Chloramines: How to Dose, What to Worry About
Transcription
Chloramines: How to Dose, What to Worry About
Chloramines: How to Dose, What to Worry About Presented by: Debra Cerda Drinking Water Quality Team Public Drinking Water Section TCEQ Public Drinking Water Conference August 9-10, 2005 Topics ! What are Chloramines? ! Why Change to Chloramines? ! Chemistry in Water < Of Chlorine < Of Chloramines ! Ratios & Dosing < Chlorine to Ammonia < Dosing for Different Types of Ammonia Topics (continued) ! ! ! ! The Balance & What’s at the Extremes? Health Effects One Extreme: Disinfection Byproducts Other Extreme: Nitrification < Why be concerned? < What is it? < How to prevent? Bonus Topics ! ! ! ! What to Look for & Where to Measure What to Do “When Ratios Go Wrong” Sources of NH3 Sequence of Injection What Are Chloramines? ! Chloramines -family of compounds used for disinfection. < Monochloramine -NH2Cl < Dichloramine - NHCl2 < Nitrogen trichloride - NCl3 ! Chlorine + Ammonia = Chloramines What Are Chloramines? ! Used in water treatment plants since 1930's ! Less effective than most other disinfectants and a weaker oxidant ! Use of chloramines results in decreased formation of many disinfection byproducts (DBPs) Why Change to Chloramination? Disinfection Byproducts of Chlorine ! TTHM = Total Trihalomethanes – Methane with three “halogens” on it – Halogen - Chlorine or Bromine molecule ! HAA5 = Haloacetic acids (group of 5) – Acetic acid with 1, 2, or 3 halogen molecules – Five are regulated ! Others not discussed today: HKs, HANs, CH How do they form? Every silver lining has a cloud ! Cl2 + Precursor = DBP < Chlorine reacts with carbon to form DBPs – Total Organic Carbon (TOC) is a surrogate for disinfection by-product precursors < More contact TIME leads to more DBPs < Higher TEMPERATURE makes more DBPs ! NOTE: You may not have to switch from chlorine if you optimize process control!! Special note for Texas: We have naturally occuring BROMIDE here ! Bromide Ion [Br-] – LOTS in E. Texas and Gulf (0.2 to 1.2 mg/L) Bromide Bromide ! Cl2 + Precursor (+Br-) = DBP < If you have more Br- . . . more DBPs Bromine’s Contribution to DBPs ! The Br! concentration in the source water is important, but is rarely measured. A few generalizations are helpful in assessing the likely relative concentration of bromide: Why Change to Chloramination? Other Disinfectants have Byproducts ! Chlorine Dioxide < Chlorite (ClO2) - Acute respiratory ! Ozone < Bromate (BrO3) - Strongly carcinogenic Starting With the Basics: Chlorination and Chloramination in Water Chemistry in Water: Chlorine ! Dissolution, Hydrolysis, and Dissociation Cl2 + H2O º HOCl + Cl- + H+ H+ Cl - (-) H O Cl O Cl Breakpoint Chlorination ! Addition of chlorine in quantities sufficient to first satisfy the chlorine demand (including the demand from nitrogen compounds originally in water), and then produce a free chlorine residual ! Results in free chlorine residual < Allows disinfectant properties of free chlorine to be fully utilized < Chloramination in drinking water treatment occurs following breakpoint chlorination 1. Readily oxidizable, simple components of source water consume chlorine 2. Chlorine reacts with organic and inorganic nitrogen in source water; monochloramine is formed 2 1 Combined Chlorine Residual 3. Transition zone - free chlorine residual created and destroyed at same rate; monochloramine formed 4. Residual is destroyed; di- and trichloramine formed and destroyed. 4 2 3 1 Combined Chlorine Residual 5. Breakpoint - all available nitrogen has been oxidized; free chlorine begins to persist 6. Free chlorine residual increases 6 4 2 3 Breakpoint! 