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Logo of ijacInternational Journal of Analytical Chemistry
 
Int J Anal Chem. 2010; 2010: 102146.
Published online 2010 June 27. doi:  10.1155/2010/102146
PMCID: PMC2905694

Calculation of the C3A Percentage in High Sulfur Clinker

Abstract

The aim of this paper is to clarify the influence of the clinker SO3 on the amount of C3A. The calculation of the cement phases percentages is based on the research work, Calculation of the Compounds in Portland Cement, published by Bogue in 1929 .The usage of high sulphur fuels, industrial wastes, and tires changes completely the working condition of Bogue because the assumed phase compositions may change. The results prove that increasing the amount of SO3 in the low alkali clinker decreases the percentages of C3A due to the high incorporation of alumina in the clinker phases mainly C2S and C3S. The correlation is linear till the clinker SO3 reaches the 2%. Over that the influence of the clinker SO3 became undetectable. A new calculation method for the determination of the C3A in the high sulphur and low alkali clinker was proposed.

1. Introduction

Portland cement is a hydraulic material composed primary of calcium silicates, aluminates, and ferrites. In a rotary kiln, at temperature reaching the 1450°C, clinker nodules are produced from a finely ground, homogenised blend of limestone, shale and iron ore.

The nodules are subsequently ground with gypsum, which serves to control setting, to a fine powder to produce finished Portland cement. The composition and texture (crystal size, abundance, and distribution) of clinker phases result from complex interactions of raw feed chemical and mineralogical composition, particle size distribution, feed homogenization, and the heating and cooling regime.

In order to simplify these phenomena, Bogue [1] proposed an approach for the development of the clinker phases. The ferric oxide (Fe2O3) reacts with aluminium oxide (Al2O3) and lime (CaO) to form the tetracalcium aluminoferrite (C4AF or Ca4Al2Fe2O10). The remaining aluminium oxide reacts with lime to form the tricalcium aluminate (C3A or Ca3Al2O6). The lime reacts with the silicate oxide (SiO2) to form two calcium silicates phases, the dicalcium silicate (Belite, C2S or Ca2 SiO4) and tricalcium silicate (Alite, C3S or Ca3SiO5).

Based on the above approach, Bogue proposed four formulae for the calculation of the clinker phase concentrations.

Increasing the amount of the high sulphur fuels and the level of waste valorisation, in the cement kilns, changes completely the working condition of Bogue. The negative influence of sulphate on the percentages of silicate phases (alite and belite) was earlier detected by the XRD but that on the tricalcium aluminate (C3A) is still unclear due to the conclusion contradiction in the reported literature.

2. Influence of Sulphur on Silicate Phases

The sulphates reduce the viscosity and surface tension of the clinker liquid phases, shifting the equilibrium of the melt into unstable range which is characterized by low nucleus forming frequency and high growth rate of crystal leading to stabilization of the Belite crystals. The incorporation of sulphur in the Belite stabilizes the Belite structure, whereby the uptake of CaO is inhibited and the formation is suppressed [2]. This phenomenon increases the amount of Belite and decreases that of Alite in the clinker [3]. This reported conclusion was assured by many investigations done later [2, 4, 5].

3. Influence of Sulphur on Aluminates C3A (Ca3Al2O6)

The composition of the matrix (aluminates and ferrites) is not altered by the level of SO3 in the clinker [6]. In particularly the amount of the tricalcium aluminate (Ca3Al2O6) is not affected by the SO3 level [2, 7]. This conclusion was not compatible with the observation of Hamou-Tagnit and Sarker, indicating that increasing the SO3 level increases the amount of Ca3Al2O6 in the clinker [8] where the conclusion of Borgholm and Jons showed the opposite [9].

These contradictions in the literature were due to the fact that many parameters could affect the development of C3A (Ca3Al2O6) principally the kiln atmosphere and the raw meal chemistry. Locher and others [10] detect that the kiln atmosphere, especially the amount of oxygen, had an influence on the amount of C3A. Reducing kiln atmosphere inhibits partly the oxidation of the bivalent iron (Fe2+), presented in the kiln feed, leading to increase in the amount of C3A.

The sulphur introduced into the cement kiln from both sides, the kiln feed and kiln burner, is in chemically reduced form such as S0, S1−, and S2−. These sulphur forms are oxidized to S4+ and S6+ in the kiln system. This oxidizing process consumes some oxygen quantity leading to a reduction in the amount of oxygen in the kiln system.

