ULTRA-PURE, READY-MADE CHLORINE DIOXIDE SOLUTION REMOVES BIOFOULING AND PREVENTS REGROWTH WITHOUT DAMAGE TO MEMBRANES Thomas E. McWhorter, CDG Environmental LLC., 301 Broadway Suite 420 Bethlehem, PA 18015 215-327-4748 [email protected] Introduction Published test results demonstrate that pure chlorine dioxide supplied in ready-to-use aqueous solution can remove bio-fouling and prevent its regrowth on TFC membranes and filters in reverse osmosis or ultrafiltration system without damage to membranes. Previous results showing membrane damage from chlorine dioxide are believed to be caused by impurities such as chlorine or chlorous acid in chlorine dioxide made at the point of use. Biofouling in Membrane Systems One of the biggest problems plaguing the fast-growing field of membrane-based water purification is bio-fouling. Bacteria and other microorganisms form a slimy layer that adheres to the surfaces of membranes, filters, pipes and other components of a reverse osmosis or ultra-filtration system. Biofilm consists of bacteria and other microorganisms bound together and to a surface by polysaccharide “glue”. Biofilm formation is especially problematic in water containing high levels of nutrients such as tertiary municipal wastewater and other wastewater streams. Biofilm blocks the flow of water through membranes and filters and necessitates frequent shut-down for off-line cleaning or replacement of elements. Off-line cleaning often results in damage to expensive membranes. Biofilm usually forms most quickly on the feed side of the membrane, but it can also form in the permeate stream or even within the membrane.1 Biofilm in the permeate stream can reach a thickness where it sloughs off, resulting in bacteria-laden particles in the product stream. Chlorine, hypochlorite, and related chemicals are not effective at controlling biofilm and can quickly damage membranes.1 Some disinfectants are only partly effective against biofilm in part because the disinfectants cannot penetrate the polysaccharide matrix. Therefore, when membrane performance is compromised by biofilm, the membrane must be taken off-line for mechanical cleaning and disinfection. During the shutdown for offline cleaning the total system must be shut down, causing loss of production, or a secondary set of membranes must be provided, often at substantial cost. Off-line disinfectants never remove 100% of the biofilm so biofilm re-seeds itself and grows back faster after every cleaning.1 1 2015 © American Water Works Association AMTA/AWWA Membrane Technology Conference Proceedings All Rights Reserved In many membrane systems the water is pre-filtered using cartridge filters to remove particles as small as a fraction of a micron before the water passes through the membranes. These filters are often subject to rapid bio-fouling by microorganisms that grow in the nutrient-rich media. This fouling usually necessitates shutdown and replacement of filter cartridges. Chlorine Dioxide Chlorine Dioxide (ClO2) has been used for more than 70 years in disinfection of drinking water and oxidation of certain drinking water contaminants. It is a broad range biocide and selective oxidant. In aqueous solution it reacts with other compounds by taking an electron to convert ClO2 (dissolved gas) to ClO2- (dissolved chlorite ion). Environmental Fate When ClO2 reacts in solution, it produces chlorite (ClO2-) and chloride (Cl-) ions. The USEPA has established standards for acceptable levels of ClO2 and ClO2- in drinking water and water discharged to the environment. Simple, off-the-shelf equipment is available to monitor the required parameters. Over time, in the presence of reducing chemicals, ClO2- reacts further to become Cl-. Thus the ultimate environmental fate of ClO2 is the generally benign chloride ion. Selective Reaction An example of chlorine dioxide’s selective oxidation capability is its ability to rapidly oxidize manganese from the water-soluble Mn-2 to the insoluble Mn-4 state without fully oxidizing the metal to produce soluble Mn-8 (permanganate). Many drinking water companies use chlorine dioxide in this reaction to convert dissolved manganese to particles that can be removed by filtration. ClO2 is also frequently used to replace chlorination in drinking water where chlorine reacts with organics in the feed water to produce trihalomethanes and haloacetic acids (THMs and HAAs) which are increasingly regulated as carcinogens. Chlorine dioxide does not chlorinate the hydrocarbons. Unlike chlorine, chlorine dioxide does not react with ammonia, which is often present in large concentrations in processed wastewater. Traditional ClO2 Manufacturing Options Historically, ClO2 was considered unstable. Popular wisdom was that it could not be shipped and must be produced at the point of use. When stored as a dissolved gas in water, the product lifetime usually ranged from hours to a few days. In such circumstances, chlorine dioxide in less than ton quantities was usually produced near the point of use in one of a variety of processes2. One of the most common processes is the “acid/chlorite” or two-component process in which an aqueous solution of sodium chlorite is mixed with one of a variety of acids (typically hydrochloric acid) in Reaction 1. Solutions of sodium chlorite are typically marketed as “stabilized sodium chlorite” and acid is marketed as “activator” for use in this reaction. 