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Texture and structural refinement and quantitative Rietveld analysis of crystalline deposits to support failure investigations

Published online by Cambridge University Press:  10 April 2025

Husin Sitepu*
Affiliation:
Research & Analytical Services Department, Saudi Aramco, Dhahran, Saudi Arabia
Noktan M. AlYami
Affiliation:
Research & Analytical Services Department, Saudi Aramco, Dhahran, Saudi Arabia
Ibrahim M. Al-Zahrani
Affiliation:
Research & Analytical Services Department, Saudi Aramco, Dhahran, Saudi Arabia
*
a)Author to whom correspondence should be addressed. Electronic mail: husin_sitepu@yahoo.com

Abstract

In the present study, the High Score Plus software (Malvern Panalytical, 2014), combined with the PDF-4+ database release 2023 (ICDD, 2018), was used to perform phase identification from all the powder XRD data sets of 0.5 g by weight of the crystalline deposits from various units of refineries and gas plants. Subsequently, the Rietveld method with the generalized spherical harmonic description for preferred orientation correction [Von Dreele (1997). Journal of Applied Crystallography 30: 517–25; Sitepu (2002). Journal of Applied Crystallography 35: 274–77; Sitepu et al., (2005). Journal of Applied Crystallography 38: 158–67; Sitepu (2009). Powder Diffraction 24: 315–26] were used to determine texture and crystal structure refinement of scale deposits (calcite – CaCO3) from the boiler equipment at a gas plant and quantitative phase analysis of (i) iron oxide corrosion products from the boiler tube, (ii) synthetic mixtures of 87.0 wt% by weight of barite (BaSO4), 10.0 wt% by weight of hematite (Fe2O3), and 3.0 wt% by weight of quartz (SiO2), (iii) iron oxide corrosion products from the affected equipment parts in a refinery, (iv) vanadium oxide (V2O5), sodium vanadium oxide (NaV2O5), sodium vanadium sulfate hydrate (Na2V(SO4)2⋅H2O), and mackinawite (FeS) compounds found in the ash deposits from an external surface of the boiler tubes in a refinery, and (v) iron sulfide corrosion products found at the affected equipment in the sulfur recovery unit. The results revealed that the phase identification of powder XRD data is an excellent tool to determine the nature, source, and formation mechanism of crystalline deposits – part of the scale and corrosion products formed by the processes in the various units of refineries and gas plants. The quantitative Rietveld analysis results serve to guide the engineers at the refinery and gas plants to overcome the problems by applying the right procedures. For example, for iron oxide corrosion products, at a high temperature, magnetite will coat the iron/steel to prevent oxygen reaching the underlying metal. At low temperature, lepidocrocite formed and with time it transformed into the most stable goethite. Akaganeite is formed in marine environments. Additionally, for iron sulfide corrosion products, pyrophoric iron sulfide (pyrrhotite – FeS) results from the corrosive action of sulfur compounds (H2S) and moisture on the iron (steel). Additionally, for the crystalline ash samples from an external surface of the boiler tubes in a refinery, if sodium and vanadium compounds appear, the fuel oil is poor. For the boiler crystalline deposits, if a hematite phase appears, it means that the boiler feed water contains dissolved oxygen; and if the metallic copper appears among the crystalline deposits, it indicates erosion in the boiler tubes, and therefore, special precaution is required to prevent the plating out of copper during cleaning operations. Finally, for crystalline deposits from the steam drum equipment at the sulfur recovery unit, if magnetite has a high quantity, it indicates the presence of dissolved oxygen in the boiler feed water.

Information

Type
Technical Article
Copyright
© The Author(s), 2025. Published by Cambridge University Press on behalf of International Centre for Diffraction Data
Figure 0

TABLE I. Summary of the WDXRF elements concentration (wt%) and phase identification results of powder XRD data of the 0.5 wt% by weight of the crystalline deposits along with the quantitative Rietveld analysis results (wt%) for each of the identified phases.

Figure 1

Figure 1. Schematics of the (a) parts of the powder XRD goniometer and optics and (b) integration of XRF with powder XRD as well as with the Rietveld method (Sitepu et al., 2024).

Figure 2

Figure 2. The Rietveld fit for the whole powder XRD pattern of the inorganic crystalline materials of scale deposits in the form of calcite (CaCO3) obtained from the Rietveld refinement with a generalized spherical harmonic description for preferred crystallographic orientation correction. The observed data are indicated by a plus sign and the calculated profile is the solid line in the same field. The sets of vertical lines below the profiles represent the positions of all possible Bragg reflections for the calcite phase.

