of perchlorate into a system that currently does not contain perchlorate. Utilities may be faced with a situation in which they are required to maintain perchlorate, bromate and chlorate concentration below federal and/or state MCL and at the same time be under the pressure to switch to sodium hypochlorite. As a result additional steps to reduce chlorate, bromated and perchlorate will be required. Sodium hypochlorite as a disinfectant has the following advantages: it can easily be stored and transported or it can be produced on-site and the dosage is simple. It is as safe and effective as chlorine gas for disinfection and maintaining chlorine residual in the distribution system. However, Sodium hypochlorite is a corrosive substance and when it comes in contact with air it disintegrates. Also it is not effective against Giardia Lambia and Cryptosporidium. As previously noted, sodium hypochlorite solutions contain many regulated and unregulated contaminants including bromate, chlorate and perchlorate (Asami et al, 2009; Greiner et al, 2008; Weinberg et al, 2003; Gordon et al, 1993). NSF/ANSI Standard 60 covers the chemicals used in water treatment including the disinfectant chemicals. These standards are developed to ensure that the treatment chemicals do not add unsafe levels of chemicals or contaminants to drinking water. Changes to Standard 60 are constantly under consideration. New changes that can impact the disinfection process are anticipated to go into effect in 2013. Although there may be other changes to Standard 60, those affecting sodium hypochlorite are of great importance to the water industry since it is the most widely used disinfectant after chlorine gas. The details about how these contaminants are formed and regulated is summarized in this article. e r SodiumHypochloriteFeedSystem New Jersey proposed maximum contaminant level (MCL) of 5 ppb. Minnesota does not have a standard for perchlorate at this time. The USEPA has issued an advisory limit of 15 ppb of chlorate per litre of water. NSF Standard 60 is expected to have a perchlorate limit established by January 2013. Consulting Engineers & Surveyors New Broadway Avenue Water Treatment Plant City of Saint Peter, Minnesota Perchlorate Perchlorate ion is an endocrine-disruption chemical that can affect the human thyroid system. Perchlorate is a product of decomposition of sodium hypochlorite. The levels of perchlorate increase with the age of the sodium hypochlorite solution. The perchlorate can also be found in raw water supplies due to improper disposal of wastes from the manufacturers of the rocket propellants. There is no regulation for perchlorate in drinking water at this time, however, several states have established regulatory limits for perchlorate in drinking water. Examples of the regulatory limits are: California 6 parts per billion (ppb); Massachusetts 2 ppb; and, Water supply and treatment, wastewater collection and treatment, municipal engineering, water resources engineering, land surveying and mapping. 507-625-4171 | www.bolton-menk.com Ten offices serving the upper midwest Spring 2012 MRWA TODAY 31 Chlorate Chlorate is formed when the bleach solution of sodium hypochlorite decomposes. Thermal decomposition of bleach is the primary source of chlorate. The concentration of chlorate increases during storage as a function of time, temperature, and a suite of chemical factors (Adam & Gordon, 1998; Gordon et al, 1995). There is no current federal regulation for chlorate, however, a regulatory standard is being considered for addition to Standard 60 by January 2013. Chlorate is included in the contaminant candidate list and will probably be included in the unregulated contaminant mandatory rule. Bromate Bromate is potent human carcinogen. It results from the oxidation of bromide via mechanism analogous to that of chlorate (Asami et al, 2009), although its concentration remains constant once the available bromide has been converted to bromate (Snyder et al, 2009). The maximum contaminant levels (MCL) standard for bromate in potable water plant effluents is 10 parts per billion (ppb). Bromate in drinking water comes from two different sources: 1. Hypochlorite manufacturing process – a. Bulk generation - Bromide ions are found in the salt used to make chlorine and sodium hydroxide. The two raw materials react to form sodium hypochlorite. Virtually all of the bromine in chlorine and the bromide in the sodium hydroxide quickly convert to bromate at the pH of sodium hypochlorite. As a result the addition of hypochlorite solution to water adds bromate to the finished water. 