Evolution of heat during the synthesis of ­hydrosilicates in aerated concrete

The heat evolved during the synthesis of 11.3 Å tobermorite from lime and quartz is 125 kJ/kg and the synthesis of xonolite is 50 kJ/kg, which raises the pressure and temperature in the autoclave. Recommendations are given below for controlling the composition of the hydrate and for reducing the consumption of steam during the autoclaving.

1 Introduction

It is well known that heat is evolved during the reactions when calcium silicate hydrates are formed from calcium hydroxide and finely ground quartz in an autoclave. The exact values for the heat evolution of this process are very difficult to determine so at first the problem was approached theoretically. The results of these theoretical calculations are given by Babuschkin et al. [1]. The reaction for the formation of tobermorite from calcium hydroxide and quartz at a temperature of 179 °C has a reaction enthalpy of ΔHP = 30–31 kcal/mol. However, an enthalpy of ΔHP = 20–25 kcal...

1 Introduction

It is well known that heat is evolved during the reactions when calcium silicate hydrates are formed from calcium hydroxide and finely ground quartz in an autoclave. The exact values for the heat evolution of this process are very difficult to determine so at first the problem was approached theoretically. The results of these theoretical calculations are given by Babuschkin et al. [1]. The reaction for the formation of tobermorite from calcium hydroxide and quartz at a temperature of 179 °C has a reaction enthalpy of ΔHP = 30–31 kcal/mol. However, an enthalpy of ΔHP = 20–25 kcal/mol was determined later by Babuschkin for this reaction. The results from the calculation for tobermorite and xonolite at a temperature of 180 °C are shown below.

The following values were assumed for the reaction enthalpy and also for the heat capacity of tobermorite and its intermediate phases:

Data [1] in:

kcal/Mol kJ/Mol kcal/Mol kJ/Mol
∆H0 298td = 2556 10 684 Cp = 10.6 + 189 ·T·10-3 462.3 + 0.79 · T
∆H0  SiO2 = 217.7 910 Cp = 11.7 + 8.2 ·T·10-3 52.4 +34.3·10-3  ·T
∆HC2(or)2 = 235.5 983.5 Cp = 19.0 + 10.8 ·T·10-3 79.4 +45.1·10-3 ·T

The molar standard entropy  in kcal/Mol (or kJ/Mol)

for tobermorite is 146  (610.3)
for quartz is 10.0  (41.8)
for Ca(OH)2 is –20  (83.6)

2 Calculations

The calculation of the enthalpy is carried out as described by Babuschkin et al. [1] for the synthesis reaction of tobermorite and xonolite at a temperature of 280 °C:
1. Calculation of the reaction enthalpy H298:
Ca(OH)2 + 1.25 SiO2 + 0.1 H2O = CaO · SiO2 · 1.1 H2O
∆H298= – 2556,3 + 235.3 + 1.2 · 217.7 + 0.1 · 68.3 = 
  5⇥–7.9 kcal/Mol · K
2. The change in standard enthalpy:
∆S0 298 = 146 – 20 – 1.2 ·10 – 0.1 ·16.7 = 4.47 kcal/Mol · K
5
3. The heat capacity of tobermorite at 180 °C is:
Cr = 110.6 + 189 ·453 ·10-3 = 196.2 kcal/mol ·K
4. Molar mass of tobermorite:
MTb = 146.8 Da
(Da – Dalton is used as the unit of measurement for the atomic and molar masses. Editor’s note: 1 Da = 1 g/mol)
5. Calculation of the changes in heat capacity during the reaction:
∆Cr = ∆a + ∆B ·T + ∆c ·T-2
= 67.15 + 158.6 ·10-3 ·T
= 71.9 kcal/mol · K
6. Calculation of the heat evolved at a reaction temperature of 180 °C:
∆HT = ∆H298+∫ 458                    298 ∆Cp · dT = 7.9 ·103 +
160 (67.15 + 158.6 ·103 · 453)
= 7.9 ·103 + 160 (67.15 + 71.84)
= 7.9 ·103 + 22.2 ·103
= 30.1 kcal/mol · K
= 125.8 kJ/mol

This means that the theoretical result for the heat evolution for tobermorite agrees with the values from Babuschkin [1].

The rise in temperature in the autoclave can now be determined, for which the specific heat capacity of tobermorite is calculated as follows:

Crsp = 196,2 = 1,33 kap · K
146,8    kr 
∆HTb = CP ·∆t ·m

In this case m = 1 kg, which gives a temperature rise of ∆t 30,1   1,33  = 22,6°. The heat capacity of tobermorite is slightly higher than that of the starting components so ∆t = 23 °C is used for the calculation.