5NaClO2 + 4HCl => 4ClO2 + 5NaCl + 2H2O Reaction 1 2 2015 © American Water Works Association AMTA/AWWA Membrane Technology Conference Proceedings All Rights Reserved This reaction proceeds very slowly and typically produces substantial quantities of byproduct impurities such as chlorous acid (HClO2), as well as unreacted HCl. A second common manufacturing technique is the three component system that mixes sodium chlorite with hydrochloric acid and sodium hypochlorite (bleach) in Reaction 2. 2NaClO2 + NaOCl + HCl =>2ClO2 + 2NaCl + NaOH Reaction 2 This reaction overcomes some of the problems of Reaction 1. However, bleach (NaOCl) is notoriously unstable and the reactor must be frequently readjusted to accommodate variations in bleach concentration. As a result, the product usually contains impurities such as chlorine or NaOCl. The “Rio Linda” generator mixes aqueous sodium chlorite with gaseous chlorine in an eductor to produce chlorine dioxide in a water stream in the reaction 2NaClO2 + Cl2 => 2ClO2 + 2NaCl Reaction 3 Even slight mis-adjustments to this system can result in elemental chlorine in the resulting product and damage to membranes. The “Gas:Solid” system passes a stream of dilute chlorine gas over a matrix containing solid sodium chlorite. The resulting dilute chlorine dioxide stream produced by Reaction 3 is essentially 100% pure as long as the solid sodium chlorite is replenished frequently enough. If the solid sodium chlorite is not replenished as needed, chlorine gas will break through the bed and damage membranes. The processes described above represent the most commonly-used approaches to on-site production of chlorine dioxide at a scale up to one ton/day or so. It is clear that if any of these processes are used to produce chlorine dioxide for disinfecting membrane systems, the membrane can be exposed to damaging chemicals on an on-going basis and/or during upset conditions. Chlorine Dioxide for Disinfecting Membranes and Filters and Preventing Bio-fouling Chlorine dioxide has long been known as an effective disinfectant for removing and preventing biofilm and for cleaning membranes and filters.3 Low doses of chlorine dioxide (< 1ppm in most cases and typically 0.25 ppm) applied continuously, prevent the growth of biofilm and can penetrate polysaccharide slime to remove existing biofilm. Chlorine dioxide can also be useful in off-line cleaning of filters or membranes. Chlorine dioxide exists in water as a dissolved gas. Therefore chlorine dioxide introduced into a feed-water stream of a membrane will disinfect the feed stream and the feed side of the membrane. It will also permeate the membrane and kill any microorganisms within the structure of the membrane. Then it will be carried along with the permeate stream and disinfect the permeate side of the membrane and the product water. Chlorine dioxide can be introduced to an RO system upstream of cartridge filters and can greatly increase the useful life of cartridge filters by controlling or eliminating biofouling. In this application, chlorine dioxide passes through the cartridge filters and into the membrane modules where it disinfects and prevents biofilm on the membranes. 3 2015 © American Water Works Association AMTA/AWWA Membrane Technology Conference Proceedings All Rights Reserved Because chlorine dioxide is normally unstable, in the past it was always made near the point of use. The traditional processes for making chlorine dioxide always produced some level of chlorine contamination and/or contamination by other chemicals that can quickly damage membranes. Even chlorine dioxide generators that normally produced chlorine-free chlorine dioxide sometimes produced chlorine contaminants during process upsets. Though it was well-known3 that pure chlorine dioxide does not damage TFC membranes, the use of chlorine dioxide for disinfection of membrane systems was very limited. Ultra-pure Ready-to-use Chlorine Dioxide Solution Until recently, membrane manufacturers warned against use of chlorine dioxide for disinfecting membranes because chlorine-free chlorine dioxide was not available. A few years ago, CDG Environmental, LLC, of Bethlehem, PA developed a storage-stable, shippable chlorine-free chlorine dioxide solution containing 3000 ppm of ultra-pure chlorine dioxide in water. This patented disinfectant is marketed as CDG Solution 3000 by CDG. It is also marketed by distributors under different brand names. Solution 3000 is stable in storage and shipment with a shelf-life of 9 months or longer at room temperature. It is made in a patented process that includes dissolving ultra-pure chlorine dioxide gas in ultra-pure water under strict quality control monitoring. Concentrations of elemental chlorine in Solution 3000 are less than 10 ppm in 3000 ppm of dissolved chlorine dioxide. Thus, if Solution 3000 is used at a typical 0.25 ppm dose in a membrane system, elemental chlorine concentration in contact with membranes will be less than 0. 