32 MRWA TODAY Spring 2012 b. On-site generation – The electrolysis process of the brine solution used in the on-site generation of sodium hypochlorite produces hypochlorite that contains bromate. The concentration of bromide varies tremendously in different salt sources. 2. Ozonation - Bromide ions can be present in both surface water and ground water supplies. When water containing bromide ions is exposed to disinfection using the Ozonation process, the reaction of bromide with ozone will produce bromate. At present the current maximum contaminant level of bromate allowed in the sodium hypochlorite is 69 parts per million (ppm), but is expected to reduced to 39 ppm by January 2013. Solution A quick solution to keep perchlorate and chlorate levels low is to quickly turnover the sodium hypochlorite storage. The graph below shows the effect of age on perchlorate in sodium hypochlorite based on the NSF study of 60 chemicals. Graph 1: Aging Effect of Sodium Hypochlorite Solution on Formation of Perchlorate. 4. Use fresh hypochlorite solution when possible. For utilities using an on-site generation system: use low-bromide salt to minimize the amount of bromide present in the brine. The conversion of a hypochlorite system to a chlorine gas system would eliminate the concern since perchlorate and chlorate are not present in chlorine gas. References Adam, L.C. & Gordon, G., 1999. Hypochlorite Decomposition: Effects of Temperature, Ionic Strength, and Chloride Ion. Inorganic Chem., 38:6:1299. Asami, M.; Kosaka, K.; & Kunikane, S., 2009. Bromate, Chlorate, Chlorite and Perchlorate in Sodium Hypochloroite Solution Used for Water Supply. Jour. Water Supply Res. & Technol.-Aqua, 58:2:107. Source: Best Management Practices for Sodium Hypochlorite by Dave Purkiss, March 23, 2011 – PowerPoint presentation. Frequent cleaning of the storage tank can prevent old sodium hypochlorite from remaining in the tank. Temperature reduction and/or dilution of the solution on receipt from the supplier can also reduce the formation of chlorate. An AWWA research team developed a plan to investigate the factors impacting the formation of perchlorate, bromate and other contaminants in hypochlorite solutions. They then developed a set of guidelines or recommendations to assist utilities in minimizing the formation of such contaminants. The AWWA report (Snyder et al., 2009) provides the following recommendations to reduce or lower the formation of chlorate and perchlorate in the system: 1. Store hypochlorite solutions at a lower temperature as higher temperatures speed up the chemical decomposition of hypochlorite and results the subsequent formation of chlorate and perchlorate. Every 5oC reduction in storage temperature will reduce the rate of perchlorate formation by a factor of approximately 2. Gordon, G.; Adam, L.C.; & Bubnis, B.P., 1995. Minimizing Chlorate Ion Formation in Drinking Water When Hypochlorite Ion is the Chlorination Agent. Jour. AWWA, 87:6:97. Gordon, G.; Adam L.C.; Bubnis, B.P.; Hoyt, B.; Gillette, S.J.; & Wilczak, A., 1993. Controlling the Formation of Chlorate Ion in Liquid Hypochlorite Feedstocks. Jour. AWWA, 85:9:89. Greiner, P.; McClellan, C.; Bennett, D.; & Ewing, A., 2008. Occurrence of Perchlorate in Sodium Hypochlorite. Jour. AWWA, 100:11:68. Snyder, S.A.; Stanford, B.D.; Pisarenko, A.N.; Gilbert, G.; & Asami, M., 2009. Hypochlorite – An Assessment of Factors That Influence the Formation of Perchlorate and Other Contaminant. AWWA and Water Research Foundation Rept. www.awwa.org/files/GovtPublicAffairs/PDF/HypochloriteAssess. pdf (accessed May 23, 2011). Weinberg , H.S.; Delcomyn, C.A.; & Unnam, V., 2003. Bromate in Chlorinated Drinking Waters: Occurrence and Implications for Future Regulation. Envir. Sci. & Technol., 37:14:3104. 2. Control the pH of stored hypochlorite solutions at a pH of 11-13 even after dilution. 3. Dilute stored hypochlorite solutions upon delivery since the decomposition of hypochlorite and subsequent formation of chlorate and perchlorate is dependent upon hypochlorite concentration and ionic strength. A higher ionic strength and hypochlorite concentration will lead to greater production of chlorate and perchlorate. For example: diluting a 2 molar hypochlorite solution by a factor of 2, the rate of perchlorate formation decreases by a factor of 7; a four-fold dilution will decrease the rate of formation by factor of 36; and a ten-fold dilution will decrease the rate of perchlorate formation by a factor or 270. PROGRESSIVE CONSULTING ENGINEERS, INC. • • • • Civil Engineering Water Treatment Water Supply Rate Studies 2 MG Tower, Ramsey, MN (763) 560-9133 (763) 560-0333 Fax [email protected] 6120 Earle Brown Drive, Suite 629 Minneapolis, MN 55430 5,500 gpm WTP, Blaine, MN Spring 2012 MRWA TODAY 33
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