UV Oxidation and Disinfection

UV Oxidation and Disinfection
UV Oxidation and Disinfection
UV Oxidation and Disinfection
UV Oxidation and Disinfection
UV Oxidation and Disinfection
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UV Oxidation and Disinfection Technical Information

"The Discovery and Subsequent Research of Cryptosporidium Inactivation"

"UV Experience for Inactivating Cryptosporidium in Surface Water Plants"

The disinfection of pathogenic microbes in drinking water has been largely successful over the last century due to the use of chlorination. However, research conducted in the 1970's revealed that by-products formed during the chlorination process are potentially carcinogenic and that there is a direct correlation between the concentration of chlorination by-products and the probability of certain cancers and other health problems. Following these discoveries, drinking water regulators have struggled to find a balance between the benefits of chlorination and the harmful side effects caused by chlorination, within the confines of technological and economic limitations.

In the U.S.A., the Surface Water Treatment Rule (SWTR) of 1989 mandates inactivation levels for giardia cysts and enteric viruses, and also sets treatment standards for Trihalomethanes (THMs). The SWTR provides guidance to drinking water facilities through "CT" tables that prescribe the inactivation efficacy of various processes under varying water quality conditions. By following this guidance, most water treatment plants were able to provide an adequate degree of disinfection while not compromising their Disinfection By-Product (DBP) limits and without requiring major changes to their plants. However, continuing DBP health effect research indicated that even the DBP standards required in the 1989 SWTR produced an unacceptable level of risk and the SWTR was amended in 1996 to further lower DBP standards. In addition, a major outbreak of cryptosporidiosis in Milwaukee in 1993, and other minor cryptosporidiosis outbreaks caused regulators to create a removal requirement for cryptosporidium oocysts in the 1998 Interim Enhanced Surface Water Treatment Rule (IESWTR) and most likely a disinfection requirement in the final ESWTR (LT2ESWTR). The new DBP standards have caused many plants to fall out of compliance, requiring either extensive plant modifications or new disinfection strategies. The LT2ESWTR will include a cryptosporidium disinfection requirement and many surface water plants will fall out of compliance due to the very poor efficacy of chlorination for cryptosporidium. Therefore, due to these apparently conflicting conditions, a void was created for a water treatment technology that is effective for protozoa and viruses, does not create DBPs, and is economically feasible.

UV technologies have long been known to be effective for viruses and bacteria in drinking water and guidelines for the disinfection of viruses exist in the Alternative Disinfectants and Oxidants Guidance Manual. However, UV was widely considered to be ineffective for encysted protozoa as it was thought that the UV light would not penetrate the cyst membrane, and since giardia is the controlling microbe for chlorine dose determinations, no reductions in chlorine usage could be gained by using UV. Therefore, UV Disinfection was not used for surface waters in North America.

New breakthrough research conducted by Calgon Carbon Corporation in 1998 however proved that UV disinfection is, in fact, very effective for inactivating cryptosporidium and giardia at low UV doses. Subsequent to Calgon Carbon's research, the USEPA created a UV subworkgroup to report to the Federal Advisory Committee (FACA) on issues and costs related to UV disinfection. In advance of new guidance manuals for UV disinfection, many utilities have begun to consider UV disinfection in their plants either as an additional barrier for protozoa disinfection or to get "CT" credits for UV for giardia so that chlorine doses can be lowered to meet the 1998 DBP standards.

Authors: Daniel Brooks, Gary Van Stone, and Wayne Lem, Calgon Carbon Corporation, Pittsburgh, Pennsylvania, USA.

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"Application of a Medium Pressure UV System for the Treatment of N-Nitrosodimethylamine (NDMA)"

N-nitrosodimethylamine (NDMA) was first detected in 1990 as a problem pollutant in drinking water wells at levels as high as 3,000 ppt in Elmira, Ontario, Canada. The waste from a large chemical plant over many years had led to the contamination of the drinking water wells for the community. After extensive evaluation and testing, it was determined that UV photolysis was the most effective treatment method which led to the installation of a Calgon 270 kW Rayox® UV system in 1991. The system has been continuously treating water to this day. At about the same time, NDMA was found in the drinking water on an Indian reserve in Ontario, and a similar UV system was installed to remove NDMA from that water. Since then NDMA has been detected as a pollutant in ground waters, surface waters, industrial effluents and wastewaters in many jurisdictions. Many sources have been identified, including chemical plants that manufacture pesticides and herbicides, rubber manufacturing plants, rocket fuel manufacturing plants and wastewater treatment plants.

