Marina C.
Koether
Department of Chemistry and Biochemistry, Kennesaw State University, 1000 Chastain Road, Kennesaw, GA 30144, USA
First published on 11th October 2001
The percentage composition of Al13, [AlO4Al12(OH)24(H2O)12]7+, in water treatment coagulants is an important criterion in the development and use of polymeric coagulants. Polymeric coagulants are generally used in cold climates or with highly turbid waters. Size exclusion chromatography–flame atomic absorption spectrometry (SEC-FAAS) can separate Al13 and monomeric Al within 6 min. The percentage composition of Al13 and monomeric Al is determined by solving two simultaneous equations. Due to overlapping peaks, a 10% error is associated with this method of quantification. This method can be used on coagulants of varying “r values” (r = [OH−]/[Al3+]), or on mixtures of those coagulants and monomeric aluminium.
Marina C. Koether |
Bench-scale and pilot-plant studies are used to determine the optimum treatment conditions based on the water quality. The conventional jar-test is the simplest method for determining the optimum treatment conditions. It involves the coagulation, flocculation and sedimentation steps of water treatment, but not the filtration step. The procedure involves adding coagulants and other coagulant aids to the rapidly mixing raw water and allowing sufficient time for coagulation. The water is then slowly mixed for a set period of time to cause flocculation and is subsequently allowed to settle before measurements of residual turbidity, color, Al, etc. are made.
Two mechanisms of coagulation are predominant in the literature, and the choice of coagulant often depends on the method that applies to the particular type of raw water. The two mechanisms are charge neutralization (via compression of the double layer and adsorption to produce charge neutralization) and sweep floc (via enmeshment in a precipitate and adsorption to permit interparticle bridging). When Al salts are used as coagulants, effective coagulation occurs in the pH range of 6.5 to 8.5 where the solubility of the hydrolysis products of Al is at a minimum. If the pH of the raw water or treated water is lower or higher, pH adjustments are made to be within the pH range for effective coagulation and to avoid corrosion in the distribution lines. The metal salts hydrolyze in water and react with species in the water to form hydrolytic metal complexes. These species are essential for coagulation, but are only intermediate species during the coagulation, and they ultimately form the insoluble (hydr)oxides.1
The Al13 cation is produced in the laboratory by adding a base, such as a carbonate or hydroxide, to an acidic Al salt solution. If the ratio of OH− to Al3+ (r = [OH−]/[Al3+]) is less than 3, then the resulting solutions are considered partially neutralized Al solutions (PNAS). The characteristics of the PNAS are dependent on the mode of preparation, such as the temperature, rate of stirring and choice of reactants. These characteristics change with age, dilution, or thermal treatment.3 The r value is one factor that determines the amount of monomeric and polymeric species present. As the r value increases in PNAS, the percentage of monomeric Al decreases almost linearly and the amount of polymeric species, in particular the Al13 species, increases up to r = 2.5. Due to the specific conditions required for the synthesis of Al13, [AlO4Al12(OH)24(H2O)12]7+, it is probably not a hydrolysis product formed during the conventional water treatment process. Thus, if Al13 is to be used as a coagulating agent, it must be present in the coagulant prior to addition to the raw water.
The most common commercially available polymeric Al coagulant is PAC (poly-aluminium-chloride). In most cases, PAC has an r value of 1.5. Other formulations called PAS (poly-aluminium-sulfate) and PAHS (poly-aluminium-hydroxy-sulfate) are not commercially available but also have an r value of 1.5. PAHS can be made at the plant by adding powdered limestone to a stirred solution of alum. The percentage of Al present as Al13 is only 10%. The production and use of PAHS only adds 10% to the cost and yet more than a 10% improvement in water quality is observed in most cases studied.4–6
Solutions containing about 95% Al13 (r = 2.5) can be synthesized and have been shown to be an effective and superior coagulant to alum under certain conditions.7 Equilibrium solubility diagrams are often used to describe the species present during coagulation. However, equilibrium is not achieved during the water treatment process for alum. This indicates the reason for the poor results for alum in cold waters where the hydrolysis is slow. Al13 is effective in both warm and cold waters since the Al13 species bypasses the need for hydrolysis.
Cost can be a prohibitive factor for the use of about 95% Al13 solutions. In addition, the toxicity of Al13 is in question.2 Thus, it is proposed that solutions containing Al13 be combined with monomeric Al in ratios and in sequences that are best suited for the raw water quality parameters. The Al13 and monomeric Al percentage composition of these preparations and the commercially available coagulants can be determined through size exclusion chromatography-flame atomic absorption spectrometry (SEC-FAAS).
A Perkin Elmer AAS 4000 was used to measure Al at 309.3 nm using an Al hollow cathode lamp and a 0.7 nm slit-width, 4 cm slit nitrous oxide–acetylene flame and AA mode only. The data acquisition program was written in Borland C. The output voltage (0 to 1 V) was collected versus time using a CIO-DAS16/Jr/16 data acquisition board, a CIO-MINI37 universal screw terminal and a C37FFS-5 shielded cable. The data were displayed on a computer and saved as XY (time and absorbance) data and uploaded into Excel for analysis.