The presence of sodium oxide in the kiln feed affects the amount of C3A [11]. One of the forms of sodium oxide in the clinker is the Na2O · 8CaO · 3Al2O3· At clinkering temperature this compound reacts with sulphur to produce the Na2SO4 and C3A [11].

This study will focus only on the influence of the SO3 on the development of C3A (Ca3Al2O6). The other factors listed above are controlled to avoid any interaction with the results.

4. Experimental Procedure

The development of the Tricalcium aluminates Ca3Al2O6, in the cement kiln production, is affected by many parameters such as the kiln atmosphere [10] and the amount of sodium oxide in the raw feed [11]. This could be the reason of the large contradiction in the conclusion of the reported investigations.

In order to avoid any interactions, not only from the chemical compounds but also that related to the kiln operation, the clinker samples were selected in a stable kiln production operation conditions. All samples are commercial clinker, sampled from Cimenterie Nationale SAL. The free lime of the clinker was less than 1% and the percentage of the kiln inlet oxygen was around 3%. The samples were analyzed immediately, to avoid any influence from storage and humidity.

The variation of the clinker SO3 was made by changing the fuel type in the main burner as follows:

  1. fuel oil containing 2.0% S,
  2. petroleum coke containing 4.5% S,
  3. petroleum coke containing 6.0% S.

The chemical and mineralogical analyses were done respectively according to ASTM C114 and ASTM C1365 standards. The calibration of the ARL 9800 was done using NIST standards. The fusion Claisse machine and the Herzog HTP 40 press were used for the sample preparation of the chemical and mineralogical analysis. The KOSH (potassium hydroxide and sucrose) method was implemented in order to detect the percentage of SO3 and Al2O3 in the silicate phases.

5. Results and Discussion

The results (Figure 1) showed an obvious influence of the SO3 percentages on the amount of C3A in the low alkali clinker. In all samples, the measured percentages of C3A were lower than the calculated.

Figure 1
Influence of the clinker SO3 on the C3A.

The correlation between the amount of C3A (Ca3Al2O6) and the total percentages of clinker SO3 was linear till the clinker SO3 reached just 2%. Over that the influence of the clinker SO3 becomes indistinguishable since the standard deviation of the results according to ASTM C1365:06 is 0.47.

The results in Table 1 show that the ratio of the aluminium oxide and SO3 in the silicate phases vary from 4.18 in the low clinker sulphur, to 1.33 in the high one.

Table 1
Chemical and mineralogical analysis results.

Bonafous and other [12] noticed that this ratio is 2.  This conclusion was based on their finding that in the presence of sulphur, 3Si4+, in the silicate phases, is substituted by 2Al3+ + S6+.

Taylor [13] declared that this ratio is nearly more than 2, even in individual X-ray microanalyses, due to the presence of other substitutions and the accuracy of the results.

Our findings and especially the results of the samples 2 to 10 conform to the previous conclusions.

The reason of the high ratio in the low sulphur clinker is coming from the fact that at low temperature the Al3+ incorporates first in the silicate phases.

The alumina incorporated in the silicate phases is divided into two groups. The first one enters the structure at low temperature and without the influence of sulphur. In the absence of SO3 there is an excess of nontetrahedral cations and the number of oxygen atoms lie close to the ideal number for stoichiometric Ca2SiO4 [14]. This suggests interstitial stuffing of large cation as the main mechanism for accommodating Al on the Si site before significant solid solution of S takes place [14]. The second one is incorporated in the silicate phases with the influence of sulphur. This phenomenon is improved when the temperature exceed the 1200°C [12].

In the first sample, the ratio Al3+/S6+ is 4.18. In this case, part of the alumina is incorporated into the silicate phases without the influence of sulfate.

The amount of SO3 in the silicate phases is 0.22% and that for Al2O3 is 0.92 (Table 1).

Based on the findings of Bonafous and other [12] the ratio Al3+/S6+ is 2. The calculated amount of alumina entered into the silicate phase crystals with the influence of sulphur in the first sample is 0.22 × 2 = 0.44%. The amount of alumina entered into the silicate phase crystals without the influence of sulphur in the first sample is 0.92 – 0.44 = 0.48%.

