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PROJECT TOPIC- SOLVENT EXTRACTION STUDIES ON Zn(II) AND Cd(II) COMPLEXES OF 1,5-DIMETHYL-2-PHENYL-4[(E)-(2,3,4- TRIHYDROXYPHENYL)]DIAZENYL-1,2-DIHYDROXYL-3HPYRAZOL- 3-ONE

PROJECT TOPIC- SOLVENT EXTRACTION STUDIES ON Zn(II) AND Cd(II) COMPLEXES OF 1,5-DIMETHYL-2-PHENYL-4[(E)-(2,3,4- TRIHYDROXYPHENYL)]DIAZENYL-1,2-DIHYDROXYL-3HPYRAZOL- 3-ONE

 

ABSTRACT

The azo-ligand, 1,5-dimethyl-2-phenyl-4-[(E)-(2,3,4-trihydroxylphenyl) diazenyl]- 1,2-dihydro-3H-pyrazol-3-one (H3L) and its Zn(II) and Cd(II) complexes have been synthesized and characterized based on stoichiometric, molar conductance, electronic and infra-red spectral studies. The results showed that H3L reacted with the metals in 2:1 ratio. H3L coordination was through the hydroxyl, azo and carbonyl groups to form [Zn(H2L)2]2+ and [Cd(H2L)2]2+ respectively. Solvent extraction studies on Zn(II) and Cd(II) using 1,5- dimethyl-2-phenyl-4-[(E)-(2,3,4-trihydroxylphenyl) diazenyl]-1,2-dihydro-3H-pyrazol-3-one were carried out with CHCl3. Effects of other extraction variables like, pH, salting-out agent, masking agent and acids were also investigated. Cd(II) was quantitatively extracted in 0.001 M HCl up to 100%; and 0.001 M of either thiocyanate, or 0.001 M tatrate masked Cd(II) up to 90%, under five minutes. Extraction of Zn(II) with H3L/CHCl3 was quantitative in 0.001 M HCl up to 96% under seventy minutes. In the same vein, 1 M cyanide and 1 M thiocyanate masked it up to 79% and 67% respectively. Cd(II) was successfully separated from Zn(II) following four-cycle extraction up to 96.5% in 0.001 M HCl using H3L/CHCl3 in the presence of 1 M cyanide. Recovery of Zn(II) and Cd(II) from rubber carpet was up to 90% and 85% respectively under the established parameters. The extraction constant was established for both Zn(II) and Cd(II) complexes from the results obtained from pH, where the slope was 0.141 and 0.0516, and the extraction constant 7.316 and 3.899 respectively. Hence, H3L is a promising extractant for Zn(II) and Cd(II) ions.

CHAPTER ONE
1.0 INTRODUCTION

During the years 1900 to 1940, solvent extraction was mainly used by the organic chemist for separating organic substances. Since in these systems, the solute, (desired component) often exist in only one single molecular form, such system are referred to as nonreactive system1. However, it was also discovered that mainly weak acids could complex metals in the aqueous phase to form complex soluble in organic solvent. This is an indication
that organic acid may be taken from the aqueous or the organic phase; such system is referred to as reactive system.

This has become a tool for analytical chemist, when the extracted metal complex showed a specific colour that could be identified spectrometrically.
Solvent extraction is a process whereby two immiscible liquids are vigorously shaken in an attempt to disperse one in the other so that solutes can migrate from one solvent to the other2. When the two liquids are not shaken the solvent to solvent interface area is limited to the geometric area of the circle separating the two solvents. However as the two liquids are vigorously shaken the solvents become intimately dispersed in each other.

The dispersal is in the form of droplets. The more vigorous the shaking the smaller the droplets will be. The smaller the droplets are, the more surface area there is between the two solvents. The more the surface area between the two solvents, the smaller the linear distance will be that molecules will travel to reach the other solvent and migrate into it. The shorter the linear distance travelled by the molecules, the more rapid will be the extraction. The fundamental reason for molecules to migrate from one phase into another is solubility.

