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Measurements of moisture content for a series of concrete were conducted to analyse the impacts of water to cement (W/C) ratio and temperature on the moisture content–relative humidity (RH) curves (Jiang and Yuan, 2013). Based on the experimental results and the multi-layer molecules adsorption Brunauer-Emmett-Teller (BET) analysis, the authors proposed a three-parameter model to capture the relationship between moisture content, temperature and RH in concrete (Equation 7 in Jiang and Yuan, 2013)

where S is the pore water saturation, H is the RH in concrete, and λ1, λ2 and λ3 are the adjustable parameters. Through regression analysis, the authors obtained functions of λi = 1,2,3 to temperature and W/C ratio (Equations 7a–7c in Jiang and Yuan, 2013). Then the established model was verified by an independent water vapour sorption test. However, the physical meanings of Equation 8 have not been elucidated clearly. As a matter of fact, Equation 8 has an expression very similar to the Guggenheim-Andersen-Boer (GAB) model (Timmermann, 2003)

where Wm is the GAB monolayer capacity, C and K are respectively the energy constants related to the first monolayer's sorption energy and the further layers' sorption energy. As a matter of fact, the GAB model was developed from the BET model, and shares with it the two original BET constants (Wm and C). The only difference is that the GAB model introduces an extra term K based on the assumption that the sorption state of the sorbate molecules in the layers beyond the first is the same, but different to the pure liquid state (Timmermann, 2003; Pradas et al., 2004), see Figure 9 for mechanism illustration.

Comparing Equations 8 and 9, one can find that

Note that both the first monolayer sorption energy term C and the further layers' sorption energy term K are associated with temperature (Pradas et al., 2004)

where C0 and K0 are the pre-exponential coefficients, μ1 and μ2 are the energy (or chemical potential) of the adsorbate in the first adsorption layer and that of the pure sorbate in the saturated state respectively, μ0 is the energy in a reference state, R is the ideal gas constant and T is the Kelvin temperature. In fact, μ2μ1 denotes the adsorption energy. Combining Equations 10 and 11, one obtains

From Equations 12b and 12c, one can also have

Fitting the values of λ1, λ2(= K) and λ3 obtained by Jiang and Yuan through Equations 12 and 13, one can obtain the quantities of the energy terms μ0μ1, μ0μ2 and μ2μ1. Figures 10, 11 and 12 show the variation of λ1, λ2(= K) and C with temperature and the fitting curves for all the used three series of concrete. Results of water vapour sorption on quartz in Timmermann (2003) showed that both the K and C have much higher values than those in Jiang and Yuan (2013). Obviously, it can be found that all the fitting curves can capture the data in Jiang and Yuan (2013). Clearly, the parameter λ1 and the first monolayer sorption energy term C decrease and the parameter λ3 increases with increasing temperature, indicating that μ0μ1 > 0, μ2μ1 > 0 and μ0μ2 < 0, or μ2 > μ0 > μ1. The values of μ2μ1, μ0μ1 and μ0μ2 for concrete with different W/C ratios are displayed in Figure 13. Note that the values of μ2μ1 (19–22 kJ/mol) extracted directly from Equation 13 are much lower than those of [(μ0μ1)–(μ0μ2)] (27–33kJ/mol) from Equations 12a and 12b, which is probably due to the suspected non-equilibrium data in Jiang and Yuan (2013). The values of the sorption energy (μ2μ1) increase as the W/C ratio increases, probably because more porous CSH gels form for concrete with higher W/C ratio. However, the values of all the sorption energy terms for porous concrete are significantly lower than those for water vapour adsorption on other porous materials, such as silicate glass (Leed and Pantano, 2003), activated carbons (Muller et al., 1996), disordered mesoporous silica (Puibasset and Pellenq, 2005) and high-silica zeolites (Bolis et al., 2006). More importantly, the obtained values are even lower than the latent heat of liquefaction of water in the bulk phase (44 kJ/mol), implying that the adsorption would not occur spontaneously. This result could be misleading. Again, the tests by Jiang and Yuan conducted under the non-equilibrium condition may be a crucial reason to underestimate the adsorption energy. It is thus expected that, with the water vapour sorption test at sufficient equilibrium condition, the adsorption energy of water vapour in cement-based material can be evaluated appropriately.

