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Article

Effecting Partial Elimination of Isocyanuric Acid from Swimming Pool Water Systems

1
Department of Mechanical Engineering, University of La Rioja, 26004 Logroño, La Rioja, Spain
2
Department of Mining Exploitation and Prospecting, University of Oviedo, 33004 Oviedo, Principality of Asturias, Spain
*
Author to whom correspondence should be addressed.
Water 2019, 11(4), 712; https://doi.org/10.3390/w11040712
Submission received: 6 March 2019 / Revised: 3 April 2019 / Accepted: 3 April 2019 / Published: 6 April 2019
(This article belongs to the Section Water Use and Scarcity)

Abstract

:
It is essential to disinfect the water in swimming pools in order to deactivate pathogenic microorganisms. Chlorination of swimming pool water provides rapid and long-lasting disinfection, but leads to the formation of potentially toxic compounds, including isocyanuric acid, that are used to stabilize chlorine in pool water. Hygiene and health guidelines require an isocyanuric acid concentration in swimming pools of 25 to 75 ppm and that there be no level in excess of 100 ppm. This paper provides a new method to partially remove isocyanuric acid from the water of swimming pool systems with the use of melamine-based reagents. A melamine-photometry process stabilizes the isocyanuric acid. The melamine-based reagent that is added to the raw water reacts with the isocyanuric acid and forms a precipitated salt. The reaction also creates turbidity that is proportional to the isocyanuric acid concentration in the water. It was noted in this study that the optimum functioning range of melamine doses in the raw water was 0.04 to 0.06 g/L and that the reduction of isocyanuric acid in raw water increased as the dose of melamine was increased. Thus, it is necessary to obtain an estimate of the dose of melamine that is necessary to reduce the isocyanuric acid in the water without needing to add fresh water from the network to dilute it. Finally, it can be stated that eliminating isocyanuric acid that has accumulated in a pool’s water by treatment with melamine provides an efficient process, as it eliminates the amount of isocyanuric acid that is necessary to conform to the human health criteria of the European Union Directive 2006/7/EC. Treatment with melamine also reduces water network consumption and sewer discharge by successive purges that eventually will become unnecessary. Therefore, this proposed method is environmentally and economically beneficial.