The molecules will preferentially migrate to the solvent where they have the greatest solubility. If the molecules are very polar they will generally favour the aqueous phase. If the molecules are non-polar they will favour the organic phase. The key concept to take away at this point is that the process of solvent extraction requires that the chemist adjust the solution conditions so that the radionuclide of interest is in the proper oxidation state and the solution pH is adjusted so that the appropriate complexing agent will form a neutral complex that will easily migrate into the organic phase based on those chemical conditions1.
Solvent extraction has been used predominantly for the isolation and pre-concentration of a single chemical species prior to its determination3; it may also be applied to the extraction of group of metals or classes of organic compounds, prior to their determination by techniques such as atomic absorption or chromatography. Solutes have differing solubilities in different liquids due to variation in the strength of the interaction of solute molecules with those of the solvent. For this reason, the choice of solvent for extraction is governed by the following:
1. A high distribution ratio for the solute and a low distribution ratio for undesirable impurity.
2. Low solubility in the aqueous phase.

3. Sufficient low viscosity and sufficient density difference from the aqueous phase to avoid the formation of emulsion.
4. Low toxicity and flammability.
5. Ease of recovery of solute from the solvent for subsequent analytical processing. Thus the boiling point of the solvent and the ease of stripping by chemical reagents merit attention when a choice is possible. Sometimes, mixed solvent may be used to improve the above properties; and salting-out agent may also improve extractability.

PROJECT TOPIC- SOLVENT EXTRACTION STUDIES ON Zn(II) AND Cd(II) COMPLEXES OF 1,5-DIMETHYL-2-PHENYL-4[(E)-(2,3,4- TRIHYDROXYPHENYL)]DIAZENYL-1,2-DIHYDROXYL-3HPYRAZOL- 3-ONE

 

1.1 The Solvent Extraction Process

There are five general steps that are involved in the solvent extraction process2. They rely on the fact that the solution conditions have been optimized to maximize the extraction for one radionuclide over the others: The first step is to ensure that the proper complexing agents have been added to the aqueous phase so that the extractable complex is of sufficiently low charge density, so that the transfer of the radionuclide to the organic phase will be
maximized. In the second step, the equilibration process occurs by shaking of the separatory funnel.

Unless otherwise specifically noted in a particular method, the amount of time that the two phases are shaken during this step is about two minutes. The initial organic phase is separated and set aside. Step three involves a process known as re-extraction1. The original aqueous phase is extracted with a fresh aliquot of the organic phase of the same volume as the first. This improves the efficiency of extraction of the radionuclide of interest. After step two is repeated the two organic phases are combined.

The aqueous phases are discarded at this point unless they are needed for analysis of radionuclide not extracted. In step four the combined organic phases are equilibrated with a solution of aqueous phase that is of the same composition as the original sample solution, but without any sample. This step helps to ensure that any interfering materials that may have been extracted are re-distributed back to the aqueous phase, while the radionuclide of interest remains in the organic phase. This phase known as the wash is then discarded. The final step is to strip the radionuclide of interest back into an aqueous phase using a pH and lower concentration of complexing agent so that migration back to the aqueous phase is favourable

1.2 Kinetics of Extraction

It is important to investigate the rate at which the solute is transferred between the organic and aqueous phase. In some cases, by an alteration of the contact time, it is possible to alter the selectivity of the extraction. For instance, the extraction of palladium or nickel can be very slow because the rate of ligand exchange at these metal centres, which is much lower than the rates for iron or silver complexes.

1.3 Properties of Liquids

If the externally imposed conditions of pressure and temperature permit a substance to be in the liquid state of aggregation, it possesses certain general properties; that is, it flow

PROJECT TOPIC- SOLVENT EXTRACTION STUDIES ON Zn(II) AND Cd(II) COMPLEXES OF 1,5-DIMETHYL-2-PHENYL-4[(E)-(2,3,4- TRIHYDROXYPHENYL)]DIAZENYL-1,2-DIHYDROXYL-3HPYRAZOL- 3-ONE

 

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