The heat evolved during the synthesis of xonolite is calculated in a similar way:

6 Ca(OH)2 + 6 SiO2 = 6 CaO ·6 SiO2 ·H2O + 5 H2O
∆H0 ks = 2396.7 kcal/mol (10018.2 kJ/mol)
S0 ks = 121.3/6 = 20.25 cal/mol ·K (84.6 J/mol · K)
The other starting values have been given above.
∆H218 = -2396.7 – 5 ·68.3 + 6 ·235.3 + 6 ·217.8 =
⇥–13.6 kJ/mol
∆Hks= – 13,6     6   = –2.27 kJ/mol
∆Sr453 = 20.25 + 0.8 ·16.7 – 20 – 10 = 3.61 cal/mol · K
Crks = 132.25 + 65.2 – 18.35 ·10-3 = 197.5 cal/mol · K
∆a = 132.25 – 19 – 11.2 – 0.17 ·12.65 = 180 cal/mol · K
B = 65.2 – 10.8 – 8.2 – 11.4 = 34.8
∆Ht = ∆H298 +∫ 458                    298 ∆Cp · dT =
⇥–2.27 · 10-3 + 155 (100 + 34.8 ·453 ·10-3) = 2290 cal/mol
Mks = N«. Cp = 1.74 cal/mol ·K
∆Hsp = 2290        113  = 20.2 cal/ kg
∆t= 20,3         1,74 = 11.7 °C ≈ 12 °C

It is therefore apparent that the reaction enthalpy of xonolite during its synthesis from Ca(OH)2 and quartz is 1.5-times lower than during the formation of tobermorite.

Rahimbaev [2] shows that the change in enthalpy under isothermal conditions is accompanied by slight change in the evolution of heat in the bonding system. From this it emerges that the evolution of heat during the synthesis of 11.3 Å tobermorite, such as occurs in aerated concrete during hardening in the autoclave, contributes much more than that of xonolite.

The evolution of heat during the synthesis of tobermorite in aerated concrete causes a local temperature rise within the material by 22-23 °C.

3 Graphical representation

The changes in pressure and temperature in the autoclave are shown in diagrams 1 to 3 (Figs. 1-3) The curves were recorded in the construction materials plant in Egorjewsk  (the town of Egorjewsk in the Moscow region), where aerated concrete is produced on a production line (“Masa-Henke” line).

Analysis of the curves that characterize the process occurring in the autoclave shows the following:

During the autoclaving of the product with a density D 600 the steam pressure remains stable at 1.1 MPa after the operating point has been reached.

During the autoclaving of the aerated concrete products with densities of D 400 and 500 the steam pressure rises by 0.025-0.03 MPa after the operating point has been reached. This then triggers the automatic control system for the steam pressure in the autoclave and switches off the steam supply so that after a few minutes the pressure falls back to the set value of 1.1 MPa. The pressure in the autoclave then rises until the automatic control system is actuated again.

The number of on-off cycles of the automatic control system varies between 2 and 7 while the intervals between the cycles between 15 and 20 minutes may be as much as 150 minutes. An entire cycle lasts between 2 and 3.5 hours.

The number of on-off cycles falls during the course of time. Although the first two disconnections occur after 15-20 minutes the last two will occur 40-50 minutes after the previous one.

The frequency and amplitude of the switching on and off of the steam supply depend on the quantity of lime and the aluminium powder or aluminium paste. This shows indirectly how the rise in steam pressure in the autoclave is determined not only by the synthesis of the silicate hydrates but also by the aluminate hydrate phases. However, the contribution of the aluminate hydrate phases in the overall heat balance is apparently relatively small.

The investigations show that the transformation of the tobermorite into xonolite is accompanied by the absorption of heat and an increase in the entropy of the system. According to the Le Chatelier principle it follows that a rise in temperature in the autoclave has a double effect on the tobermorite ↔ xonolite transformation process.

A rising enthalpy displaces the reaction in the direction of xonolite while a rising pressure or entropy causes a displacement in the direction of tobermorite formation. The energy factor clearly exerts an dominant influence, so an intensification of the conditions in the autoclave favours the formation of xonolite in the CaO-SiO2-H2O system although it is transformed back into tobermorite again if the concrete is cooled under conditions of high humidity [3].

4 Conclusion

Concretes based on xonolite are more weather-resistant than those based on tobermorite [4, 5] but the production of aerated concretes based on xonolite gives rise to higher energy costs. There is also no guarantee of the stability of its phase composition under normal temperature conditions.

For aerated concrete production it is therefore recommended that immediately after removal from the autoclave the product should be dried to a residual moisture content of not more than 20 %, which also contributes to stabilization of the beneficial phase composition. Because of the above-mentioned results from the autoclaving of aerated concretes with densities D 400 and 500 the steam pressure should be reduced by 0.025-0.03 MPa for the first 3–4 hours after the correct operating point has been reached. The evolution of heat during the synthesis of silicon and aluminate hydrates also lowers the energy costs by a few percent.

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