Operation of Photovoltaic Electro-Chlorination Process in Salt Water
Transcription
Operation of Photovoltaic Electro-Chlorination Process in Salt Water
Operation of Photovoltaic Electro-Chlorination Process Khouzam Operation of Photovoltaic Electro-Chlorination Process in Salt Water Pools K.Y. Khouzam School of Electrical and Electronic Systems Engineering Queensland University of Technology GPO Box 2434 Brisbane 4001 AUSTRALIA E-mail: k.khouzam@qut.edu.au Abstract Chlorine is used in swimming and spa pools to oxidise organics, to kill bacteria and to control the growth of algae. In this project, direct coupled photovoltaic power was applied to an electrolytic cell to produce liquid chlorine using brine of sodium chloride. Tests were conducted to investigate the effect of applied voltage, current, salt concentration, water flow rate, and duration of chlorination. Seven photovoltaic (PV) chlorinator installations were completed over the past twelve months in public and private pools. Results showed that proper matching can be achieved by carefully selecting the PV array parameters with respect to the load parameters. Also, the variation in solar radiation matches well the need for chlorine production and usage during the day. Using photovoltaics for salt-water chlorination is an effective way to semi-automate the input of chlorine into the swimming pool. If adopted, PV-based chlorinators promise a cheaper and cleaner alternative to mains power. INTRODUCTION Chlorine is a standard agent for sanitation in swimming and spa pools. Various compounds of liquid and dry chlorine additives are available in the market. Alternatively, liquid chlorine (sodium hypochlorite) can be produced using salt-water chlorinators by the electrolysis of salt (sodium chloride). This involves the passage of direct current through salty water to produce chlorine gas at the positive electrode. The amount of chlorine produced is proportional to the amount of charge passing in the electrodes. Salt-water chlorinators have been in the market for over twenty five years and their technology is well mature. In Australia, over 80% of swimming pools rely on salt water chlorination. In fact, all industrial chlorine production uses exactly the same technique used by the salt-water chlorinator. Conventional chlorinators use a rectifier to convert 240 V to low volt direct current to power the electrolysis plates. Tests showed that the efficiency of commercially available power converter units is around 50%. A research grant was funded under the Queensland Sustainable Energy Innovation Fund (QSEIF), to develop a photovoltaic (PV) source for the production of chlorine. The system must offer the same level of performance (if not better) as offered by commercial units. The PV chlorinator system must be simple to operate; safe and cost effective in order to compete with mains powered chlorinators. The project was able to work with Allchlor Repairs Pty Ltd, an industry partner to trial the application of photovoltaic to electro-chlorination and to progress the system into commercialisation. Through this project it is planned to: • • • • Design and install a number of PV chlorinator systems for water treatment in public and private swimming pools. Monitor and analyse chlorination parameters, along with solar radiation and pool usage. This will be used to get customer feedback on the performance of PV chlorinators. Prepare a business plan for marketing and commercialisation of the PV chlorinator system Develop a commercial turnkey product packages for residential and public swimming pools suitable for Australian and overseas markets. Destination Renewables - ANZSES 2003 Reviewed as full paper 297 © copyright 26 to 29 November Operation of Photovoltaic Electro-Chlorination Process Khouzam HISTORY OF WATER CHLORINATORS Australia, with a high standard of living, and with favourable climate, is a large market for the sales promotion of swimming pools. With the introduction of salt-water chlorinators in early seventies and to persuade prospective pool buyers, some pool builders offered a salt-water chlorinator as an option when the pool was to be built. Nowadays, there are approximately 25,000 in-ground pools added each year in Australia, and many are fitted with a chlorinator as standard equipment. Many old pools are also upgraded, with the result that around 75% of residential pools benefit from salt chlorination. Pools using salt chlorination have a concentration of approximately 0.4% to 0.8%. Salt is periodically added since the salinity level may drop due to flooding, or when water is lost through overflowing. Evaporation of water will only concentrate the salt level and will be diluted with water. The simple chemical reaction is given by: Salt + Water + DC current = Sodium Hypochlorite + Hydrogen With modern pumps, filters, heaters, PVC plumbing and other equipment, the salt-water chlorinator has become a reliable and standard part of the Australian swimming pool market. Apart from its sanitising effect, a salt water chlorination system offer the following advantages: • • • • Automatically produces chlorine whenever the system is switched on, thereby eliminating the daily chore of adding dry or liquid chlorine and eliminating the risk of storing chlorine