5 Free Chlorine Residual (HOCl and OCl -) 1 Combined Chlorine Residual Breakpoint Chlorination & TCEQ ! Breakpoint chlorination (of raw water constituents) when chloramines are used as primary disinfectant < NH3 is added after this (raw water) breakpoint < Combines with free chlorine residual to form NH2Cl. < Ammonia (NH3) dose depends on free chlorine residual, NOT chlorine dose Applying the Concepts: Ratios ! If Cl2 goes in upstream (and it should for SW) < Chlorine residual (not dose) measured < Ammonia dose determined ! Why don’t we use chlorine dose? < Free chlorine reacts with chemicals other than NH 3 in source water < Iron, manganese, hydrogen sulfide, organic matter < Reactions result in: – A reduction in color, taste, and odor – Decreased amount of chlorine (HOCl) available to form chloramines Applying the Concepts: Ratios ! Other factors < How much excess Cl2 was present < pH - Effectiveness of chloramine disinfection fairly consistent for pH 7 -9 Applying the Concepts: Ratios ! Goal is to get a good Cl2:NH3 ratio < One mole of chlorine matched with one mole of ammonia to form monochloramine, NH2Cl Chloramination Chemistry H Cl N H H H N H H H O Cl H Cl Cl H N H Cl Cl Cl N N H Cl O Applying the Concepts: Ratios ! The key is the chlorine to ammonia ratio ! Forms of Chlorine: < Sodium Hypochlorite < Gaseous Chlorine ! Forms of Ammonia (NH3): < Anhydrous Ammonia (gas) < Ammonium Hydroxide < Ammonium Sulfate (solid) < Ammonium Sulfate (liquid) Chlorine: Ammonia (Cl2:NH3) Ratio ! Molecular weight < Cl2 has a molecular weight of 71 < NH3 has a molecular weight of 17 418 . lbsCl2 1 mol Cl 2 71 lbs Cl 2 = = 1 lb NH3 1 mol NH 3 17 lbs NH 3 (for anhydrous ammonia gas) Cl2:NH3 . 4:1 (by weight) to form NH 2Cl NH3 dose = ¼ of the Cl2 residual Chlorine: Ammonia (Cl2:NH3) Ratio ! Cl2:NH3 = 4:1 most commonly used for water treatment < At higher ratios: – NHCl2 and NCl3 concentrations increase – Higher production of DBPs < At lower ratios (less chlorine): – Chloramine is present as NH2Cl – Lower production of DBPs – Increased corrosion of copper and brass – Excess NH3 can lead to nitrification in distribution system Other Ammonia Sources ! Ammonium hydroxide < Solid ! NH4OH O H H H N H H H H N H H O O S O O H H ! Ammonium sulfate < Liquid or Solid H N H Chlorine: Ammonium Hydroxide Cl2:NH4OH Ratio ! Ammonium hydroxide < Cl2 has a molecular weight of 71 < NH4OH has a molecular weight of 35 1 mol Cl 2 71 lbs Cl 2 2.02 lbs Cl 2 = = 1 mol NH 4 OH 35 lbs NH 4 OH 1 lb NH 4 OH (for pure solid ammonium hydroxide) Cl2:NH4OH . 2:1 (by weight) to form NH 2Cl NH4OH dose = ½ of the Cl2 residual Chlorine: Solid Ammonium Sulfate Cl2:(NH4)2SO4 Ratio ! Ammonium sulfate < (NH4)2SO4 has a molecular weight of 132 < Ammonium sulfate ((NH 4)2SO4) has more “ammonia” (NH 3) than ammonium hydroxide (NH4OH) < Two molecules of Cl2 are needed 2 molCl2 1 mol(NH4 )2 SO4 142 lbsCl2 = 132 lbs(NH4 )2 SO4 108 . lbsCl2 = 1 lb(NH4 )2 SO4 (for pure solid ammonium sulfate) Cl2 :(NH4)2SO4 . 1:1 (by weight) to form NH 2Cl (NH4)2SO4 dose = the free Cl2 residual Liquid Chemicals (like LAS) ! Concentration is usually reported on a weight to weight (w/w) basis < 38% (w/w) ammonium sulfate means that 1 lb of the solution contains 0.38 lb of pure ammonium sulfate ((NH4)2SO4) < In other words, it is diluted, so we need to account for that in ratio ! Adjust the dose for feedstock concentration 108 . lbsCl2 1 lb ( NH4 )2 SO4 038 . lb ( NH4 ) 2 SO4 041 . lbs Cl 2 X = 1 lb LAS 1 lb LAS 38% LAS dose = 2.5 X the free Cl2 residual The Balance & What’s at the Extremes? ! If ratio has excess chlorine , higher disinfection byproducts (DBPs like TTHMs, HAA5s) ! If ratio has excess ammonia, nitrification ! Balance it out (work with the ratios) Balancing Risk Risk of waterborne disease Risk of cancer RISK DISINFECTION Health Effects Chloramines ! The ingestion of chloramines in drinking water poses little health risk to healthy people. ! Sensitive populations: < Dialysis patients < Aquatic organisms Health Effects Chloramines ! Dialysis < Method of cleaning the blood of people with kidney problems < Membrane system with blood on one side, tap water on the other; contaminants in blood transferred to water < Similarly, compounds (i.e., chloramine) are transferred from the water to the blood Health Effects Chloramines ! Chloramines in the blood cause damage to red blood cells, which can lead to hemolytic anemia < Dialysis patients are exposed to large amounts of water (70 - 80 times the amount normally ingested) < Therefore, dialysis patients could have high exposure to chloramines if water not filtered Health Effects Chloramines ! Aquatic organisms < Both chloramines and NH3 are toxic and can be fatal to fish < Chloramines bind to iron in blood cells and inhibit oxygen-carrying