Effect of Ph on Cpe Cr(Iii) Reagent 8-Hq

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H (%)

The field allows blind spot extraction of Cr(III) using 8-HQ reagent.


Figure 3.3. Effect of pH on CPE Cr(III) reagent 8-HQ

- 4

C Cr(III) = 2.0 μg/L; C 8-HQ = 2.10 M; C TX-100 = 0.2%

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Figure 3.4. shows the dependence of the blind spot extraction efficiency of Cr(III) using PAN complexing agent on the change of environmental pH value.


Figure 3.4. Effect of pH on CPE Cr(III) PAN reagent

C Cr(III) = 2.0 μg/L; C PAN = 2.10 -4 M; C TX-100 = 0.2%

From Figure 3.4, it can be seen that Cr(III) cations form good complexes with PAN complexing agent when the pH value is > 7. The complexation between Cr(III) and 8-HQ and PAN reagents is best at pH = 8. The blind spot extraction efficiency of Cr(III) in the case of using 8-HQ complexing agent is higher than the extraction efficiency of Cr(III) in the case of using PAN complexing agent. Therefore, use 8-HQ complexing agent to conduct further studies.

Thus, by simultaneously investigating the influence of pH and complexing agent on the blind spot extraction efficiency of Mn(II) and Cr(III), we chose complexing agent 8-HQ for both blind spot extraction of Mn(II) and Cr(III). For blind spot extraction of Mn(II), borate buffer pH = 10 is the optimal environment. For blind spot extraction of Cr(III), phosphate buffer pH = 8 is optimal for the extraction process.

3.1.2. Investigation of the concentration of the complexing agent 8 - hydroxyquinoline


The blind spot extraction efficiency depends on the complex formation of metal ions with the reagent, the kinetics of complex formation and the mass transfer between phases. In section 3.1.1, the complexing agent was investigated and 8-HQ was selected as the complexing agent for the extraction of Mn(II) and Cr(III). When the low concentration of 8-HQ is not enough to form a complex with the metal ions, high concentration of 8-HQ will cause waste. Therefore, the influence of 8-HQ concentration on the CPE efficiency of Mn(II) and Cr(III) was studied.

3.1.2.1. Investigation of optimal 8-HQ concentration for Mn(II) blind spot extraction


The 8-HQ concentration was investigated by varying the 8-HQ concentration while keeping other parameters constant in the Mn(II) blind spot extraction. The experimental procedure was as follows:

+ Pipet 1.0 mL of 2.0 mg/L Mn(II) standard solution into a 10 mL glass centrifuge tube. Add 2.0 mL of pH = 10 borate buffer solution and V mL of 4.10-3 M 8-HQ solution .

+ Add 1.0 mL of 4% Triton X - 100 solution and 1.0 mL of 5% NaCl solution.

+ Make up to 10 mL with double distilled water, soak the reaction mixture in a water bath at 95 o C for 40 minutes.

+ Then, take it out and centrifuge it for 10 minutes at a centrifugation speed of 3500 rpm, cool it by soaking it in ice water for 10 minutes.

+ Separate and dissolve the viscous phase with 1.0 mL of 0.1 M HNO 3 acid solution . Determine the Mn concentration in the analytical solution using the FAAS method with optimal conditions.

+ Mn(II) extraction efficiency is equal to the ratio of the determined concentration to the initial concentration. The experiment was conducted 3 times, the average Mn(II) extraction efficiency is presented in table 3.3.

Table 3.3. Effect of 8-HQ concentration on Mn(II) extraction efficiency


STT

C 8-HQ .10 4 (mol/L)

H (%)

1

0.5

54.3 ± 2.1

2

1.0

87.0 ± 2.0

3

2.0

87.4 ± 2.8

4

3.0

90.0 ± 1.8

5

4.0

96.7 ± 1.9

6

5.0

92.6 ± 2.0

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Effect of Ph on Cpe Cr(Iii) Reagent 8-Hq

The dependence of the Mn(II) blind spot extraction efficiency on the concentration of the complexing agent 8-HQ is shown in Figure 3.5.

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C 8-HQ .10 4 (mol/L)

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From the obtained results, it can be seen that the Mn(II) extraction efficiency increases when the concentration of 8-HQ increases. When the concentration of 8-HQ is 4.0.10 -4 M, the CPE efficiency reaches a maximum of 96.7 ± 1.9%. Then the extraction efficiency decreases when the concentration of 8-HQ continues to increase. Therefore, we choose the concentration of 8-HQ 4.10 -4 M as the optimal value to conduct CPE Mn(II).