additives. Costs less than liquid or granular chlorine additives and gives water a sparkle and pleasant appearance. Eliminates skin irritation and health-related problems with prolonged bathing and helps relieve tense muscles. Causes much less strain on the eyes than ordinary pools (study by School of Optometry at QUT). Salt-water chlorinators require high current low volt (7 to 9 V) direct current to operate the electrolytic process. This is provided by an inefficient power supply, which converts 240 V alternating current to low volt uni-directional current. Water must generally be pumped into the electrolysis unit (called in-line system). The electrode plates are made of titanium with the anode often coated in platinum. Platinum serves as an effective catalyst, that speeds up chemical reactions but is not itself changed in the reaction. Photovoltaic cells produce dc power when exposed to solar radiation. Cells are connected in parallel and in series to form PV modules to produce the required voltage and current. Experiments showed that proper matching between the characteristics of the PV panel and the chlorinator load could be achieved by carefully selecting the comparative parameters. The current required is dependent on the volume of water, temperature and available free chlorine. Various types of electrode plates were tested and enhancements were made to design a chosen cell. The cost of PV devices has fallen in recent years making PV a feasible option for water treatment. PROJECT OBJECTIVES The photovoltaic chlorination project received funding through the Office of Sustainable Energy Industries; Environmental Protection Agency under a state approved “Queensland Sustainable Energy Innovation Fund”. Additional funding was provided by Queensland University of Technology to achieve the following goals: • • • Expand the use of solar power to water pumping and filtration. Improve overall system performance. This includes integrating the system to the grid and considering alternative backup systems for chlorination. Consider alternative electro-chlorination methods such as convection and submersible. Allchlor Pty Ltd has been collaborating with Queensland University of Technology during the past two years to research and develop components with the aim of assessing the feasibility of PV chlorinators for Australian and overseas markets. Destination Renewables - ANZSES 2003 Reviewed as full paper 298 © copyright 26 to 29 November Operation of Photovoltaic Electro-Chlorination Process Khouzam The project offers the following advantages: • Contributes to the renewable energy industry as the new PV chlorinator uses direct electricity produced using PV panels. The inherent matching of the source and the load is accomplished without the need for costly power conditioning or inverters. • Efficiency improvement and reduction in electricity consumption and associated emissions. The PV system offers greater safety and cost reduction in the maintenance of pools. The resulting reduction in emission amount to more than 1000 kg of CO2 annually for the average size pool. • Contributes to the growth in the swimming pool market and to establishing a commercial PV based chlorine industry. There is a niche market for the product in Australia and overseas. • The demonstration projects will contribute to increasing public awareness of environmental problems, the need to exploit alternative energy technologies, and to community acceptance of new energy technologies. PROJECT DESCRIPTION The first phase of the project was completed in 2001. This involved testing of various electrolysis parameters and electrode materials and chemicals. Experiments were conducted to examine the effect of applied voltage, current, salinity level, water flow rate, and duration of chlorination. Other tests included the effect of the dimensions of the electrodes and the spacing between them. Results showed that proper matching can be achieved by carefully selecting the PV parameters with respect to the electrolytic load. In the second phase of the project seven PV chlorinator systems were designed and installed in selected public and residential swimming pool sites in Queensland. Various systems configurations were considered and some were implemented. Figure 1 shows a schematic diagram of a PV installation in a public pool at Palmwoods, Maroochy Shire in the Sunshine Coast. The control unit is supplied with low volt dc from the PV array which in turn supplies the electrolytic cell. Chlorine is produced in the electrode cell by electrolysis and returns to the pool. The optional mains chlorinator operates in parallel and its use is limited to few hours on cloudy days. A data acquisition system is installed to record data for the purpose of monitoring. Figure 1. Schematic diagram of PV chlorinator at Palmwoods in Sunshine Coast. Destination Renewables - ANZSES 2003 Reviewed as full paper 299 © copyright 26 to 29 November Operation of Photovoltaic Electro-Chlorination Process Khouzam PHOTOVOLTAIC CHLORINATOR INSTALLATIONS A list of the PV chlorinator sites and their specifications is given in table 1. Specific recommendations on each site follow in sub-sections. Table 1. Photovoltaic chlorinators installed in and around Brisbane, Queensland. Size of System Specification Pool • 4 SX-80 W PV panels wired for 6 V provide total chlorination using Taringa in-line system. 