capacity Health Effects Chloramines ! Reducing the risk to sensitive populations < Chloramines can be removed from water by: – Granular activated carbon (GAC) – Green sand zeolite – Ascorbic acid (Vitamin C) < Notifying dialysis facilities and fish hobbyists and stores of changes to water due to chloramination can reduce risks – Allows implementation of treatment devices Health Effects Chloramines ! TCEQ approves use of chloramines on case-by-case basis – To receive approval, water utility must issue public notice to customers and notify hospitals and dialysis centers 14 days before converting to chloramines (a greater warning period is probably in best public/utility interest). Health Effects DBPs of Chloramines ! Chloramination creates fewer DBPs than free chlorine ! Some DBPs are formed in higher amounts with chloramines: < Cyanogen chloride – Irritation of eyes, skin, and respiratory tract < N-nitrosodimethylamine (NDMA) – Mutagenic, probable human carcinogen – Greater health concern than THMs – Present in higher concentrations in chloraminated water than in chlorinated water Health Effects DBPs ! NDMA not currently regulated, but due to potential health effects, some work is currently in progress to identify ways to remove NDMA from water < Air stripping, reverse osmosis, adsorption are NOT effective means for removal ! UV appears to be effective < Required dosage is higher than needed for viral < inactivation Modifications to UV systems / operation could be needed One Extreme: Disinfection Byproducts (DBPs) ! TTHM = Total Trihalomethanes < 0.080 mg/L MCL based on RAA < Carcinogenic, miscarriage (?) ! HAA5 = Haloacetic acids < 0.060 mg/L MCL based on RAA < Carcinogenic ! Stage 2 Disinfection Byproduct Rule-Locational Running Annual Average (RAA) Other Extreme: Nitrification ! Chemical Issues Biological Issues Disinfection Depletion Nitrite/Nitrate Formation Dissolved Oxygen Depletion Reduction in pH and Alkalinity DBP Formation due to Mitigation Techniques HPC Increase AOB Increase NOB Increase Other Extreme: Nitrification Chemical Issues Disinfection Depletion Nitrite/Nitrate Formation Dissolved Oxygen Depletion Reduction in pH and Alkalinity DBP Formation due to Mitigation Techniques Biological Issues HPC Increase AOB Increase NOB Increase Other Extreme: Nitrification ! Nitrite/Nitrate are acute health risks to infants up to six months of age < Methemoglobinemia (blue baby syndrome) ! Nitrite and bacterial growth consume disinfectant < Potential for violating Total Coliform Rule ! 1996 report estimated 63% of chloraminating utilities showed signs of nitrification in distribution system Nitrification ! Microbial process by which reduced nitrogen compounds (primarily ammonia) are sequentially oxidized to nitrite (NO2-) and nitrate (NO3) Nitrification ! Ammonia converted to nitrite by ammoniaoxidizing bacteria (AOBs) AOB NO2- NH3 ! Can then be converted to nitrate by nitrite oxidizing bacteria (NOBs) NOB NO2- NO3 Nitrifying Bacteria ! Ammonia-oxidizing Bacteria < Nitrosomonas most frequently identified < Nitrosococcus and Nitrosospira ! Nitrite-oxidizing Bacteria < Nitrobacter – Slow grower = process usually incomplete Sources of Free Ammonia ! Naturally occurring ! Ammonia addition for chloramination < Chloramine usage increase to reduce trihalomethanes and haloacetic acid formation ! Chloramine decay (Autodecomposition) < Monochloramine optimal Breakpoint Curve Monochloramine 5:1 3:1 4:1 >8:1 7:1 Added chlorine (fixed N) Increased Risk of Nitrification ! With temperature ! With increasing distance into distribution system ! Older pipes (tuberculation) ! Absence of sunlight ! As disinfectant demand increases ! Note: Nitrifying bacteria observed growing with chloramine residual as high as 1.5 mg/L Growth Conditions for Nitrifying Bacteria ! Temperature B B < Optimal 25 -30 C; Range of nitrification 8B -26B C ! pH < Optimal 7.0-8.0; Range 6.6-9.7 ! Chlorine to ammonia-nitrogen ratio of 3:1 ! Inadequate disinfectant residuals How to Minimize Nitrification ! Be PRO-active, not RE-active! ! Nitrification Monitoring Strategy ! Develop optimal preventative maintenance program ! Optimize process control (Bonus slides) Nitrification - Monitoring Strategy ! Parameters < Heterotrophic Plate Counts (HPCs) < Free and total ammonia < Nitrite and nitrate < Disinfectant dose and residual < Temperature < pH < DO, alkalinity, TOC, DOC < Fish Nitrification Monitoring Strategy ! Sampling locations: < Raw water < Finished water < Reservoirs < Dead-end mains < Routine coliform monitoring stations Nitrification Monitoring Strategy ! Use this data to establish baseline ! Watch for trends, for example: < PH decreasing < HPC increasing < Free ammonia decrease < Disinfectant demand increasing and residual decreasing < Nitrite increase Preventative Measures ! Short term < Periodic changes to free chlorine < Flushing programs ! Moderate < Reservoirs- Drain, clean, and inspect < “Pigging”- mechanically clean D.S. ! Long term < Booster stations to increase chloramine residual < Reservoir design and retrofitting Flushing Program “Shock” the System ! A reversion back to free chlorine may be needed each year for at least two weeks ! Notify before and after the flush < TCEQ so DBP samples delayed until the NH2Cl levels are reestablished. < The public to inform them of potential changes in the water quality and how it benefits them Flushing Program Unidirectional Flushing ! Proactively cleans the distribution system by displacing poor quality with high quality water while removing sediments and biofilms within system through scouring action Uni-directional Flushing ! Before starting: < Distribution Modeling- models the hydraulic and water quality behavior of water distribution piping systems. < EPA NET 2.0- FREE public domain software Benefits of Controlling Nitrification ! Disinfectant residual persists throughout the system ! Better protection against bacterial regrowth ! Lower chlorine and ammonia doses ! Lower maintenance and monitoring costs ! Public health protection Minimizing Nitrification - Summary ! Monitor water quality ! Limit growth conditions by controlling free ammonia ! Shock or flush system periodically to remove bioaccumulation Acronyms ! AOB - Ammonia-oxidizing bacteria ! DO - Dissolved oxygen ! DOC - Dissolved organic carbon ! FAA - Free Available Ammonia ! HPC - Heterotrophic plate count ! NH3-N - Ammonia as nitrogen ! NO2- - Nitrite ! NH2Cl - Monochloramine ! TOC - Total organic carbon ! NOB - Nitrite-oxidizing bacteria ! UDF - Unidirectional flushing Bonus Slides Applying the Concepts . . . in a practical way ! What do we need to measure to control the process? ! Where is the best spot to test for it? ! What results are we looking for? ! What do we do if we don't get them? What to Measure ! Free chlorine < To find out how much NH3 to apply ! Free Ammonia < To find out if we applied too much NH3 ! Monochloramine (our target disinfectant) ! Total Chlorine < To find out if we made any di- or trichloramines Plant Schematic Cl2 Cl2 Clarifier Mixer NH3 Cl2 NH3 Distribution Clearwell Where to Measure FAC Cl2 Cl2 Clarifier Mixer FAC FAC NH3 Cl2 NH3 Distribution Clearwell Where to Measure NH2Cl Cl2 Cl2 Clarifier Mixer NH2Cl NH3 Cl2 NH2Cl NH3 Distribution Clearwell Where to Measure FAA Cl2 Cl2 Clarifier Mixer FAA FAA NH3 FAA Cl2 NH3 Distribution Clearwell Where to Measure TAC Cl2 Cl2 Clarifier Mixer TAC TAC NH3 TAC Cl2 NH3 Distribution Clearwell What to Look For ! ! ! ! ! ! FAC = Target NH2Cl before adding NH3 Little change in FAA after NH2Cl forms FAA < 0.1 – 0.2 mg/L NH2Cl at the target Little change in TAC after NH2Cl forms TAC = NH2Cl “When Ratios Go Wrong” What to Do (Where to Start) ! NH2Cl too high < Reduce NH3 < Reduce Cl2 • FAA too high – Reduce NH3 – Increase Cl2 IT'S A BALANCING ACT • TAC dropped after NH3 addition – Increase NH3 – Reduce Cl2 • TAC > NH2Cl – Reduce Cl2 Sources of Ammonia (NH3) ! Anhydrous ammonia < NH3(g) ! Ammonium hydroxide < NH4OH ! Liquid ammonium sulfate (LAS) < (NH4)2SO4 Anhydrous NH3 ! Description < Gaseous form compressed into liquid. < Least expensive form of NH3. < Most commonly used. ! Storage < Never store Cl2 gas and NH3 gas in same room -potential formation of NCl3 (toxic). < TCEQ requires that anhydrous NH3 systems be housed and fed in separate enclosure from Cl2 system. Anhydrous NH3 - Feeders ! Feeders < Direct feed – NH3 injected directly to the water stream – Not common in Texas – Used