1. Introduction

Swimming is a popular aquatic activity that offers many health benefits. However, the quality of pool water is often compromised during busy periods. In fact, organic substances such as hair, skin particles, sunscreen, cosmetics, sweat and body fluids are brought into the water by swimmers unintentionally. These contaminate the water [1,2,3,4,5]. Therefore, to protect swimmers and others against infectious diseases, disinfecting the water of swimming pools is essential and maintaining the quality of the water should be a priority for owners and managers of swimming pools [6,7].
Although a variety of disinfectants have been used for swimming pools, the most commonly employed method is chlorination [8,9,10,11]. It is intended to prevent disinfection of recreational water, the occurrence of waterborne diseases and inactivation of pathogenic micro-organisms. Chlorine is a chemical disinfectant, which is very effective and relatively inexpensive. Chlorine is dissolved in water or added as sodium hypochlorite (NaOCl), calcium hypochlorite (Ca(OCl)2) or another derivative, such as chloroisocyanurate [12]. One problem that is associated with the disinfection of water by chlorine products is the accumulation of potentially toxic disinfection byproducts in the pool [13,14,15,16,17,18,19,20,21,22,23,24]. Hypochlorous acid (HOCl) is produced by adding active chlorine to water. HOCl is highly unstable and decomposes easily to form hydrochloric acid (HCl), water and oxygen. In order to prolong the life of the active chlorine, an isocyanurate stabilizer is commonly added to the pool water. This prevents the usual and rapid dissipation of active chlorine by photochemical reactions due to ultraviolet radiation caused by direct exposure to sunlight. Ultraviolet radiation degrades the active chlorine, thereby changing the concentration of this compound in the water. The use of isocyanuric stabilizers eliminates this problem [25,26]. Figure 1 shows the residual active chlorine in the pool’s water when an inorganic chlorinated derivative is used without a stabilizer in the disinfection process and the residual active chlorine when isocyanuric acid is used as a stabilizer.
Isocyanuric acid has received recognition for this ability but has also received the blame for over stabilization which reduces chlorine’s effectiveness. This loss in effectiveness could possibly result in recreational water emerging diseases due to water quality standards being compromised. Thus, an isocyanuric acid level of 25–75 ppm is recommended with an upper limit of 100 ppm [27]. Thus, most health and hygiene regulations require a purge and daily renewal of 5% of fresh water in the pool to remove the excess isocyanuric acid. The fresh water is obtained from network water. The health departments and other regulators consider that high levels of isocyanuric acid can be harmful to health [28]. For example, in Spain, the RD 742/2013 [29] recommends that levels should not exceed 75 ppm. If the level exceeds 150 ppm, the pool will be closed until normalization of the value is achieved. In the USA, the Department of Health & Human Services in the Model Aquatic Health Code, also recommend that the maximum concentration level of cyanuric acid be 100 ppm [30]. In France, the use of isocyanuric acid is controlled, since the drainage and filling of swimming pools due to excessive isocyanuric acid is not allowed in so many regions because of water scarcity. The isocyanuric acid cannot be removed by conventional chemical treatment. It accumulates after weeks of treatment. Thus, the health and hygiene regulations require, to drain partially (5%) the swimming pool with the influx of fresh water to re-establish the proper cyanuric acid limits. In order to reduce fresh water consumption and sewer discharge by successive purges that could become unnecessary, this paper proposes a methodology to remove the isocyanuric acid based on the addition of melamine. Melamine reacts with isocyanuric acid to form a precipitated salt and turbidity that is proportional to the concentration of isocyanuric acid present in the water. The chemical reaction between isocyanuric acid and melamine is shown in Figure 2.
To date, there are no previous studies in the literature that apply the effect of melamine on the elimination or neutralization of isocyanuric acid. In addition, there are no human studies on melamine toxicity, and the data of toxicity of melamine are limited to oral ingestion in animals and not by inhalation and dermal contact with pool water. Regarding the animal studies, to date indicate a low toxicity by oral ingestion. Melamine is not metabolized and is rapidly eliminated in the urine. Several reviews of the available information have been undertaken by the World Health Organization (WHO) [31,32]; the US Food and Drug Administration (US FDA) [33] and the European Food Safety Authority (EFSA) [34]. The US FDA has published an interim safety/risk assessment on melamine and structural analogues and has established a Tolerable Daily Intake (TDI) of melamine of 0.63 mg per kg of body weight in humans. The EFSA has published a provisional statement and recommended that a TDI of 0.5 mg per kg of body weight be adopted as tolerable daily intake value for melamine in humans. In this study, melamine is added during the purification process by a bypass which allows a dose of melamine to react with isocyanuric acid, filtering the precipitate formed before the water is returned to the pool [35]. In this way, the concentration of melamine in the pool water, if any, would be residual. Considering these statements, and due to the concentration of melamine used in this study for pool water is minimum, the harmful risk on human health of melamine can be considered as very low. The objective of this study was to develop a method to remove accumulated isocyanuric acid from the pool water in order to reduce the purged water and the consumption of network water, and to develop a low-cost scale system.