55,000 L • Electrode is installed below water surface and thus provide Residential independent chlorination and pumping (convection effect). • Chlorination operates during daylight hours. • An AC pump runs filtration for 4 hours (winter) to 8 hours (summer) per day. • No backup system is employed for chlorination. • A selector switch may be required to prevent excess chlorine. • System has been running satisfactorily for over two years. • 6 SX-80 PV panels wired for 6 V provide water chlorination. Palmwoods • A backup system is employed in parallel. 32,000 L • A control switch is installed to switch on 2 panels at a time to control Public Pool chlorine level and prevent excess chlorination. • AC motor is used for water pumping. • Water is heated using electric heat pump. • PV chlorinator is oversized and excess electricity may be exported. • 3 SX-80 PV panels wired for 6 V provide chlorination. Pallara • 1 SX-80 PV panel (12 V) provide dc pumping during daylight hours 60,000 L but bypassing water filter and using a non-return valve. Residential • A backup system is employed in parallel. • AC power is used for pumping for water filtration using night tariff. • Reverse polarity will be advantageous; otherwise system is running satisfactorily. • 8 SX-80 PV panels wired for 12 V and connected to two electrodes Logan in series provide water chlorination. Central • A backup chlorinator of 50 A and 14 V is employed on another line 97,000 L but set to low. Public Pool • Two AC motors are used for water pumping with two lines for water chlorination; one on PV and the second on grid power. • Water is heated using gas. • Solar chlorinator is performing well. • 4 SX-80 W PV panels wired for 6 V provide chlorination. Arana Hills • Chlorination operates during daylight hours. 100,000 L • Two AC pumps run independently with a combined operation of 6 Learn to hours (in winter) to 12 hours (in summer) per day. Swim Club • A backup chlorinator system is employed for chlorination on one of the two pump lines. • 6 SX-80 W PV panels wired in series provide power for dc motor Burpengary pumping for water filtration. 65,000 L • 2 SX-80 W PV panels wired in parallel for 6 V provide for water Residential chlorination. • System runs entirely on solar power but a backup power may be required for consecutive cloudy days mainly for filtration. • 4 SX-60 W PV panels are wired in parallel for 6 V to power the cell. Acacia Ridge • A 1.5 hp ac motor pump runs the water filtration. 75,000 L • System operates on timer but during daylight hours. Fitness and • A conventional backup chlorinator is set to low. Squash Club • System was recently installed and is operating satisfactorily. Location and Type Destination Renewables - ANZSES 2003 Reviewed as full paper 300 © copyright 26 to 29 November Operation of Photovoltaic Electro-Chlorination Process Khouzam Taringa The system at Taringa is privately owned. There are three pumps installed at this pool. The first pump is used to pump water to a solar heater and back to the pool. A second pump is used to operate the pool cleaner. The third pump is used to pump water through the filter, into the chlorination cell, and back to the pool. Figure 2 shows the chlorinator cell at Taringa system. Because the electrode cell is installed below water level, even when the pumps are not running, there is still water ni the chlorination cell and PV current flows between the electrodes, producing chlorine. This causes gas to build up in the cell, which becomes warm. This causes the chlorine to dissipate into the pool by convection effect. While the filter pump is running the water is stirred up for 4 hours in winter and up to 8 hours in summer. The cleaner pump is run for one hour a day and the heater pump is run mostly in summer and whenever the pool is used. Figure 2. The electrode cell housing is installed below water surface at Taringa system. The solar chlorinator works very satisfactorily and without a backup source. The owner could not recall having to manually add any chlorine during its entire two years of operation. The owner had to disconnect two PV modules in winter to stop over chlorinating. Alternatively, the salt level would be allowed to drop to below 2,000 ppm to reduce chlorine production. Palmwoods There are six SX-80 PV modules at Palmwoods (see heated public swimming pool owned by the Maroochy extensively used all year round. As such the filter pump hours in summer per day. At the time of installation regarding the installation of a grid interactive PV system. Figure 3) which chlorinates a 32,000 litres Shire in the Sunshine Coast. The pool is runs a minimum of 20 hours in winter to 24 there was discussion with council officials Data collected showed that by midday the chlorine level reaches 3 ppm especially on clear sunny days. For fear of over-chlorination, the operator shut the system entirely down manually until next day. As a consequence, the operator adds liquid chlorine to the pool early the following day at 6 am. Destination Renewables - ANZSES 2003 Reviewed as full paper 301 © copyright 26 to 29 November Operation of Photovoltaic Electro-Chlorination Process Khouzam Figure 3. PV