for low-pressure water streams, low NH3 feed rates < Solution feed – NH3 mixed with dilution water prior to injection to water stream – Most common method in Texas – Used for high-pressure water streams, high NH3 feed rates Anhydrous NH3 - Safety ! Adequate ventilation should be provided in storage facilities. – Forced-air ventilation must be installed. – The switch for ventilation should be located outside enclosure so that ventilation can be turned on prior to entering the enclosure. – A ventilator must operate under positive pressure. – Intake fan draws air into bottom of enclosure. – NH3 discharged through high-level vent (unless containment / treatment desired). < NH3 gas is lighter than air and will accumulate near the ceiling. Anhydrous NH3 - Safety ! Safety equipment: < Safety shower and eye wash fountain < Industrial gas mask < One-piece rubber or neoprene suits < Rescue harness < High-pressure water system with fog nozzles < Vapor detection units at high points in storage and feeder areas Ammonium Hydroxide (NH4OH) ! Description < Formed by reaction of NH3 with water. < NH3 + H2O 6 NH4OH < Sold as 29-30% NH3 mixtures. ! Storage < Corrosive to some materials (i.e., copper, galvanized surfaces). < Usually stored in steel or fiberglass tanks. < Should be kept cool due to low boiling point. < The NH3 vapors that form at high temperatures should be controlled. Ammonia Hydroxide (NH4OH) ! Feeders < Direct feed of NH4OH to water stream < Stainless steel diffusers with backpressure ! Safety < Safer than anhydrous NH3 since use of pressurized container not required < NH3 vapors that form above NH4OH are potent – Adequate ventilation must be provided – Vapor detection units located at high points in storage area Liquid Ammonium Sulfate (LAS) ! Description < (NH4)2SO4 ! Storage < Corrosive < Storage equipment and feed systems should be resistant to H2SO4 < Should not be stored near reactive chemicals (i.e., Cl2 or lime) or sources of heat Lime LAS LAS ! Feeders < Direct feed of LAS to water stream < Design similar to NH4OH < Diffuser with backpressure ! Operation and maintenance < Control of corrosion and scaling, as necessary ! Safety < NH3 gas can be emitted from LAS. < Provide sufficient ventilation. < Safety equipment (i.e., goggles) should be used when handling LAS Sequence of Injection ! Prechlorination (adding Cl2 before NH3) < Achieves a free chlorine residual, which results in: – Increased disinfection (esp. viruses) compared to preformed chloramines. – Removal of color, taste and odors. – Potential for DBP formation. < Most common method of chloramine production. ! TCEQ requires that Cl2 (or ClO2, O 3) be used upstream of NH3 to get any viral inactivation credit for chloramine. Sequence of Injection ! Preammoniation < NH3 added before NH3 < Reduces DBP formation, but also disinfection capability, removal of color, taste, and odor < Not allowed by TCEQ unless another disinfectant is applied prior to NH3. ! Concurrent addition < Add NH3 and Cl2 at same time. < DBP formation lower than prechlorination < Disinfection capability higher than preammoniation < Not allowed by TCEQ unless another disinfectant is applied prior to NH3 Sequence of Injection ! Preformed chloramines < Mix NH3 and Cl2 in separate tank prior to addition to water stream. < NH2Cl solutions degrade with time and are difficult to preserve. < This method can result in higher concentrations of NCl3. < As a result, the use of preformed chloramines is not common. Sequence of Injection ! Systems who use ammonia MUST inject a strong oxidizer (usually chlorine) UPSTREAM from the ammonia. < Chlorine, chlorine dioxide, ozone ! Per EPA rule (footnote in table in guidance) ! There is no TCEQ minimum distance between injection points Sequence of Injection ! SWTPs who inject ammonia into raw water < Should switch immediately to correct sequence. < Get no inactivation credit for chloramine on their SWMORs during the time when ammonia was fed first. < Must resubmit SWMORs and get violations For More Info, Contact: Debra Cerda, DWQ Team Dcerda@tceq.state.tx.us (512) 239-6045 Amanda Jigmond, TROT Team Ajigmond@tceq.state.tx.us (512) 239-6006 Marlo Berg, TROT Team (512) 239-6967 Mberg@tceq.state.tx.us