Figure 3.5. Effect of 8-HQ concentration on Mn(II) extraction efficiency


C Mn(II) = 0.2 mg/L; pH = 10; C TX-100 = 0.4%

3.1.2.2. Investigation of optimal 8-HQ concentration for blind spot extraction of Cr(III)

Investigation to find the optimal concentration of 8 - HQ for blind spot extraction of Cr(III) in phosphate buffer medium with pH = 8 and fixing other conditions such as: Triton X-100 concentration, NaCl concentration, extraction temperature, extraction time, centrifugation time. Procedure

The experimental procedure is as follows:

+ Pipet 1.0 mL of 20.0 µg/L Cr(III) standard solution into a 10 mL glass centrifuge tube. Add 1.0 mL of pH = 8 borate buffer solution to create an environment for the complexation reaction between Cr(III) and 8-HQ.

+ Add V mL of 2.10 -3 M 8-hydroxyquinoline solution.

+ Add 1.0 mL of 2% Triton X - 100 surfactant solution. Add another 1.0 mL of 5% NaCl solution.

+ Make up to 10 mL with double distilled water, boil in a water bath at 95 o C for 40 minutes.

+ Then, take it out and centrifuge it for 10 minutes at a centrifugation speed of 3500 rpm, cool it by soaking it in ice water for 10 minutes. Separate the aqueous phase to collect the viscous phase, dissolve the viscous phase with 1.0 mL of 0.1M HNO 3 acid solution in CH 3 OH. Quantify Cr by GFAAS method at a wavelength of 357.9 nm.

The experiment was carried out three times, and the average Cr(III) extraction efficiency results are shown in Table 3.4.

Table 3.4. Effect of 8-HQ concentration on Cr(III) extraction efficiency


STT

C 8-HQ .10 4 (M)

H (%)

1

0.5

81.4 ± 1.96

2

1.0

90.4 ± 2.47

3

2.0

97.9 ± 2.92

4

3.0

88.8 ± 3.21

5

4.0

85.8 ± 2.77

6

5.0

83.2 ± 3.62

The dependence of Cr(III) extraction efficiency on the concentration of complexing agent 8-HQ is shown in Figure 3.6. The Cr(III) extraction efficiency increases in the concentration range of 8-HQ 0.5.10 -4 ÷ 2.10 -4 M, then the extraction efficiency gradually decreases when the concentration of 8-HQ increases. The extraction ensures quantification when the concentration of 8-HQ > 1.10 -4 M. The extraction efficiency reaches the highest value of 97.9 ± 2.92 % when the concentration of complexing agent 8-HQ is 2.10 -4 M. Therefore, the concentration value of 8-HQ 2.10 -4 M is used to conduct further studies in

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Cr(III) blind spot extraction.


Figure 3.6. Effect of 8-HQ concentration on Cr(III) extraction efficiency


C Cr(III) = 2.0 μg/L; pH = 8; C TX-100 = 0.2%

3.1.3. Investigation of the influence of surfactants

For blind spot extraction, the selection of micelle-forming surfactants to dissolve the metal complexes is a decisive factor. In recent studies, two types of surfactants commonly used in blind spot extraction are Triton X-100 (TX-100) and Triton X-114 (TX-114). These two types of surfactants were investigated for blind spot extraction of Mn(II) and Cr(III).

3.1.3.1. Investigation of surfactants for Mn(II) extraction

The influence of surfactants TX-100 and TX-114 on the extraction efficiency of Mn(II) blind spot was investigated by fixing the surfactant concentration and factors such as pH, 8-HQ concentration, extraction temperature and time, NaCl concentration, and centrifugation time. The experimental procedure is as follows:

+ Pipet 1.0 mL of 2.0 mg/L Mn(II) standard solution into a 10 mL glass centrifuge tube. Add 2.0 mL of pH = 10 borate buffer solution and 1.0 mL of 4.10 -3 M 8-hydroxyquinoline solution.

+ Add V mL of 4.0 % Triton X-100 solution or V mL of 4.0 % Triton X-114 solution. Add 1.0 mL of 5.0 % NaCl solution and make up to 10 mL with double distilled water.

+ Soak the reaction mixture in a water bath at 95 o C for the time

50 minutes. Then, take it out and centrifuge it for 10 minutes at 3500 rpm, cool it by soaking it in ice water for 10 minutes to let the viscous mixture solidify.

+ Separate and dissolve the viscous phase with 1.0 mL of 0.1M HNO 3 acid solution and determine the Mn concentration in the analytical solution using FAAS technique at a wavelength of 279.5nm. The experiment was carried out 3 times, the average Mn extraction efficiency is presented in Table 3.5.

Table 3.5. Effect of TX-100 and TX-114 concentrations on Mn(II) extraction efficiency



STT

Volume of CHDB 4% (mL)

CHDBM concentration (%)

H (%)

TX-100

TX-114

1

0.25

0.1

75.2 ± 4.1

64.3 ± 3.5

2

0.5

0.2

86.4 ± 3.7

75.6 ± 4.1

3

1.0

0.4

88.4 ± 3.0

84.2 ± 3.1

4

1.5

0.6

93.8 ± 3.3

83.6 ± 2.7

5

2.0

0.8

92.7 ± 2.9

82.6 ± 3.1

6

2.5

1.0

93.6 ± 3.2

81.2 ± 2.9

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The effect of TX-100 and TX-114 concentrations on the extraction efficiency of Mn(II) with the complexing agent 8-HQ is shown in Figure 3.7.