This paper (Jiang and Yuan, 2013) aims to predict the moisture content of concrete under a natural climate environment, not to study the equilibrium moisture content of concrete under ambient relative humidity. The moisture content of concrete is in fluctuation owing to the effects of climatic factors in the natural environment, which is not an equilibrium condition. Therefore, the temperature and relative humidity presented in this paper are those in the concrete's micro-environment, not those in the climatic environment.

Bolis
V
,
Busco
C
,
Ugliengo
P
.
Thermodynamic study of water adsorption in high-silica zeolites
.
Journal of Physical Chemistry B
,
2006
,
110
, (
30
):
14849
14859
.
Jiang
JH
,
Yuan
YS
.
Relationship of moisture content with temperature and relative humidity in concrete
.
Magazine of Concrete Research
,
2013
,
65
, (
11
):
685
692
.
Leed
EA
,
Pantano
CG
.
Computer modeling of water adsorption on silica and silicate glass fracture surfaces
.
Journal of Non-Crystalline Solids
,
2003
,
325
, (
1–3
):
48
60
.
Muller
EA
,
Rull
LF
,
Vega
LF
,
Gubbins
KE
.
Adsorption of water on activated carbons: A molecular simulation study
.
Journal of Physical Chemistry
,
1996
,
100
, (
4
):
1189
1196
.
Pradas
MM
,
Sanchez
MS
,
Ferrer
GG
,
Ribelles
JMG
.
Thermodynamics and statistical mechanics of multi-layer adsorption
.
Journal of Chemical Physics
,
2004
,
121
, (
17
):
8524
8531
.
Puibasset
J
,
Pellenq
RJM
.
Water adsorption in disordered mesoporous silica ‘‘Vycor'' at 300 K and 650 K: A Grand Canonical Monte Carlo simulation study of hysteresis
.
Journal of Chemical Physics
,
2005
,
122
, (
9
):
094704,
,
094704-1-10
.
Timmermann
EO
.
Multilayer sorption parameters: BET or GAB values
.
Colloids and Surfaces A
,
2003
,
220
, (
1
):
235
260
.

Data & Figures

Figure 9.

Schematic illustration of (a) the BET and (b) the GAB multilayer sorption mechanisms

Figure 9.

Schematic illustration of (a) the BET and (b) the GAB multilayer sorption mechanisms

Close modal
Figure 10.

Variation of λ1 with temperature for concrete samples with different initial W/C ratios. Points represent data from Jiang and Yuan (2013) and lines are fitting curves by Equation 12a

Figure 10.

Variation of λ1 with temperature for concrete samples with different initial W/C ratios. Points represent data from Jiang and Yuan (2013) and lines are fitting curves by Equation 12a

Close modal
Figure 11.

Variation of λ2 with temperature for concrete samples with different initial W/C ratios. Points represent data from Jiang and Yuan (2013) and lines are fitting curves by Equation 12b

Figure 11.

Variation of λ2 with temperature for concrete samples with different initial W/C ratios. Points represent data from Jiang and Yuan (2013) and lines are fitting curves by Equation 12b

Close modal
Figure 12.

Variation of the monolayer sorption energy constant C with temperature for concrete samples with different initial W/C ratios. Points represent data from Jiang and Yuan (2013) and lines are fitting curves by Equation 13

Figure 12.

Variation of the monolayer sorption energy constant C with temperature for concrete samples with different initial W/C ratios. Points represent data from Jiang and Yuan (2013) and lines are fitting curves by Equation 13

Close modal
Figure 13.

Sorption energy in terms of W/C ratio: (μ2μ1) extracted from Equation 13, (μ0μ1) and (μ0μ2) from Equations 12a and 12b respectively

Figure 13.

Sorption energy in terms of W/C ratio: (μ2μ1) extracted from Equation 13, (μ0μ1) and (μ0μ2) from Equations 12a and 12b respectively

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