Abstract
A paper mill in Minnesota uses 100% chlorine dioxide (ClO2) to bleach its pulp and the run-off flows into the St. Louis River. ClO2 is safe when used as a water treatment, but there can be toxic environmental effects over 5 mg/ L.
A Beers Law plot of absorbance of ClO2 versus concentration was developed for the first time in order to continue with this study. Various sites upstream and downstream of the paper mill were sampled to determine an average amount of ClO2 concentrations in the river at each site.
This study has concluded that the levels of ClO2 in the St. Louis are under the levels that could be hazardous to the river and its aquatic life. The greatest concentration of ClO2, 0.3612 mg/L, was found at site 5, which was closest to the paper mill. This value is low enough to indicate there is not a significant effect on the river.
Introduction
In this project, I monitored the concentration of ClO2 in the St. Louis River in Cloquet, Minnesota, upstream and downstream from a paper mill plant that lies directly on the river. This plant uses ClO2 exclusively to bleach the pulp.
Hypothesis
My hypothesis was that there would not be any detectable levels of ClO2 upstream of the paper mill, but there would be significant concentrations of ClO2 downstream of the mill, perhaps over the maximum amount that is considered safe from a biological viewpoint.
Background
In the past, the pulp and paper industry have used chlorine gas (Cl2) to bleach pulp. As a result, run-off from these plants contained chlorophenols, chloroform, and chlorinated organic compounds. Traces of these toxic chemicals were detected in the river in the late 1980s and, since then, environmental agencies have motivated the industry to use bleaching techniques that eliminate these chemicals. One new technique to bleach pulp was developed that uses ClO2. The "Pollution Prevention Act of 1990" was passed to compel the pulp and paper plants to use the new techniques (Elemental Chlorine-Free).
ClO2 has a greater oxidation potential than Cl2. During the bleaching process, Cl2 and ClO2 turn into chlorinated organics. Cl2 combines with the lignin (substance that holds wood fibers together), while ClO2 oxidizes the lignin so it opens up the aromatic structure. Other chlorinated organics formed by ClO2 bleaching are water-soluble and do not bio-accumulate. Therefore, ClO2 seemed to be the best alternative that would help the eco-system and still bleach the pulp (Elemental Chlorine-Free).
In addition to use in pulp bleaching, ClO2 is also used in the treatment of drinking water. The maximum residual concentration of ClO2 that does not release objectionable taste or odor in treated water is 0.4 to 0.5 mg/L. The maximum amount of ClO2 that is considered safe from the toxicological viewpoint is up to 5 mg/L (ClO2: Chemistry and the Environmental Impact of Oxychlorine).
The chemistry of the reaction of ClO2 in water is not known. There are two possible equlibra for the reaction of ClO2 with water. It is not known which path the reaction follows.
4 ClO2 + HCl + 2H2O <==> 5 HClO2
or
2 ClO2 + HClO3 + HCl + H2O <==> 4HClO2
Since there are two possible equations for the reaction, stoichiometry can not be used to determine the concentration of the ClO2. First, a method had to be developed to determine the concentration and then study of ClO2 in the St. Louis River was undertaken.
In Cloquet, Minnesota, a pulp and paper plant that lies directly on the St. Louis River started using the new technique of bleaching with ClO2. In 1994, the mill used 10% of ClO2, and in 1994, they switched to 100% use of the ClO2. Determining the reaction of ClO2 in water would be significant for further study of the environmental impacts of this process of bleaching.
Methods and Materials
Beers Law Plot for ClO2
The concentration of ClO2 was found by creating a Beers Law plot of absorbance versus concentration. This was the first time the concentration of ClO2 in water has been determined.
First, ClO2 gas was synthesized in water by placing a small piece of sodium chloride (NaClO2) into a round bottom flask and, using a syringe, 0.5 mL of concentrated hydrochloric acid (HCl) was dropped into the sodium chloride. The synthesis equation is:
NaClO2 + HCl à HClO2 (g) + NaCl
A syringe was used to suck the HClO2 gas out of the flask and inject the HClO2 into
an erlenmeyer flask filled with 200 mL of distilled water. This produced aqueous ClO2. The ClO2 was pipeted in into a cuvette for diode-array analysis, and the absorbance of ClO2 was determined at 358 nm.
Next, 4 g of potassium iodide (KI) was dissolved in 10 mL of distilled water. This solution was added to 50 mL of the synthesized ClO2 solution. The remaining ClO2 solution was stored in an ice bath in the dark to prevent photo and thermal decomposition between each test.
The solution was titrated with standardized 1M sodium thiosulfate (Na2S2O3) to a yellow end point, then 5 mL of starch solution was added to turn the solution to blue. The solution was titrated until clear. This procedure was repeated two times using the remaining ClO2 solution to obtain an average concentration of ClO2.