Figure 3

TABLE II. Summary of the refined cell parameters of calcite (CaCO3) of the approximately 0.5 g by weight of the inorganic crystalline materials of scale deposits in the form of calcite (CaCO3) obtained from the Rietveld refinement with a generalized spherical harmonic description for the preferred orientation correction.

Figure 4

TABLE III. Summary of the refined atomic positions of the approximately 0.5 g by weight of the inorganic crystalline materials of scale deposits in the form of calcite (CaCO3) obtained from the Rietveld refinement with a generalized spherical harmonic description for the preferred orientation correction.

Figure 5

TABLE IV. Summary of the figure-of-merit and goodness-of-fit index of approximately 0.5 g by weight of the inorganic crystalline materials of scale deposits in the form of calcite (CaCO3) obtained from the Rietveld refinement with a generalized spherical harmonic description for the preferred orientation correction.

Figure 6

Figure 3. The pole density distribution plot for <104> for calcite (CaCO3) data is derived from the Rietveld refinement with a generalized spherical harmonic description for the preferred orientation correction. The pole density distribution function is maximum at the orientation angle φ = 0° and minimum at φ = 90°. The φ is the angle between the pressing axis and the normal of the (104) calcite plane. The pole density distribution function is unity if the corrosion deposits are randomly oriented, and yields no variation between the crystallographic orientation correction factor and the orientation angle (i.e., straight line).

Figure 7

Figure 4. The comparison between the calculated and measured powder XRD patterns from 0.6 to 6.0 Å of the d-spacings (horizontal) for the corrosion deposits from the boiler following the Rietveld refinement with a generalized spherical harmonic description for the preferred orientation correction. The observed data are indicated by a plus sign and the calculated profile is the solid line in the same field. The sets of vertical lines below the profiles represent the positions of all possible Bragg reflections for the magnetite, hematite, goethite, and quartz phases.

Figure 8

Figure 5. Variation between the quantitative phase analysis results (wt%) obtained from the Rietveld refinement with the generalized spherical harmonic description for the crystallographic preferred orientation correction and the identified phases for corrosion deposits from the specific boiler equipment in the gas plant.

Figure 9

Figure 6. Variation between the March preferred orientation corrections with orientation angle derived from the Rietveld refinement with the generalized spherical harmonic description for the crystallographic preferred orientation correction and the identified phases for (a) the <001> magnetite (Fe3O4) and (b) the <001> hematite (Fe2O3). The pole density distribution function is maximum at the orientation angle φ = 0° and minimum at φ = 90°. The φ is the angle between the pressing axis and the normal of the (001) magnetite and hematite planes. The pole density distribution function is unity if the corrosion deposits are randomly oriented.

Figure 10

TABLE V. Summary of the refined structure parameters and weight percentage (wt%) results for the mixture of barite (87.0 wt% by weight), quartz (10.0 wt% by weight), and hematite (3.0 wt% by weight) obtained from the Rietveld refinement with the generalized spherical harmonic description.

Figure 11

Figure 7. Variation between the quantitative phase analysis results (wt%) obtained from the Rietveld refinement, with the generalized spherical harmonic description for the crystallographic preferred orientation correction, and the identified phases for the powder XRD data of the synthetic mixture of barite (87.0 wt% by weight), quartz (10.0 wt% by weight), and hematite (3.0 wt% by weight).

Figure 12

Figure 8. Variation between the weight percentage (wt%) and the identified phases for corrosion crystalline deposits from the specific boiler equipment in a gas plant, obtained from the Rietveld refinement with the generalized spherical harmonic description.

Figure 13

Figure 9. Phase composition results obtained from the Rietveld refinement with the generalized spherical harmonic description for each of the identified phases of powder XRD data of the crystalline ash deposits from the external surface of the boiler tubes in the refinery.

Figure 14

Figure 10. Quantitative Rietveld analysis (phase composition, wt%) results obtained from the Rietveld method with the generalized spherical harmonic description for the preferred orientation correction for all of the powder XRD data sets of crystalline materials part of deposits from the affected equipment at the sulfur recovery unit − (a) condenser tube side #1, condenser #4, and condenser manway cover; and (b) inlet head, waste tubes, condenser #1 tubes, condenser #4 inlets, condenser #4 tubes, and steam drum.