2. Materials and Methods

To determine if the process of removing the proposed isocyanuric acid is appropriate, the following steps were developed: First, in order to control the quality of the pool water, the level of isocyanuric acid was determined by adding melamine and employing the Melamine-Photometry method using sodium acetate and melamine as reagents. The reagent of reference standard (2 g/L melamine) was prepared by dissolving 3.5 g of sodium acetate and 0.2 g of melamine in several samples of 100 mL of fresh water. For isocyanuric acid analysis, it was necessary to homogenize the water sample, and then transfer a 10 mL of it to a test tube. This 10 mL of water sample was mixed with 5 mL of prepared reagent. The resulting turbidity was measured in the spectrophotometer at λ = 525 nm using a 50 mm quartz cuvette. Finally, the precipitate that formed was removed using a filter of 0.45 μm pore size, and the absorbance of the clarified water was measured. The concentration of isocyanuric acid was determined by the difference between the total absorbance obtained in the water sample after complexation and filtration. The spectrophotometric measurements to determine the concentration of isocyanuric acid based on atomic absorption, were carried out on a Unicam Helios α model spectrophotometer (Unicam, Cambridge, UK). The turbidity measurement was conducted with a 2100Q Turbidimeter (Hach Company, Loveland, CO, USA) according to the ASTM D1889-00 standard [36], and Total Suspended Solids following the standard ASTM D5907-10 method [37]. The pH and the CE of the solutions were measured with a Multi-parameter MultiLine 3630 IDS (WTW, Weilheim, Germany) following the ASTM D1293-18 [38] and ASTM D1125-14 [39] standards respectively. After determining the isocyanuric acid concentration, the correlation between isocyanuric acid and melamine was determined by the following procedure:
Since it was not possible to have real pool water that contain a predetermined concentration of isocyanuric acid to study the repeatability of the isocyanuric acid determination method, a synthetic solution with a known isocyanuric acid loading was prepared in the laboratory. The melamine-photometry method was applied again on this synthetic solution. These synthetic samples were prepared by dissolving 0.05 g of isocyanuric acid in 500 mL of tap water that had a temperature between 10° and 20° and a pH between 7.2 and 7.5. Subsequently the samples were shaken vigorously for 20 min using a magnetic plate stirrer. Finally, the isocyanuric acid content was analyzed to verify that the concentration of the solution sample was what was sought. The different doses of the melamine prepared reagent were added to the samples in the jar test. The jar test that was used in the experiments involved a programmable apparatus (FLOCUMATIC, Selecta, Spain [40]). This apparatus consisted of six paddles on a bench. The paddles were connected to each other by a gear mechanism, and were rotated simultaneously by the same motor at a controlled speed (200 rpm) and for a specified time (10 min). Water samples were transferred to the jars. Then, a different dose of the melamine prepared reagent (0–1 g/L) was added to each beaker. After rapid stirring, the homogeneous sample was filtered by a glass fiber filter (0.45 μm). After each sample had been filtered, the water was analyzed to determine the isocyanuric acid present in the resulting liquid. At this stage, it was important to calculate the efficiency of the method in removing the isocyanuric acid and to quantify the performance by the amount of reagent (melamine) added. Comparing the efficiency of the method of removal efficiency to the isocyanuric acid parameter is described by the following:
E = [(ICNI − ICNF)/ICNI] × 100
where:
  • E = isocyanuric acid removal efficiency (%)
  • ICNI = isocyanuric acid concentration in raw water (mg/L)
  • ICNF = isocyanuric acid residual concentration in the filtered water (mg/L).
The last step of the proposed procedure consisted of filtering the insoluble complex isocyanuric acid–melamine. In this stage, the insoluble complex, isocyanuric acid–melamine, was removed by filtration. The filter used in this case was a Silex filter. These filter elements are used in majority of water purification installations for swimming pools mainly due to their ease of use.

3. Results and Discussion

The removal of isocyanuric acid was investigated by an experimental design procedure. The experimental results of the different steps of the new system for isocyanuric acid removal are presented in the following pages.

3.1. Results of the Repeatability of the Melamine–Photometry Process

This section provides the repeatability test results of the melamine–photometry process by which, the spectrophotometer and the correlation between isocyanuric acid and melamine, the amount of isocyanuric acid in water samples was determined. In the process of melamine-photometry, the repeatability of the quantitative results is of key importance. Figure 3 shows the linear correlation (R2 = 0.93) in the two different essays of the analytic method that were conducted with two different spectrophotometers. From the analysis, it can be deduced that the error is very acceptable for this type of tests and permits us to conclude that the analysis of isocyanuric acid by adding melamine method is very reliable.