The synthesis process was repeated ten times to obtain points for the Beers Law plot. Stoichiometry was used to determine the concentrations of each solution of ClO2.
Lastly, a Beers Law plot of absorbance versus concentration of ClO2 in water was determined.
Analysis of St. Louis River Water
The St. Louis River water was analyzed by collecting samples at four sites upstream and four sites downstream of the paper plant. Sampling sites 1 through 4 were upstream of the paper plant, and sampling sites 5 through 8 were downstream of the plant. The depth was measured at each sampling site. Clean, plastic, washed bottles that were taped to prevent light from photo-decomposing the ClO2 during transportation were used to collect the samples. Before collecting the water samples, the bottles were rinsed with river water, and then the whole plastic container was dipped into the river until the bottle was full. The cap was twisted on while the bottle was submerged, and the bottle was placed into a container of dry ice to slow thermal decomposition during transportation. The temperature of the river water was taken at each site, using an electronic thermometer. The pH of the samples was taken at the laboratory, using an Interface. The absorbance of the ClO2 was measured using the diode-array, and the concentration was determined by using the Beers Law plot developed previously.
Results
Calculated from the absorbance data in Table 1, the average of the upstream absorbencies was 0.0333, and the average of the downstream absorbencies was 0.0069. The standard deviation for upstream was 0.0395, and the standard deviation downstream was 0.00296. The 95% probability that the true average absorbance of ClO2 upstream of the paper mill is between 0.064 and 0.0342. The downstream probability is between 0.0000288 and 0.00495. The t-test value of upstream and down stream gave a value of 2.944.
Table 1: Absorbance (@ 358 nm) of ClO2 at Various Sites
Upstream and Downstream of the St. Louis River
from July 31 to October 20, 1998
Absorbance Up Stream Absorbance Down Stream
| Date |
Site 1 |
Site 2 |
Site 3 |
Site 4 |
Site 5 |
Site 6 |
Site 7 |
Site 8 |
|
July 31 |
-0.0147 |
-0.0887 |
-0.0606 |
0.0020 |
0.0085 |
|||
|
Aug 26 |
-0.0027 |
0.0114 |
0.0044 |
0.0054 |
0.0094 |
|||
|
Oct 20 |
0.0004 |
0.0071 |
0.0073 |
The concentration of each sample was determined by using the Beers Law Plot.
Table 2: Concentration (mol/ L) of ClO2 at Various Sites Upstream
and Downstream of the St. Louis River
from July 31 to October 20, 1998
Upstream Concentrations Downstream Concentrations
|
Date |
Site 1 |
Site 2 |
Site 3 |
Site 4 |
Site 5 |
Site 6 |
Site 7 |
Site 8 |
|
July 31 |
-2.5x10-5 |
-1.1x10-4 |
-7.8x10-5 |
-5.5x10-6 |
2.0x10-6 |
|||
|
Aug 26 |
-1.1x10-5 |
5.4x10-6 |
-2.7x10-6 |
-1.6x10-6 |
3.1x10-6 |
|||
|
Oct 20 |
-7.3x10-6 |
4.1x10-7 |
6.4x10-7 |
The calculations for mg/ L of ClO2 are shown in table 3.
Table 3: ClO2 levels (mg/ L) at Various Sties Upstream
and Downstream of the St. Louis River
from July 31 to October 20, 1998
Upstream Levels Downstream Levels
|
Date |
Sit 1 |
Site 2 |
Site 3 |
Site 4 |
Site 5 |
Site 6 |
Site7 |
Site 8 |
|
July 31 |
-1.6650 |
-7.4095 |
-5.2282 |
-0.3686 |
0.1360 |
|||
|
Aug 26 |
-0.7334 |
0.3612 |
-0.1822 |
-0.1046 |
0.2059 |
|||
|
Oct 20 |
-0.4924 |
0.0274 |
0.0429 |
Conclusions
The results for the absorbance of ClO2, seen in Table 1, found that the absorbances are non-existent or extremely low upstream of the plant and there are traces of ClO2 below the plant. The greatest absorbance, 0.0114, is found at site 5, which is exactly at the paper mill. The absorbance lowers after this point, probably from photo and thermal decomposition. The standard deviation of absorbance shows that the range of values for downstream are closer to the downstream average than the upstream points are to their average. The two averages are significantly different because the t-value, 2.944, is greater than the confidence level value at 95%, which is 2.20.
