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Infinite dilution activity coefficient measurements of organic solutes in fluorinated ionic liquids by gas-liquid chromatography and the inert gas stripping method

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par Kaniki TUMBA
University of Kwazalu-Natal - Master 2009
  

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4.2. The inert gas stripping technique

4.2.1. Chemicals

To validate the method, experiments were performed with NMP as solvent whereas n-hexane, hex-1-ene, hex-1-yne, methanol, cyclohexane, benzene and acetone were used as solutes in the ionic liquid trihexyltetradecylphosphonium bis (trifluoromethylsulfonyl) imide, [3C6C14P] [BTI]. Appendix C provides additional information about the solvents, including their source, purity, density and refractive index. No further purification was undertaken for the solutes as they were of high purity. Solvents were purified by heat treatment under vacuum.

4.2.2. Experimental Set-up

As part of this study, it was intended to construct an entire inert gas stripping set up with an equilibrium cell able to accommodate small volumes of samples, less than 50 g. This was a necessity since ionic liquids are very expensive chemicals. The second reason why a dilutor cell was needed is for systems that are not suitable when using the GLC technique. Examples of these are systems involving solutes that are solid at room temperature, solvent mixtures and those leading to a very long retention time. Design parameters for the dilutor cell were discussed in the previous chapter. The greatest part of the design work was centered on the dilutor cell as it is the most determinant piece of the set up performance. Figure 4-1 presents the simplified flow diagram of the set up used in this study, which is similar to the one described by Krummen et al. (2000) and Coquelet and Richon (2005). Photograph 4-2 gives the experimental set up of the inert gas stripping apparatus.

Figure 4-1: Flow diagram of the experimental set up for the inert gas stripping method.
A-Helium, Nitrogen and air supply for the GC; B- Nitrogen line; C-Valve; D- flow regulator; E-
Immersion temperature controller; F-Coil tube (Heat exchanger); G-Transparent acrylic bath; H- Dilutor
cell; I-Capillaries; J-Presaturation cell; K-Platinum resistance thermometer; L-Pressure transducer; M-
Sampling valve; N-GC apparatus; O-PC monitor; P-Cold trap; Q- Coil tube (Heat exchanger); R-Soap
bubble flow-meter; S-Magnetic stirrer.

4.2.2.1. Gas cylinders

Four gases are used in this work:

· Nitrogen as stripping gas;

· Helium as carrier gas for the GC apparatus;

· Air and Hydrogen to produce the ignition flame for the GC (FID only).

The four cylinders containing the above gases are fitted with regulators. Nitrogen flow rate is controlled by a smaller regulator. Its value is determined by means of a soap bubble flow meter.

4.2.2.2. Water bath

An 18-litre transparent acrylic water bath, with maximum allowed temperature of 70 oC, was used to accommodate the cells during experiments. During experiments, leaks could be easily detected by the observation of gas bubbles, due to the transparency of the bath. A Haake Difisons temperature controller kept the water in the bath at a constant temperature set before each run. The nitrogen line (1/4 inch inner diameter and 12 m long) was coiled and immersed in the water bath to allow the gas to equilibrate to the set-point temperature before entering the cells. In order to reduce heat loss to the atmosphere, the water surface in the bath was completely covered with polystyrene chips. The temperature stability of the bath was #177;0.1 K.

4.2.2.3. Cells

The two glass cells are identical and have a total volume of 50 cm3 each. They were made for the purpose of this work by a Durban glass blower, Mr. Peter Siegling. Metallic parts were manufactured and fitted by the School of Chemical Engineering workshop staff members, Mr. Ken Jack and Mr. Kelly Robertson. The shape is similar to the cells previously used by other researchers (Coquelet and Richon 2005). Mass transfer considerations discussed by Richon et al. (1980) were taken into account to determine the cell height using equation (3-95), assuming

the degree of the equilibrium attainment = 0.99 From the literature, ranges of different

properties related to FILs (See table 2-2) were used in equation (3-95) to find out the most suitable height for the cell. The same procedure was used by Li et al. (1993) to find out the optimum height of the dilutor cell used in the study of IDAC`s for nonelectrolytes solutes in water. For systems involving ionic liquids, the presaturator cell was removed. As shown in Photograph 4-3, the dilutor cell is fitted with ten stainless steel capillaries (0.1 mm inner diameter) purchased from Anatech, through which the stripping gas is introduced. During experiments, they should be placed in such a way that bubbles are not directed to the vortex. This will prevent bubbles coalescence (George 2008). A class A Pt-100 temperature sensor (length 250 mm, outer diameter 3 mm and limiting error of 0.25 oC) fitted with stainless steel pot seal and a Sensotec pressure transducer are inserted in order to measure the temperature of

the mixture and the pressure in the dilutor cell. To obtain accurate readings, both sensors had to be calibrated. A CTH 6500 digital thermometer (accuracy: #177;0.03 %) and a CPH 6000 pressure calibration standard (accuracy: #177;0.1 %) for temperature and pressor sensor calibrations, respectively. The bolt (G) along with the Teflon piece (H) seal the cell to ensure that no portion of nitrogen flows through other channels than the provided capillaries. Agitation of the solution contained in the cell is achieved by means of a magnetic stirrer. Other features of the designed cell are given by Photograph 4-3.

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