9 ppb (less than 1 part per billion). Examples of Membrane Test Results Many membrane users are adapting their systems to Solution 3000. A few have published the results of their testing. Published results of tests on full-scale commercial RO plants with TFC membranes have shown that the use of chlorine-free chlorine dioxide for disinfecting membrane systems often greatly reduces the operating cost of the membrane system. In one plant4, continuous application of chlorine dioxide at a dose of 0.20 – 0.25 ppm resulted in an increase in filter cartridge life from two weeks to eight weeks while simultaneously reducing pressure drop across the cartridges and allowing replacement of 5 micron cartridges with 1 micron cartridges. In the same plant, the chlorine dioxide passed through the filter cartridges and into the RO modules. Before chlorine dioxide use, the membranes were sent off-site for cleaning every 2-3 weeks. After the use of chlorine dioxide, the membranes did not have to be sent for off-site cleaning during the 12-month duration of the trial. Over the duration of the trial, there was no deterioration in permeate quality and no apparent oxidative damage to the membranes upon post-trial examination. As a dissolved gas ultra-pure chlorine dioxide passed through micro-filters and the membranes with essentially no change in concentration so the same chlorine dioxide dose controlled biological contamination and biofilm in the feed stream, the permeate stream and the reject stream. 4 2015 © American Water Works Association AMTA/AWWA Membrane Technology Conference Proceedings All Rights Reserved In another plant trial1, the use of chlorine dioxide resulted in increased flux through the membrane with negligible change in permeate conductivity over the 19-month trial. Of course, the success of chlorine dioxide in improving membrane performance is dependent on the extent to which bio-fouling is the limiting factor in membrane performance. The manufacturer or its distributors can be helpful for full-scale or pilotscale application testing as well as design guidelines on applications equipment, piping and other installation considerations. Shipping and Application Solution 3000 is shipped in ready-to-use polymeric containers ranging in size from 5 – 330 gallons. Containers can be supplied with specially designed Colder Fittings that permit connection and disconnection without exposing workers to volatile gas from the solution. The concentrated product 3000 can be metered into the process stream using standard metering pumps and off-the-shelf controls. Solution 3000 is storage-stable for at least nine months at room temperature and can be stored at temperatures ranging from 32oF to 140oF. References (1) (2) (3) (4) Dimotsis, George, Field trial experience using chlorine dioxide as cleaner for biofilm control in an RO application, Dripping Wet Water San Antonio, Texas Simpson, Gregory D. PhD, (2005), “Practical Chlorine Dioxide” pp 67-75 Dow Chemical Company Product Guideline (1998), Form No. 609-01010-498QRP CH 172-041-E-498 Zupanovich, John, Bishop David and Doak, Andrew, Chemtreat, Inc., Duff, Andrew, Covanta Energy (2012) “Microbiological Control in Thin Film Composite Membrane Systems Using a High Purity Chlorine Dioxide System” American Water Works Membrane Technology Conference Proceedings 5 2015 © American Water Works Association AMTA/AWWA Membrane Technology Conference Proceedings All Rights Reserved Chlorine Dioxide Solution Eliminates Biofouling without Damage to Membranes Tom McWhorter CDG Environmental LLC. AMTA/AWWA © 2015 © American Water Works Association AMTA/AWWA Membrane Technology Conference Proceedings All Rights Reserved 1 “Biofilm is the last great challenge in reverse osmosis system design and operation.” AMTA/AWWA © 2015 © American Water Works Association AMTA/AWWA Membrane Technology Conference Proceedings All Rights Reserved 2 Biofilm • Bacteria, algae, other microorganisms • Bound together and to surfaces with a polysaccharide “glue” • Lives and grows on nutrients in water • Most problematic in high nutrient streams like tertiary wastewater AMTA/AWWA © 2015 © American Water Works Association AMTA/AWWA Membrane Technology Conference Proceedings All Rights Reserved 3 Biofilm Effects • Clogs membranes and filters • Reduces flux through membrane or filter • Requires frequent shutdown for offline cleaning or replacement • Can penetrate membranes and grow on permeate side and inside membrane • Most biocides will not penetrate the film AMTA/AWWA © 2015 © American Water Works Association AMTA/AWWA Membrane Technology Conference Proceedings All Rights Reserved 4 Consequences of Biofilm • Clogs membranes and