The levels of ClO2 at each site, seen in Table 3, are all below the toxic level of
5 mg/ L. The lowest amounts are near the beginning of the water source at site 1 and gradually increase, having the greatest amount at site 5. Then the levels decrease and increase again at site 8. The reason for this increase is vague, but the detection levels of ClO2 in the St. Louis River are still at safe levels.
This study has concluded that there is a significant difference of absorbance between the upstream absorbance of ClO2 and the downstream absorbance, but the measurements show that the difference is not significant enough to make the river unsafe.
Further studies could be done to obtain more samples taken at lower depths. This test would determine if the ClO2 absorbance differs, since photo and thermal decomposition has a lesser effect at deeper levels. Taking samples to observe if there are significant amounts of chlorophenols, chloroform, or chlorinated organic compounds in the river is another possibility because even though ClO2 is not found to be directly present, ClO2 by-products could be a significant problem. Testing the absorbance during the winter would also be interesting to see if absorbance changes with drastic change in temperature.
Appendix A
Beers Law Plot
As seen in Figure 1, the absorbance increases with a greater concentration of ClO2. The equation for the regression line equation of this graph is:
y = 0.0067476 + 868.89 * x

Appendix B
Standardizing Na2S2O3
The Na2S2O3 solution was standardized using titration. First, 9.0544 g of sodium
thiosulfate was dissolved in 500 mL distilled water to make the Na2S2O3 solution. Next,
2 g of KI was dissolved in 20 mL of distilled water, and 0.15 g of potassium iodate (KIO3) was added into the KI solution. This solution was diluted in 100 mL of distilled water. Then, 20 mL of sulfuric acid solution (1 mL of sulfuric acid to 39 mL distilled water) was mixed with the diluted solution. This solution was titrated with Na2S2O3 until it became a slight yellow color, and then 5 mL of starch was added, changing the solution to blue. Na2S2O3 was then added until the solution turned clear. The procedure to standardize the Na2S2O3 solution was repeated three times, and the average was calculated by stoichiometry. The stoichiometry for this reaction is:
IO3- + SI- + 6H+ à 3I2 + 3H20
2S2O32- + I2 à S4O62- + 2I-
These equations were used to determine the molarity of the Na2S2O3 , by using the formula below.
(g KIO3) (mol KIO3 / g KIO3) (mol I2/ mol IO3-) (mol S4O62- / mol I2) = mol S4O62-
(mol / L S2O32-) (L S2O32-) = mol S2O32-
Appendix C
Calculations for Concentrations of ClO2
By these equations, the concentrations for each solution of ClO2 were determined:
2ClO2 + 2I- à I2 + 2ClO2-
I2 + 2S2O32- à 2I- + S4O62-
The following calculations were done:
(mol S2O32-) (1 mol I2/ 2 mol S2O32-) (2 mol ClO2/ 1 mol I2) = mol ClO2
(mol ClO2/ L ClO2) = M ClO2
Appendix D
Locations of Water Sampling Sites: Cloquet, Minnesota
Appendix E
Calculations for Statistical Analysis
The average was determined by adding all the upstream absorbencies divided by the number of values. The downstream average was determined the same way but using downstream values.
Upstream: -0.166 / 5 = -0.03325
Downstream: 0.0555 / 8 = -0.0069
The standard deviation was determined by subtracting the average absorbance for upstream from each upstream value and squared. Then these were all added together and divided by the degrees of freedom (number of points minus one). Lastly, this value was square rooted. The standard deviation for downstream was found using the same equation but replacing the upstream values with downstream values.
Upstream: 0.03985
Downstream: 0.002963
The confidence interval was found by multiplying the 95% confidence level at that degree of freedom with the standard deviation. This product was divided by the square root of the number of upstream points, and then added/ subtracted to the average upstream absorbance. The downstream values were found by the same method, except the upstream values were replace by downstream values.
Up stream: [(2.78 * 0.03848) / 2.236] (+ / -) * -0.03325
= -0.06396 < confidence interval < 0.03422
Down Stream: [(2.36 * 0.02960 / 2.828] (+ / -) * 0.006913
= -0.00002881 < confidence interval < 0.0049166895
The t-value was determined by adding the number of points taken downstream minus one. Then the sum was multiplied by the standard deviation for downstream squared; plus, the number of points for upstream minus one, multiplied by the standard deviation of upstream squared. This was divided by the sum of both degrees of freedom, multiplied by the number of points for upstream and downstream. The average downstream absorbance was subtracted from the average upstream and this value was divided by the value above.
T- value: 0.0401625 / 0.0136414607
= 2.944365262
Appendix F
Calculations for ClO2 levels (mg/ L)
The following equations were used to determine the mg/ L of ClO2.
(mol ClO2 / L)(67.4515 g ClO2/ mol)(1000 mg/ g) = mg ClO2/ L
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