Figure 3.7. Effect of TX-100 concentration on Mn(II) extraction efficiency

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C Mn(II) = 0.2 mg/L; pH = 10;C 8-HQ = 4.10 M

The dependence of Mn(II) blind spot extraction efficiency on the concentration of Triton X-114 surfactant is shown in Figure 3.8.


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Figure 3.8. Effect of TX-114 concentration on Mn(II) extraction efficiency

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C Mn(II) = 0.2 mg/L; pH = 10; C 8-HQ = 4.10 M

In the case of using Triton X-100 surfactant, when increasing the concentration of Triton X-100, the Mn(II) extraction efficiency increased and reached the maximum value of 93.8 ± 3.25% when increasing the concentration of TX-100 by 0.6%. For Triton X-114 surfactant, the extraction efficiency increased when increasing the concentration of Triton X-114 in the range of 0.1% ÷ 0.4%, then the extraction efficiency decreased slightly when increasing the concentration of Triton X-114. The experimental results are completely consistent because when the surfactant content is small, the Mn complex will not be completely dissolved, but when the surfactant concentration is large, the volume of the viscous phase increases, leading to an increase in the viscosity of the sample, thereby reducing the analytical signal.

The extraction efficiency of Mn(II) with the complexing agent 8-HQ in the case of using surfactant Triton X-100 is higher than when using Triton X-114. This can be explained as follows: the chemical formula of Triton X-100 is C₈H₁₇C₆H₄(OCH₂CH₂) n OH with n = 9 ÷ 10, the chemical formula of Triton X-114 is C₈H₁₇C₆H₄(OCH₂CH₂) n OH with n = 7 ÷ 8. Thus, Triton X-100 and Triton X-114 are homologous to each other, because TX-100 has more - OCH₂CH₂ - groups than TX-114, so its ability to dissolve the complex is better. At the same concentration, TX-100 solution has a higher blind spot temperature than TX-114 solution. Therefore, Triton X-100 will form micelles and separate phases more slowly than Triton X-114. Therefore, Triton X-100 will extract MnQ 2 complex better than Triton X-114. Triton X-100 was chosen for further studies on Mn(II) blind spot extraction.

The Mn(II) blind spot extraction can be quantitatively obtained when the Triton concentration is in equilibrium.

X-100 was greater than 0.2%. The highest Mn(II) extraction efficiency reached 93.8 ± 3.25 % at Triton X-100 concentration of 0.6%. Therefore, the Triton X-100 concentration of 0.6% was selected as the optimal concentration for blind spot extraction of Mn(II).

3.1.3.2. Investigation of surfactants for Cr(III) extraction

The influence of type and concentration of surfactant on the blind point extraction of Cr(III) with complexing agent 8-HQ and pH = 8 phosphate buffer system was investigated according to the following procedure:

+ Pipet 1.0 mL of 20.0 µg/L Cr(III) standard solution into a 10 mL glass centrifuge tube. Add 2.0 mL of borate buffer solution pH = 8 and add 1.0 mL of 2.10 -3 M 8-hydroxyquinoline solution.

+ Add V mL of 2% Triton X-100 surfactant solution or V mL of 2% Triton X-114 solution.

+ Add 1.0 mL of 5.0% NaCl electrolyte solution to promote phase separation of TX-100. Make up to 10 mL with double distilled water, soak the reaction mixture in a water bath at 95 o C for 50 minutes.

+ Then, take it out and centrifuge it for 10 minutes at a centrifugation speed of 3500 rpm, cool it by soaking it in ice water for 10 minutes.

+ Separate the viscous phase, dissolve the viscous phase with 1.0 mL of 0.1M HNO 3 acid solution in CH 3 OH. Determine the Cr concentration using GFAAS technique with the optimal conditions of the machine. The average extraction efficiency results of 3 experiments are presented in Table 3.6.

Table 3.6. Effect of TX-100 and TX-114 concentrations on Cr(III) extraction efficiency


CHDB Volume

2% (ml)

CHDBM concentration

(%)

H (%)

TX-100

TX-114

0.125

0.025

41.6 ± 3.2

40.6 ± 4.1

0.25

0.05

67.7 ± 2.9

54.5 ± 3.7

0.5

0.1

90.3 ± 2.6

87.1 ± 3.12

1.0

0.2

93.0 ± 2.8

85.5 ± 3.0

1.5

0.3

87.2 ± 1.9

84.2 ± 2.9

2.0

0.4

87.6 ± 2.4

83.2 ± 3.0

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