filters • Reduces flux and/or increases pressure requirements • Can grow inside membrane structure • Can penetrate membrane and enter permeate. AMTA/AWWA © 2015 © American Water Works Association AMTA/AWWA Membrane Technology Conference Proceedings All Rights Reserved 5 Shortcomings of Remedies • Most disinfectants cannot penetrate biofilm • Offline cleaning is expensive and may damage membranes. – Backup membranes and replacement of filters – Downtime – Not effective against embedded organisms – Does not remove 100% - grows back faster after every cleaning AMTA/AWWA © 2015 © American Water Works Association AMTA/AWWA Membrane Technology Conference Proceedings All Rights Reserved 6 Chlorine Dioxide • • • • Broad range biocide Effective at very low concentration Environmental fate is chloride ion Selective oxidant – Does not form THM or HAA – Does not react with ammonia – Does not oxidize bromide to bromate AMTA/AWWA © 2015 © American Water Works Association AMTA/AWWA Membrane Technology Conference Proceedings All Rights Reserved 7 Chlorine Dioxide • Exists as a non-ionic dissolved gas • Penetrates and destroys biofilm • Permeates membranes – Disinfects feed, permeate and waste stream – Disinfects inside membrane structure • Prevents biofouling of membranes, filters, piping and other wetted surfaces. AMTA/AWWA © 2015 © American Water Works Association AMTA/AWWA Membrane Technology Conference Proceedings All Rights Reserved 8 Chlorine Dioxide • Does not damage TFC (polyamide) membranes • Previously reported damage caused by chlorine and other contaminants • In the past pure chlorine dioxide was unavailable AMTA/AWWA © 2015 © American Water Works Association AMTA/AWWA Membrane Technology Conference Proceedings All Rights Reserved 9 Chlorine Dioxide • Traditionally unstable – made at point of use – Acid/chlorite reactors – Acid/chlorite/bleach reactors – Chlorine gas/chlorite reactors • All produce chlorine and/or other contaminants if not maintained and adjusted properly AMTA/AWWA © 2015 © American Water Works Association AMTA/AWWA Membrane Technology Conference Proceedings All Rights Reserved 10 New Chlorine Dioxide Supply • Ready-made solution • 3000 ppm chlorine dioxide + ultra-pure water • Storage stable for > 9 months at room temperature • Application requires only chemical feed pump • Essentially zero chlorine or other contaminants AMTA/AWWA © 2015 © American Water Works Association AMTA/AWWA Membrane Technology Conference Proceedings All Rights Reserved 11 Application • Delivered in plastic containers 5 – 330 gal. • Recommended 0.1 – 1.0 ppm chlorine dioxide continuously • Apply continuously upstream of filters AMTA/AWWA © 2015 © American Water Works Association AMTA/AWWA Membrane Technology Conference Proceedings All Rights Reserved 12 Case 1 Application • Tertiary treated waste water processed for cooling tower make-up • Chlorine dioxide applied upstream of filters • Applied at 0.1 – 0.25 ppm depending on seasonal factors AMTA/AWWA © 2015 © American Water Works Association AMTA/AWWA Membrane Technology Conference Proceedings All Rights Reserved 13 Case 1 Filter Results • Micro-filter changed 5 micron to 1 micron • Lower pressure drop across filters • Filter life improved from 12-14 days to 8 weeks AMTA/AWWA © 2015 © American Water Works Association AMTA/AWWA Membrane Technology Conference Proceedings All Rights Reserved 14 Case 1 Membrane Results • Lower membrane feed pressure with slower rate of increase • Membrane life approximately doubled • 15 months(25,000 ppm-hours) with no membrane damage – Based on rejection rate – Based on microscopic analysis – Accelerated lab testing shows similar result AMTA/AWWA © 2015 © American Water Works Association AMTA/AWWA Membrane Technology Conference Proceedings All Rights Reserved 15 Case 2- Application • Clarified river water • TFC Membranes • Continuous application to already fouled membranes AMTA/AWWA © 2015 © American Water Works Association AMTA/AWWA Membrane Technology Conference Proceedings All Rights Reserved 16 Case 2 - Results • Former DNBPA disinfectant ineffective • Chlorine-free chlorine dioxide does not damage membrane after 19 months • Flux increases, pressure declines approaching original performance • Chlorine dioxide concentration unchanged by passage through membrane AMTA/AWWA © 2015 © American Water Works Association AMTA/AWWA Membrane Technology Conference Proceedings All Rights Reserved 17 Conclusions • Pure chlorine dioxide does not damage TFC membranes at recommended doses. • Restores membrane performance • Effective for biofilm elimination • Chlorine dioxide permeates membrane AMTA/AWWA © 2015 © American Water Works Association AMTA/AWWA Membrane Technology Conference Proceedings All Rights Reserved 18 Plans • Accelerated test of long term effects on membranes • Other membrane materials and processes AMTA/AWWA © 2015 © American Water Works Association AMTA/AWWA Membrane Technology Conference Proceedings All Rights Reserved 19
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