: Nina Siebers
: Bentonite Functionalised with 2-(3-(2-aminoethylthio)propylthio)ethanamine (AEPE) for the Removal of Hg(II) from Wastewaters. Synthesis, Characterisation and Hg(II) Adsorption Prop
: Diplomica Verlag GmbH
: 9783836618472
: 1
: CHF 29.20
:
: Naturwissenschaft
: English
: 73
: kein Kopierschutz/DRM
: PC/MAC/eReader/Tablet
: PDF


"In this study, natural bentonite clay was first purified and then functionalised with the chelating ligand 2-(3-(2-aminoethylthio)propyl hio)ethanamine (AEPE) to improve the adsorption capacity and selectivity towards Hg(II) ions. The surface modification was characterised with the help of powder X-ray diffraction (XRD), Fourier transform infrared spectroscopy (FT-IR), BET isotherm to determine the specific surface area while the thermal stability of the samples was studied using thermogravimetric analysis (TGA). FT-IR and TGA demonstrated the presence of the chelating ligand on the modified clay. XRD pattern indicated that the chelating agent AEPE was only grafted onto the surface of the purified bentonite, whereas the interlayer distance did not change. N2 specific surface area measurement also indicated the coverage of AEPE onto the surface of purified bentonite.
Adsorption of Hg(II) ions from aqueous solutions as a function of pH, contact time, initial concentration, ionic strength, interfering ions and adsorbent dose was studied. The adsorption process followed a pseudo-second order kinetics and monolayer adsorption. The adsorption of Hg(II) ions increased with increasing pH and reached a plateau value in the pH range of 4.0-8.0. The removal of Hg(II) was found to be higher than 99% at an initial concentration of 20 mg/L using adsorbent dose of 0.01 g. The presence of NaNO3 as background electrolytes at concentration ranging from 0.01 to 2.0 M decreased the adsorption of Hg(II) ions. Furthermore, the adsorption capacity increased with increasing adsorbent dose. Sorption data analysis was carried out using Langmuir isotherm for the uptake of Hg(II) ions at a concentration range of 20-400 mg/L. The adsorption process was found to be favourable as the separation parameter is less than unity (RL<1). The maximal adsorption capacity was found to be 48.69 mg/g obtained from Langmuir equation."


"Chapter 3.2.2.2 Characterisation of the clay products from purification and modification

All clay products obtained from purification and modification of bentonite were characterised by FT-IR (KBr pellet technique), XRD (flat surface technique) and TGA. Additionally an XRD pattern of raw bentonite was also recorded. The purified bentonite and the final modified bentonite were additionally characterised for surface area with BET isotherm. For FT-IR, a KBr (potassium bromide) pellet technique was used. The KBr pellet was prepared by grinding the solid sample with solid (KBr) and applying great pressure to the dry mixture. The sample was mixed with KBr in a ratio of 1 : 100 (Sample : KBr). The powder X-ray diffraction must be done with finely ground samples. For that, the sample was ground in a mortar until it becomes a fine-grained sample. The sample was put in the middle of the glass slide and pressed flat with another glass slide. Several repeats involving pressing and cleaning off powder around the well were necessary. It was important that the top of the sample be coplanar with the top of the glass slide holder. Then the XRD pattern was recorded. The BET isotherms for the determination of the surface area of the purified and AEPE-bentonite were recorded with N2 as sample gas at -195.8°C."

Bentonite Functionalised with 2-(3-(2-aminoethylthio)propylthio)ethanamine (AEPE) for the Removal of Hg(II) from Wastewaters1
Content3
Abbreviations6
Physical characteristics6
Index of figures8
Index of tables10
Index of schemes11
Index of equations12
Abstract13
1 Introduction14
1.1 General information14
1.1.1 Mercury and resulting environmental problems14
1.1.2 The removal of mercury by adsorption using clay minerals14
1.2 Theoretical Background17
1.2.1 Structure and properties of bentonite17
1.2.2 Chelating agents19
1.2.3 Characterisation techniques20
2 Aims22
3 Experimental23
3.1 Material23
3.1.1 Reagents and chemicals23
3.2 Methods27
3.2.1 Synthesis27
3.2.2 Characterisation30
3.2.3 Adsorption of Hg(II) from aqueous solution31
4 Results and Discussion33
4.1 Characterisation33
4.1.1 1H and 13C NMR spectra of AEPE33
4.1.2 XRD pattern34
4.1.3 FT-IR spectra37
4.1.4 TGA40
4.1.5 BET42
4.2 Adsorption of Hg(II) from aqueous solution44
4.2.1 Effect of pH45
4.2.2 Effect of contact time47
4.2.3 Adsorption isotherm49
4.2.4 Effect of ionic strength53
4.2.5 Interfering ions54
4.2.6 Effect of adsorbent dose and kinetics58
5 Conclusion and Outlook62
6 References63
7 Appendix69