The entry of alumina into silicate phase reduces the amount available for the C3A formation. The amount, of the first group, is influenced to an important degree by the changes in the composition of the ferrite compound [15] and it is compensated by the replacement of Al3+ by other ions in the C3A crystal, mainly the Si4+ and Fe3+ [16]. These phenomena lead to minimize the effect of the first group on the amount of C3A. The measured amount of the C3A becomes less than that calculated by Bogue by an average of only 3% [15].

The amount of sulphur in the silicate phases depend on the percentages of belite. The concentration of sulfate in belite is 4 to 5 time that in alite [13]. Regarding the second group, the incorporation of sulfate in the Alite and Belite, tends to increase the amount of alumina in the silicate phases [16]. This phenomenon was shown in the clinker samples 2 to 10. The incorporation of alumina was increased, in correlation with the sulfate, in the silicate phases. The ratio of Al2O3/SO3, in the silicate phase, became around 2.

Bonafous and other [12] explain the ability of silicate phases, principally the belite, to accept simultaneously Al and S at higher dosage by the existence of synergism between both. The presence of AlO4 5−decreases the negative charge induced by the substitution of SO4 2− for SiO4 4− [12]. The calculation of the sulphate phases becomes inaccurate when the percentage of clinker SO3 exceeds 1%. The reason for that is related to the SO3/Alkali ratio. At lower ratio, sulphate preferably combines with alkali to generate the Acranite K2SO4 and Aphtihitalite (K3Na (SO4)2) [17]. Increasing the ratio leads to the development of calcium langbeinite (Ca2K2 (SO4)3) [17]. In remarkably high ratios of SO3/Alkali and SO3 content, the anhydrite CaSO4 has been detected in particular clinkers [14, 18, 19].

The incorporation of alumina in the silicate phases seams to stop (samples 11 and 12) when the clinker SO3 exceeds the 2%.

Our result conforms to previous findings. Taylor calculated the maximum probable amount of SO3 in the silicate phases to be about 0.8% [13]. Miller and Tang found the largest amount of SO3 present in the silicate phases to be 0.68% [20]. The extra amount of sulphate shown in the over 2% clinker SO3 (samples 11 and 12) could come from the presence of anhydrite in the solid phase since it is not in correlation with the alumina.

The first group of alumina was calculated from the first sample with the lower clinker sulphate. The calculation of the second group of alumina in the silicate phase was done by detecting the amount of the first group (0.48) from the total amount of alumina in the silicate phases.

The correlation between the total clinker SO3 and the amount of alumina incorporated in the silicate phases, under the influence of sulphur, is acceptable (Figure 2). The percentages of alumina in the silicate phase, forced by the sulphur, became 0.469 × %SO3 + 0.15.

Figure 2
Relation between the total clinker SO3 and the alumina incorporated in the silicate phases forced by sulphur.

The first group of alumina incorporated in the silicate phases, without the sulphur influence, is compensated by the substitution of other elements, where as the second one is not (Figure 1).

The impurities are one of the main factors of the stabilization of various clinker crystalline forms. The most important consequence of the occurrence of impurities in the lattices of matrix clinker compounds is a disagreement between the calculated and real amount of phases in clinker.

The amount of C3A in high sulphur clinker could be calculated by the following formula:

% of C3A = 2.65 × (%Al2O3 – (%Al2O3 (Silicate  phases)) −1.692 × %Fe2O3

    C3A=  2.65  ×  (%Al2O3(0.469  ×  %SO3  +  0.15))1.692  ×  %Fe2O3.
(1)

In the proposed formula, the percentage of SO3 will be equal to 2 when the clinker SO3 exceeds the 2%, because over this limit the amount of alumina, in the silicate phases, becomes constant regardless the clinker SO3.

The calculated C3A amount by the new formula is more realistic than that calculated by Bogue formula (Table 2).

Table 2
Comparison of the C3A results.

6. Conclusion

Increasing the amount of SO3 in the low alkali clinker decreases the percentages of C3A due to the high incorporation of alumina in the silicate phases. The correlation is linear till the clinker SO3 reaches the 2%. Over that the SO3 influence became undetectable.

In order to be more realistic, the proposed calculation of the C3A percentages takes into consideration the Al2O3 loss. The outcome shows that the new calculated results match more closely with the measured one, than with those calculated by Bogue formula.

References

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