The preparation of polymeric Al solutions containing about 95% Al13 involves heating 30 mL of 1.67 M AlCl3 (hydrate from Fisher) to 80 °C, adding 50 mL of 1.25 M Na2CO3 (Fisher) and quantitatively transferring the solution to a 100 mL volumetric flask to achieve a final concentration of 0.501 M Al and an r value of 2.5. During these experiments, the r = 2.5 solution produced solids that did not redissolve. This would indicate that the concentration of aluminium was less than indicated, as solids are formed and remain when r > 2.5. Thus, the r = 2 solutions were used representing about 95% Al13. Further dilution of 20 mL to 100 mL with the mobile phase is required immediately before SEC-FAAS. The maximum concentration measured is 0.10 M Al. The samples were also measured by FAAS in the continuous mode, separate from the column, by a further dilution of 2 mL into 100 mL in order to quantify the total Al. These solutions were 54 ppm in Al. Calibration standards were made from Fisher 1000 ppm Al solution with the maximum at 50 ppm Al.
Samples of r = 0 are monomeric aluminium solutions. As r increases, more polymeric species are present. Two sets of samples were measured. The unmixed samples studied were of varying r values (0, 1, 1.5, 2). The mixed samples involved mixing solutions of varying r values (1, 1.5, 2) with solutions of r = 0 in various ratios.
Fig. 1 Example of an analysis of aluminium standards and sample solutions using FAAS without SEC. Sample solutions a, b, c and d are 54, 40.5, 27 and 13.5 ppm Al, respectively. For solutions 4, 5, 6, and 7 refer to Table 1. |
abstr = 160s = 4.38[Al]Al13 + 0.0600[Al]monomeric aluminium | (1) |
abstr = 202s = 0.431[Al]Al13 + 1.31[Al]monomeric aluminium | (2) |
Fig. 2 SEC-FAAS analysis of aluminium solutions (0.10 M Al) with various r values. |
Fig. 3 SEC-FAAS analysis of mixtures of aluminium solutions of various r values. |
Solution | Abs (160 s) | Abs (202 s) | [Al13] | [Al3+] | % Al13 |
---|---|---|---|---|---|
1. 0.10 M Al r = 0 | 0.006 | 0.131 | 0 | 0.1 | 0 |
2. 0.10 M Al r = 1 | 0.110 | 0.092 | 0.0243 | 0.0622 | 28 |
3. 0.10 M Al r = 1.5 | 0.171 | 0.069 | 0.0385 | 0.0401 | 49 |
4. 0.025 M Al r = 2 + 0.075 M Al r = 0 | 0.102 | 0.132 | 0.0220 | 0.0935 | 19 |
5. 0.050 M Al r = 2 + 0.050 M Al r = 0 | 0.182 | 0.0986 | 0.0407 | 0.0619 | 40 |
6. 0.0625 M Al r = 2 + 0.0375 M Al r = 0 | 0.283 | 0.0949 | 0.0639 | 0.0514 | 55 |
7. 0.10 M Al r = 2.0 | 0.365 | 0.0626 | 0.0831 | 0.0205 | 80 |
It should be noted that this method is not truly quantitative and that detection limits are not obtained and are not relevant for the purpose of these measurements. The day-to-day fluctuations and drift observed during each analysis causes poor precision and results, approximately 10% error in the quantitative results. As seen in Figs. 2 and 3, the r = 2 solution has a tail on its elution peak that interferes with the monomeric peak. This overlap increases the uncertainty of the measurement. However, by examining the shape of the peaks, the percentage composition as found in Table 1 can be expected. Peak heights at the two retention times were used in solving the two simultaneous equations to calculate the concentrations of the two substances in the mixtures. This method is user-friendly for small utilities using relatively old FAAS instrumentation for this work. The cost of such a setup is minimal due to the possible use of a strip chart recorder with the older FAAS instruments rather than the computer interface used here.
The results in Table 1 also illustrate the percentage Al13 created in the r = 1 and r = 1.5 solutions. These values are high when compared to those found in PAC and PAHS. Those solutions only contain 10% of the aluminium as Al13. The increased amount is probably due to the heating involved in the preparation of these solutions. It would be more advisable to mix monomeric solutions with the polymeric solution to maximize the effectiveness and minimize cost.
Fig. 1 illustrates the continuous response obtained by FAAS versus the transient responses obtained in the chromatograms in Figs. 2 and 3. Although solution-sampling time was sufficient to establish a steady-state plateau, the plateau had a high amount of scatter and thus the average had a high amount of uncertainty. The mobile phase had a high concentration of KCl, which would deposit over time on the flame head. Periodic cleaning of the flame head was necessary between chromatograms. The instrumentation can be relatively inexpensive since high tech instrumentation (low detection limits) is not necessary for this work. Thus, old instrumentation or field instrumentation is suitable.
Separation and detection of Al13 and monomeric Al is feasible by SEC-FAAS. Chromatograms are completed within 6 min. It is foreseeable that this method may be used in the future, as the use of Al13 as a coagulating agent increases in the water treatment industry. Thus, the future of water treatment in this area involves exploring the applicability of mixtures of Al13 with monomeric Al versus monomeric aluminium and the timing of their application to the water stream due to the different mechanisms involved.
Footnote |
† Electronic Supplementary Information available. See http://www.rsc.org/suppdata/em/b1/b105581J/ |
This journal is © The Royal Society of Chemistry 2002 |