Recently there has been considerable concern in California about the detection of NDMA in drinking water feed wells at levels as high as 900 ppt. NDMA was found to be a carcinogen in animals and assessed as a Class 1 carcinogen by the USEPA. It is currently listed as a priority pollutant on the US EPA National Priorities List. California has set an "action level" of 20 ppt for NDMA and treatment systems are required to treat to the detection limit of 2 ppt.

NDMA is often produced as a byproduct in the industrial use of dimethylamine (DMA). DMA is a semi-volatile organic chemical that is soluble in water and has been commercially used for several decades. For example, from the mid 1950's till April, 1976, it was manufactured and used as an intermediate in the production of 1,1-dimethylhydrazine, a storable liquid rocket fuel that contained approximately 0.1% NDMA as an impurity. In addition 1,1-dimethylhydrazine oxidizes to produce NDMA. DMA is also used for the inhibition of nitrification in soil, as a plasticizer for rubber and polymers, as a solvent in the fiber and plastics industry, an antioxidant, a softener of copolymers, and as an additive to lubricants. DMA is used in rubber processing where it reacts with nitrite to produce NDMA which can be present as a contaminant in the final rubber product.

N-nitrosodimethylamine is also present in many other products such as tobacco smoke and a variety of foods such as cheeses, soybean oil, canned fruit, various meat products, bacon, various cured meat, cooked ham, milk, fish and fish products, apple brandy, and other alcoholic beverages including beer.

NDMA is thermally stable in aqueous solutions, and conventional methods such as biological treatment, air stripping, and activated carbon are not effective for NDMA treatment. Since NDMA is photochemically labile, advanced oxidation technologies, based on irradiation with ultraviolet (UV) light, have been promoted for the removal of NDMA in contaminated waters. Direct UV photolysis readily destroys the compound and has been used commercially for over 10 years for the treatment of NDMA in contaminated groundwater.

In direct UV photolysis, a high powered lamp emits UV radiation through a quartz sleeve into the contaminated water. The photons of light are absorbed by NDMA resulting in breaking of the N-N bond in the molecule. The destruction of NDMA is therefore dependent upon the amount of UV light which is applied to the contaminated water and the UV wavelengths emitted by the lamp.

Authors: Wayne Lem, P.Eng., Calgon Carbon Corporation, Pittsburgh, Pennsylvania, USA.

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"Comparison of MS-2 Biodosimetry Challenge Results with Computational Fluid Dynamics Modeling for a UV Disinfection Reactor"

This project evaluated a medium pressure ultra-violet (UV) reactor downstream from a conventional surface water treatment plant to determine the UV dose delivered by the reactor. The data was compared with computational fluid dynamics (CFD) results under the same test conditions to determine if CFD could accurately predict the dose.

The UV disinfection reactor was challenge tested with MS2 coliphage at a flowrate of 200 gpm and 600 gpm. The CFD model gave excellent agreement at the 600 gpm case as the predicted dose was within 3% of the dose obtained by biodosimetry. The CFD dose for the 200 gpm case was high by about 17% compared to that observed by biodosimetry. In general, the CFD model was able to accurately predict the dose obtained by biodosimetry within 3%-17%. This is well within the range of error expected in biodosimetry experimentation. The model was tested over a wide range of both flow rate (200 and 600 gpm) and number of lamps operating (1 or 4 lamps) in a Calgon Carbon 4x1 kW Sentinel UV Disinfection Reactor.

CFD plays an important role for efficient reactor design at Calgon Carbon Corporation. CFD is currently being utilized to optimize the existing reactor designs with results showing that disinfection treatment efficiency gains of up to 25-35% can be realized. Future challenge studies incorporating these reactor modifications will be compared with CFD predictions.

Authors: Wayne Lem, P.Eng., Calgon Carbon Corporation, Pittsburgh, Pennsylvania, USA.

