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Estimation of various Aluminum bearing phases in Bauxite using XRF and TGA

Estimation of various Aluminum bearing phases in Bauxite using XRF and TGA

An investigation  to understand the  efficacy of Xray Diffraction for the  estimation  of various Aluminum bearing  phases  in Bauxite in comparison to Thermogravimetric analysis:

Bauxite is the major source of Aluminum. Trihydrate alumina (Al2O3, 3 H2O) or Gibbsite, also known as low temperature alumina due to its lower extraction  temperature is the  major aluminum bearing material.  Along with Gibbsite, Boehmite or Diaspore both  of which are monohydrate alumina (Al2O3, H2O) are  the  other  aluminum  bearing  materials  in Bauxite. Extraction of these monohydrate phases require considerably higher temperature that leads to  additional  energy  cost  and  thus  accurate  estimation  of trihydrate  and  monohydrate alumina in Bauxite is of high importance  from the viewpoint of economic viability.

The typical wet chemical approach to estimate  trihydrate  alumina involves caustic digestion in the  range  of 140°C to 150°C temperature whereas  the  estimation  of the  monohydrate alumina requires  significantly higher temperature in excess of 200°C in presence  of strong caustic solution. The process is extremely hazardous as it involves handling of caustic solution at  elevated  temperatures and  can cause  serious  injuries to  the  persons  involved. It also involves use of typical vessels with high durability and strict maintenance protocol  of the experimental  set up, thereby  requiring a safer and faster alternative  that can bypass use of hazardous chemicals.

In our  laboratory  we  have  studied  4 such bauxite  samples  using thermogravimetry and powder   X   ray  diffraction  to  understand  the  mineralogical  nature   of  the  bauxite  and subsequent quantification  of Aluminum bearing phases were also attempted. The samples were  subjected  to  TG  analysis as  well as  Xray diffraction.  Total Al2O3   content  was  also estimated using typical wet chemical approach that involves complexometric titration.

The TG curves were interpretated and from the weight loss patterns in the range of 150°C to
350°C and 450°C to 550°C respectively, estimation  of try hydrate and mono hydrate alumina content  were  attempted. The summary  of the  weight  loss and  corresponding  calculated aluminum bearing phase contents  are tabulated in table 1.

Table 1: Summary of TG data

Sample ID

Weight Loss

Corresponding trihydrate Alumina

Weight loss

Corresponding Monohydrate Alumina

Total Al2O3 content

1

16.386

47.35

2.370

15.81

44.22

2

15.172

43.84

2.653

17.70

31.43

3

16.386

47.35

2.370

15.81

43.54

4

12.257

35.42

2.620

17.48

37.881

 

On the other  side, PXRD analysis were carried out for the same set of samples and phase quantification  was attempted using Rietveld refinement. The phase  composition  of all the samples are tabulated in table 2 


Table 2: Summary of PXRD data

Sample ID

Aluminium bearing Phases

% Phase composition

Total Al2O3

content

% Al2O3 from wet analysis

1

Diaspore (Al2O3, H2O)

6.22

36.97

38.01

 

Boehmite (Al2O3, H2O)

10.23

 

 

 

Gibbsite (Al2O3, 3 H2O)

61.93

 

 

 

Kaolinite (Al2O3.2SiO2.2H2O)

3.28

 

 

2

Diaspore (Al2O3, H2O)

9.06

32.24

32.68

 

Boehmite (Al2O3, H2O)

6.95

 

 

 

Gibbsite (Al2O3, 3 H2O)

51.85

 

 

 

Kaolinite (Al2O3.2SiO2.2H2O)

5.02

 

 

3

Diaspore (Al2O3, H2O)

13.23

33.43

33.32

 

Boehmite (Al2O3, H2O)

6.40

 

 

 

Gibbsite (Al2O3, 3 H2O)

52.48

 

 

 

Kaolinite (Al2O3.2SiO2.2H2O)

5.57

 

 

4

Diaspore (Al2O3, H2O)

8.34

30.35

31.41

 

Boehmite (Al2O3, H2O)

3.63

 

 

 

Gibbsite (Al2O3, 3 H2O)

47.68

 

 

 

Kaolinite (Al2O3.2SiO2.2H2O)

7.63

 

 

 

The total Alumina content  of the samples were also measured with a classical wet technique and  a comparison  was made  to  understand the  efficiency of the  instrumental processes involved. The total  alumina  content  obtained  from the  wet  experiments  was is in good agreement with the calculated total Al2O3  content  obtained  from the XRD experiments.  On the other hand, the data obtained from the weight loss observed in the TG patterns resulted in much higher recoveries with comparison to the PXRD and wet analysis. This is consistent with the nature of the Gibbsitic material and a plethora of literature data can be found where a thermogravimetric factor is required to properly estimate the tri and monohydrate alumina contents  using TG method  which is beyond the scope of this work. From the powder  Xray data,  besides  mono  and  trihydrate alumina  phases,  presence  of kaolinite  clay was  also confirmed. The same is difficult to identify in the TG thermogram as no water loss peak was observed  for kaolinite.  The TG  thermogram accounts  for only the  mono and  trihydrate alumina and  missed out  on the  clay mineral which will also contribute in the total  Al2O3 obtained in the wet methods. As evident from the data, the PXRD analysis appears to be more robust as it does not require usage of certain factors which are purely empirical in nature and may often mislead. The PXRD method also employs a much larger sample quantity compared to the TG method  and thus nullifies the issue of heterogeneity to a large extent.  It can also provide information on all the crystalline aluminum bearing phases that is often not possible in the TG method. 

TG thermograms of samples 1-4 (Top to bottom)

 

Rietveld Refinement for samples 1-4 with phase composition (Top to bottom)

Although, for the purpose of the aluminum extraction the information of total trihydrate and monohydrate alumina content  is sufficient and PXRD analysis is capable enough to provide information  on  that  thereby  providing an  alternative  analytical pathway  which is rapid, effective, sufficiently accurate and does not involve hazardous chemicals and intensive energy consumption.

 

Contributed By: Dr. Arijit Goswami, Dr. Satirtha Sengupta and Alakta Saha
 

 


 

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