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. Author manuscript; available in PMC: 2019 Apr 1.
Published in final edited form as: J Am Ceram Soc. 2017 Nov 4;101(4):1453–1470. doi: 10.1111/jace.15323

Table 3.

Stoichiometry and assumed thermodynamic and kinetic parameters for simulated reactions. Except where noted, the collection of reactions and the parameter values are taken from Reference [36] and references therein. The reactions and solubilities for C–S–H are based on a newer solid solution model in Reference [47], and the kinetic parameter values were chosen to give approximately the same rates of nucleation and growth as simulated in Reference [36].

Reaction k+/μmol mn s−1(a) ln K
I0B/mns1
(a)
q/K3
Ca3SiO5+4H2O3Ca2++H3SiO4+5OH
112.5(b) −39.0(b)
C2S3H122Ca2++3H3SiO4+OH+7H2O
1.5 × 10−7 −37.43 1.1 × 1027(b) 2.0 × 109(b)
C5S3H125Ca2++3H3SiO4+7OH+4H2O
1.5 × 10−7 −80.43 7.3 × 1026(c) 1.7 × 1010(c)
Ca(OH)2Ca2++2OH
7.2 −11.97 7.35 × 1026(d) 2.5 × 109(d)
CaOH+Ca2++OH
6 × 105 −2.81
H3SiO4+OHH2SiO42+H2O
1.5 107 1.91
(a)

n = 2 or 3 for heterogeneous or homogeneous processes, respectively.

(b)

Based on linear regression of measurements in Ref. [28].

(c),(d)

Heterogeneous nucleation on Ca3SiO5 and C−S−H, respectively.