3.2. The Efficiency Achieved in Eliminating Isocyanuric Acid from Sample Water

The isocyanuric acid removal efficiency was checked in the first series of tests, by adding melamine (0–1 g/L) to the raw water (synthetic solution). Figure 4 shows the amount of residual isocyanuric acid in the water after adding melamine and subsequently filtering the water (lower line) versus adding melamine and no filtration (upper line). Figure 4 shows that the addition of 0.3 g/L of melamine resulted in the removal of 98% (practically all) of the insoluble isocyanuric acid–melamine complex.
Figure 5a shows the results obtained after another series of trials were conducted to narrow the range of melamine addition and optimize its consumption (melamine doses between 0.02 to 0.08 g/L). Figure 5a shows that the correlation coefficient is 0.97. This means that there is an almost linear relationship between the residual and the melamine isocyanuric acid that is added. Similarly, isocyanuric acid concentration varies inversely to the dose of melamine. This inverse relationship can be calculated by Equation (2).
ICN (mg/L) = −1103.6 × M (g/L) + 116.89
where:
  • ICN = isocyanuric acid concentration (mg/L)
  • M = melamine dose (g/L).
When the concentration of isocyanuric acid in the raw water and the filtered water is known, the isocyanuric acid that was removed in the physical-chemical treatment can be calculated and, also, the efficiency of the same. Figure 5b shows the evolution of residual isocyanuric acid that was removed from the water sample after melamine was added, and the water was filtered. In this case, the dose of melamine that was added was between 0.02 and 0.08 g/L. It was noted that the addition of 0.02 g/L of melamine produced an isocyanuric acid removal of 9% on average, whereas a dose of 0.08 g/L, decreased by 70% the presence of the isocyanuric acid in water.
Considering that the amount to be removed in the sample water should be between 20% and 50% of isocyanuric acid, further tests were conducted at lower doses (0.04 to 0.06 g/L) of melamine. These appear in Figure 6a,b respectively. Figure 6a shows an average concentration of 80 to 48 mg/L of residual isocyanuric acid in the filtered water, after an addition of 0.04 and 0.06 g/L of melamine, respectively.
Similarly, Figure 6b shows that, as the efficiency of isocyanuric acid removal increased by adding more melamine. It also shows that the average percentage of removal of isocyanuric acid was 16% for 0.04 g/L and 52% for the higher dose of 0.06 g/L.
All of these data led to the conclusion that the optimum working range of doses of melamine in the raw water was between 0.04 and 0.06 g/L, with the reduction of isocyanuric acid in the initial water increasing as the dose is increased. This stage of the study facilitated verification of the method based on the addition of melamine to determine isocyanuric acid. It was also noted that the socyanuric acid–melamine complex could be removed by filtration. As a result, one can estimate the melamine dose that is necessary to reduce the isocyanuric acid of the water without a need to add tap water.

3.3. Results of the Repeatability of the Linear Correlation of Isocyanuric Acid–Melamine

The results of the study of repeatability and reproducibility of the linear correlation isocyanuric acid–melamine are described next. In order to verify the linear relationship obtained in the above results, the reduction of 20 mg/L of initial water, isocyanuric acid containing isocyanuric acid ranging from 20 to 100 mg/L was included in the study. For this reason, a constant dose of 0.04 g/L melamine was added to each of the samples synthesized. The addition of a dose of 0.04 g/L of melamine obtained an average value of removal of 22 mg/L of isocyanuric acid (Figure 7). These values confirm a high repeatability of the conducted measurements. These results coincide with those of the previous tests.
Table 1 summarizes the results of this test, the standard deviation and the mean value of isocyanuric acid that was eliminated. The tests involved adding 0.04 g/L of melamine to different water samples that contained isocyanuric acid between 20 and 100 mg/L. The accuracy of the results from the analytical method was very good. The repeatability of the results measured as the deviation was satisfactory; its value was 4.

3.4. Filtering Results of Insoluble Complex Isocyanuric Acid–Melamine

The complexation of isocyanuric acid with melamine produces an insoluble complex isocyanuric acid–melamine, which is in the form of microscopic crystals that are suspended in water. In the last stage of the study, these microscopic crystals that are suspended in water were removed by Silex filtration filters, which act as natural filtering agents.
Figure 8 shows the percentage of isocyanuric acid removed by particle size of the filter medium. From Figure 8, it is deducted that increasing the grain size of the sand decreases the isocyanuric acid removal rate, because the filter with lower granulometry of 0.4–0.8 mm is the most efficient as it removes 50% of the isocyanuric acid in the water samples. Filters of Silex sand with reduced granulometry (0.1–0.3 mm) produced a better quality of filtered water. This resulted in both a greater number of washes and cleaning of the hardest filters. In turn, this increased the expense of the isocyanuric acid removal process.

4. Conclusions

A methodology for removal of isocyanuric acid in swimming pool water is presented in this paper. The development process can be used to control isocyanuric acid in swimming pool water that cannot be removed by conventional pool water treatment. Thus, dilution with fresh water is necessary to keep the cyanuric acid at an acceptable concentration.
Chlorination of swimming pool water provides rapid and long-lasting disinfection, but leads to the formation of potentially toxic compounds, including isocyanuric acid, that are used to stabilize chlorine in pool water. The treatment requires draining 5% of the water from the pool to eliminate the isocyanuric acid that has accumulated, in compliance with the European Union Directive 2006/7/EC [41]. The proposed method, Melamine-photometry, allows the partial removal of the isocyanuric acid that has accumulated in the water of the pool. The process involves the removal of isocyanuric acid by a melamine-based reagent. The melamine reacts with isocyanuric acid in a process that offers satisfactory repeatability and accuracy, forming an insoluble complex that is easy to remove by filtration. It was found in this study that the optimum functioning range of melamine doses in raw pool water was 0.04 to 0.06 g/L and that the reduction of isocyanuric acid in the raw water increased as the dose increased. Thus, an estimate of the dose of melamine that is necessary to reduce the concentration of isocyanuric acid in the water has been obtained without needing to add water to the network. In summary, the removal of accumulated isocyanuric acid by a chemical treatment that uses melamine has become economically and environmentally beneficial. It reduces water network consumption, as well as sewer discharge, by successive purges that eventually will be unnecessary.