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"Scale-up of a Medium Pressure UV System for the Treatment of N-Nitrosodimethylamine (NDMA) and its Advantages Over Low Pressure UV Systems"

Recently there has been considerable concern in California about the detection of N-nitrosodimethylamine (NDMA) in drinking water at levels as high as 900 ppt. NDMA was found to be a carcinogen in animals and assessed as a Class 1 carcinogen. It is currently listed as a priority pollutant on the US EPA National Priorities List. California has set an "action level" of 20 ppt for NDMA.

NDMA is thermally stable in aqueous solutions. Conventional methods such as biological treatment, air stripping and activated carbon are not effective for NDMA treatment. NDMA is photochemically labile, so advanced oxidation technologies that are based on irradiation with ultraviolet (UV) light have been promoted for the removal of NDMA in contaminated waters. Direct UV photolysis readily destroys the compound and has been used commercially for over 10 years for the treatment of NDMA contaminated groundwater.

In this paper, the selection and scale-up considerations for UV systems designed to destroy NDMA are reviewed. A fundamental part of UV system selection involves an evaluation of medium pressure and low pressure UV systems. The differences between medium pressure and low pressure systems are discussed and system costs are compared.

The water evaluated for this discussion was an NDMA-contaminated drinking water at LaPuente Valley Water District treated through an ISEP® continuous ion exchange module for perchlorate removal. The stream was tested for the use of ultraviolet treatment in October 1998. The UV irradiations were carried out in a semi-batch 1 kW UV Rayox® reactor (Calgon Carbon Corporation). The treatment results from the 1 kW Rayox® reactor were used in Calgon Carbon's proprietary model to confirm the results expected in the full-scale system. The full-scale equipment, installed in December 1999, to treat a flowrate of 2,500 gpm consisted of two Calgon Carbon 12 lamp Rayox® UV Towers utilizing medium pressure UV lamps and a skid mounted peroxide dosing module. Ultimately, the full-scale system performed very closely to predicted results from lab scale efforts.

For virtually all large scale treatment applications, medium pressure UV systems are advantageous over low pressure systems when comparing the overall capital, installation, and operating costs for the project. While economics is a big determinant in system selection, other factors such as footprint, number of existing installations, reliability, and ease of maintenance must be included in the selection criteria. Taking into account all these factors, the Rayox® Tower, with its high efficiency medium pressure UV lamps, was able to achieve optimal performance for NDMA destruction with the lowest overall lifecycle costs.

Authors: Wayne Lem, P.Eng., Calgon Carbon Corporation, Pittsburgh, Pennsylvania, USA.

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"Inactivation of Cryptosporidium parvum by Medium-Pressure Ultraviolet Light in Finished Drinking Water"

The inactivation of Cryptosporidium parvum in finished drinking water by medium-pressure UV light (200-300 nm) has been investigated at both the bench scale, using a collimated beam apparatus, and at the demonstration scale, using a Calgon Carbon Corporation Sentinel™ system at the Mannheim Water Treatment Plant, Kitchener, ON, Canada. The viability of the oocysts was assessed using both in vitro (fluorogenic vital dyes (DAPI/PI) and maximized in vitro excystation) and in vivo (neonatal mouse infectivity) assays. In the bench-scale studies, a high degree of inactivation (>4 logs) was found at UV doses as low as 41 mJ cm-2, as assayed by neonatal mouse infectivity; whereas the in vitro surrogate assays showed little or no inactivation at this and higher doses. This indicates that the in vitro assays are unreliable and grossly overestimate the UV doses required to prevent infection by the oocysts in susceptible hosts. The demonstration studies, which were carried out under the NSF/EPA ETV Program, provided results that agreed very well with the bench-scale results and furthermore showed that a UV dose as low as 19 mJ cm-2 provided 3.9 logs inactivation of the Cryptosporidium oocysts.

Authors: James R. Bolton and Bertrand Dussert, Calgon Carbon Corporation, Markham, ON, Canada; Zia Bukhari, Thomas Hargy and Jennifer L. Clancy Clancy Environmental Consultants, Inc., St. Albans, VT .

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Visit the Calgon Carbon Engineered Solutions web site for technical papers and other decision-critical information about our Rayox® and Sentinel™ advanced oxidation and distillation technologies.



UV Oxidation and Disinfection

UV Oxidation and Disinfection
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