chlorinator in public swimming pool at Palmwoods in the Sunshine Coast. The system at Palmwoods requires a controller to better match chlorine requirement and make use of excess energy. According to Australian Guidelines (1989) and Queensland Health (2000) a high level of chlorine may be permitted and would therefore reduce the frequency to super-chlorinate the pool in times of heavy demand. Thus, although the system is considered oversized, the operator could leave it on and allow the chlorine level to rise to up to 8 ppm, which will avoid adding liquid chlorine. Pallara The system (Figure 4) at Pallara is privately owned. It comprises four SX-80 W PV modules. Three modules are connected in parallel (6V) and a backup power pack is used. To reduce electricity bills for pumping an 80 W 12 V PV module is used to circulate the water through the electrode cell using a dc motor pump and a non-return valve. Because of its low power rating the plumbing line is designed to bypass a large sand filter. A second motor runs the pump for water filtration on night tariff. Figure 4. PV water pumping and chlorination system at Pallara, south of Brisbane. Destination Renewables - ANZSES 2003 Reviewed as full paper 302 © copyright 26 to 29 November Operation of Photovoltaic Electro-Chlorination Process Khouzam Although a solar powered motor was used to pump the water through the electrode, it was found that the cell plates require very frequent cleaning. This is probably because the water was not filtered prior to chlorination. It is considered to use a current booster to the motor for pumping the water through an auxiliary low-pressure filter. A control circuit for switching the plates polarity for self-cleaning has been recommended. Logan Central This system comprises eight SX-80 PV modules wired for 12 V, connected to two electrodes in series via a selector switch and provide a peak current of 42 A. Due to some building restrictions with the design of the support structure, the system suffers some shading loss of 10% until around 10 am. A photograph of the system is shown in Figure 5. Two other electrodes are connected in series to a mains-power pack rated 50 A at 14 V and is almost always set to minimum. This heated pool capacity is 97,000 litres and is used all year round. Figure 5. PV chlorination system at Logan City Gardens Centre public swimming pool. The chlorine level of the pool during the test period (12 months) was within recommended values and the PV system was able to meet the chlorine demand. The operator of the pool is experienced in pool maintenance and has the system well tuned. If there is no high load, the operator will usually turn off the power pack and just keep the solar system. The system demonstrated that the backup unit was only required on severely consecutive overcast days. Thus, there is no need to expand the size of the PV system, and alternatively liquid chlorine could be used if necessary. Arana Hills The pool at Arana Hills is part of a health and fitness club. The chlorinator system comprises four SX80 W PV modules, in-line electrode, and an ac motor-pump for filtration. For greater reliability, there is a similar plumbing system running in parallel but employing a conventional power pack. Thus water chlorination uses nearly 50% of the energy requirement from PV while mains supplies the remaining. The proper place for the installation of the PV array would have been on top of the equipment room, which is also facing north. However, for reasons of security and vandalism, the PV modules were installed away from the entrance of the pool, as shown in Figure 6. Destination Renewables - ANZSES 2003 Reviewed as full paper 303 © copyright 26 to 29 November Operation of Photovoltaic Electro-Chlorination Process Khouzam Figure 6. Photovoltaic chlorinator in swimming pool at a sports club in Arana Hills. The club manager expressed interest in the installation of a larger PV system with the view to reduce the club’s electricity bill. A grid interactive PV system may be integrated with the pool chlorinator. Burpengary The installation at Burpengary comprises eight SX-80 PV modules, a dc motor driving a centrifugal pump, a chlorinator cell and a control and instrumentation circuit. Six modules are used for pumping for water filtration and two modules run the chlorinator cell in an in-line system. The system normally works from sunrise to sunset unless disconnected manually by the owner. This is the first system that runs entirely on solar power and no backup power was put in place. Figure 7. Eight SX-80 W PV modules are used to run the swimming pool at Burpengary. Destination Renewables - ANZSES 2003 Reviewed as full paper 304 © copyright 26 to 29 November Operation of Photovoltaic Electro-Chlorination Process Khouzam The system was installed in September 2002; but a trial dc motor driving the pump was replaced in May 2003. The chlorinator has been performing well with only two PV modules during low pool usage. On clear sunny days with solar radiation intensity of around 5 kWh/sq metre, the chlorine level remains adequate until around 5 pm. However, on consecutive cloudy days, insufficient chlorine level was noticed. This is mainly due to the reduced filtration time on cloudy days. A larger electrode plate rated 