Author Contributions

Experimental work: M.C.B., E.P.V.G., R.L.L. and F.S.G. Results analysis, revision and improvement of the manuscript: All authors.

Funding

This research received no external funding.

Conflicts of Interest

The authors declare no conflict of interest.

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Figure 1. Comparison of residual active chlorine levels vs. the use of stabilizers (or lack thereof) [22].
Figure 1. Comparison of residual active chlorine levels vs. the use of stabilizers (or lack thereof) [22].
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Figure 2. The insoluble complex that is formed by the reaction of isocyanuric acid and melamine.
Figure 2. The insoluble complex that is formed by the reaction of isocyanuric acid and melamine.
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Figure 3. Linear correlation of the two methods studied.
Figure 3. Linear correlation of the two methods studied.
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Figure 4. Variation of isocyanuric acid residual in the filtered water vs. adding melamine (0–1 g/L).
Figure 4. Variation of isocyanuric acid residual in the filtered water vs. adding melamine (0–1 g/L).
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Figure 5. Range of melamine additions (0.02–0.08 g/L): (a) Variation of isocyanuric acid residual in the filtered water, (b) variation of isocyanuric acid removed in the filtered water.
Figure 5. Range of melamine additions (0.02–0.08 g/L): (a) Variation of isocyanuric acid residual in the filtered water, (b) variation of isocyanuric acid removed in the filtered water.
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Figure 6. Range of doses of addition of melamine (0.04–0.06 g/L): (a) Variation of isocyanuric acid residual in the filtered water; (b) variation of isocyanuric acid removed in the filtered water.
Figure 6. Range of doses of addition of melamine (0.04–0.06 g/L): (a) Variation of isocyanuric acid residual in the filtered water; (b) variation of isocyanuric acid removed in the filtered water.
Water 11 00712 g006
Figure 7. Variation of isocyanuric acid removed in the filtered water versus the addition of 0.04 g/L of melamine.
Figure 7. Variation of isocyanuric acid removed in the filtered water versus the addition of 0.04 g/L of melamine.
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Figure 8. Isocyanuric acid removal rate vs. particle size of the filter medium tested.
Figure 8. Isocyanuric acid removal rate vs. particle size of the filter medium tested.
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Table 1. Results of isocyanuric acid after addition of a constant dose of melamine and removal of isocyanuric acid.
Table 1. Results of isocyanuric acid after addition of a constant dose of melamine and removal of isocyanuric acid.
Melamine Dose (g/L)Isocyanuric Acid Initial (mg/L)Isocyanuric Acid Residual (mg/L)Isocyanuric Acid Removed (mg/L)
0.041007426
0.04806317
0.04603624
0.04402119
0.0420218
0.041006931
0.04805921
0.04603525
0.04402119
0.0420119
Isocyanuric acid average removed standard deviation224

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Corral Bobadilla, M.; Vergara González, E.P.; Lostado Lorza, R.; Somovilla Gómez, F. Effecting Partial Elimination of Isocyanuric Acid from Swimming Pool Water Systems. Water 2019, 11, 712. https://doi.org/10.3390/w11040712

AMA Style

Corral Bobadilla M, Vergara González EP, Lostado Lorza R, Somovilla Gómez F. Effecting Partial Elimination of Isocyanuric Acid from Swimming Pool Water Systems. Water. 2019; 11(4):712. https://doi.org/10.3390/w11040712

Chicago/Turabian Style

Corral Bobadilla, Marina, Eliseo P. Vergara González, Rubén Lostado Lorza, and Fátima Somovilla Gómez. 2019. "Effecting Partial Elimination of Isocyanuric Acid from Swimming Pool Water Systems" Water 11, no. 4: 712. https://doi.org/10.3390/w11040712

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