50 A was later installed and improved the chlorine level substantially including on cloudy days. Implementing a backup system may improve water quality. An option would be to construct a convection electrode cell in the pool walls and use liquid chlorine for superchlorination as required. Acacia Ridge This system runs a pool chlorinator at a sports and squas h club in Acacia Ridge. It comprises four SX60 PV modules, a backup mains unit, a salt cell and an instrumentation circuit, as shown in Figure 8. According to the owner, the system was set to run during daylight hours and has been running without a problem since it was installed in May 2003. Because the system was recently commissioned chlorination data are not yet available. Figure 8. Installation and wiring of the salt cell at swimming pool in Acacia Ridge. COMMERCIAL POTENTIAL A business plan for commercialisation was prepared. This included the system’s main strengths, weaknesses, opportunities and threats (SWOT) against conventional chlorinators. The PV electrochlorination system relies on two existing technologies/products: photovoltaics and electrolysis plates. Thus, it is envisaged that the set up cost of the production facility can be kept low. It is believed that the PV chlorinator can be marketed for the following reasons: • • • The technique of electrolysis of sodium chloride is mature and has been in use for many years. There is no major change with the introduction of PV. A 300 W power supply unit for chlorination costing $500 can be replaced with 240 W PV array at a cost of $1500 and with no running cost saving over $200 a year, making a payback period of five years. The PV chlorinator can either be used in new pools or retrofitted to existing ones. Furthermore, Destination Renewables - ANZSES 2003 Reviewed as full paper 305 © copyright 26 to 29 November Operation of Photovoltaic Electro-Chlorination Process • • • Khouzam with a total solar power system for chlorination and filtration, the need for ac cable extensions and trenching will be eliminated. In spite the controversy of using chlorine for treatment, many people in Australia and around the world would regard this product as ‘environmentally friendly’. The PV array can be installed above the pool thus providing shade and reducing loss of chlorine due to evaporation. The solar option could contribute to the growth in the swimming pool market amongst Australians who regard the pool an important recreation activity. CONCLUSIONS The results demonstrated that the use of direct-coupled PV in the water electro-chlorination process offers the following salient features: • • • • The electrolysis makes use of the non-linear characteristic of PV array; in its intrinsic matching quality, and without a need for expensive power conditioning. The PV system offers over-current protection caused when salt concentration is exceeded or due to contaminants in the water (an inherent problem with commercial units). PV produces high quality dc (without ripple), which in turn offer more effective and sustained ion separation during electro-chlorination. There is some inherent matching of solar radiation, chlorine requirement and production and pool usage. This is true for the daily as well as the seasonal variation in radiation and in temperature. Seven PV chlorinators are being evaluated and showed that the use of PV for water treatment is a practical, technically feasible and generally cheaper alternative to mains power. In spite some challenges with installations, all systems are performing adequately well. The PV-based chlorinator application will contribute to the renewable energy industry by creating demand for PV devices. PV offers unpolluted production of electricity, which would result in an annual saving of one ton of CO2 and other pollutants for an average size pool. The use of PV electrolysis promises to offer environmental benefits, energy and cost savings if used in electrochemicals and industrial processes. ACKNOWLEDGMENTS This project is funded through the Queensland Sustainable Energy Innovation Fund, Environm ental Protection Agency. Further contribution was provided by Queensland University of Technology and by Allchlor Repairs Pty Ltd. The author wishes to thank Dr. Martin Gellender (EPA) and Mr. Jeff Braithwaite (Allchlor) for their continued support. REFERENCES Appelbaum J. (1987), The Quality of Load Matching in a Direct-Coupling PV System, IEEE Transactions on Energy Conversion, EC-2, No. 5, December 1987, pp.534-541. Khouzam K.Y. (2000), Demonstration of a Solar Electrochemical Plant in the Form of Salt-Water Chlorinator”, Final Report prepared for Department of Mines and Energy, Office of Sustainable Energy, QSEIF, October 2000. Khouzam K.Y. (1991), Optimum Load Matching In Direct-Coupled PV Systems - Application to Resistive Loads, IEEE Transactions on Energy Conversion, EC-5, No. 2, June 1990, pp.265-271. National Health and Medical Research Council (1989), Australian Guidelines for Disinfecting Private Swimming Pools, Australian Government Publishing Service, ISBN 064410291 8, 1989. Queensland Health (2000), Swimming and Spa Pool Water Quality and Operational Guidelines, February 2000. Destination Renewables - ANZSES 2003 Reviewed as full paper 306 © copyright 26 to 29 November