2. Materials and Methods
Sulphate resisting portland cement type CEM I 42.5N CC (
SC) produced by the Tam Diep plant, which is the leading cement manufacturer in Vietnam using the most modern world technologies. The main characteristics of clinker and Portland cement based on it met the requirements of ASTM C150-07 [
11], GOST 22266-2013 [
12] (State standard of Russia) and TCVN 6067:2018 [
13] (State standard of Vietnam).
The physical and mechanical properties, as well as the chemical and mineral compositions of the used cement are shown in
Table 1,
Table 2 and
Table 3.
Active mineral admixtures allow to reduce the consumption of cement, as well as to compact the structure of concrete by reducing the porosity of the cement stone and thereby improving its operational properties, and in addition, to avoid stratification of the concrete mixture when using water-reducing superplasticizers [
14,
15,
16]. Local active mineral ingredients used in the work included fly ash class F from Vung Ang (
FA) conforms to the standard TCVN 10302:2014 [
17] and GOST 25818-2017 [
18], Vina Pacific SF-90 Silica fume (
SF) and rice husk ash (
RHA) conforms to the standard TCVN 8827:2011 [
19]. Their composition and properties are shown in
Table 4 and
Table 5.
Granulometric composition of
FA,
SF and
RHA, shown in
Figure 1, was determined using the method of laser granulometry.
Silica sand (
SS) of the Lo River (Vietnam) was used as a fine aggregate. It is a popular construction sand in Vietnam with good quality and low price. The grain size composition of sand is important for the preparation of concrete mixtures of the required consistency, since it has a significant effect on their workability and the amount of mixing water required for this. The regulatory requirements for the physical and mechanical properties of sand are set out in the Russia and Vietnam standards GOST 8736-2014 [
20] and TCVN 7570:2006 [
21]. The results of their determination are presented in
Table 6.
As a coarse aggregate, we used crushed stone (
CS) with D
max = 10 mm, which is mined in open pits in Ninh Binh (Vietnam) and whose properties corresponded to the requirements of the standards GOST 8267-93 [
22] and TCVN 7570:2006 [
21]. The physical and mechanical properties of the used crushed stone are shown in
Table 7.
A special requirement is imposed on the cleanliness of the aggregate, since dusty, silty and clay particles envelop the surface of the grains and impair their adhesion to the cement stone. Therefore, the content of such particles in a coarse aggregate should not exceed 3%.
The superplasticizer SR 5000P (
SP) from SilkRoad (Vietnam) with a density of 1.1 g/m
3 at a temperature of 20 ± 5 °C was used as a plasticizing additive in concrete mixtures, which reduces the water demand of equally mobile concrete mixtures by 30–40% that meets the requirements of GOST 24211-2008 [
23] and ASTM C494/C494M-19 [
24]. The main characteristics are shown in
Table 8.
According to the passport data provided by the manufacturer, the optimal dosage of the superplasticizer SR5000P for obtaining a concrete mixture with the highest mobility is in the range of 0.9 ÷ 1.2% of the mass of the adhesives. If the SP consumption exceeds this amount, then this can lead to water separation and stratification of the concrete mixture. Therefore, the work used the average value of the recommended dosage of the superplasticizer in the amount of 1% by weight of the adhesives.
Water (
W) used for the preparation of concrete mixtures complied with the requirements of GOST 23732-2011 [
25] and TCVN 4506:2012 [
26]. Such water should not contain impurities that affect the setting of concrete, as well as reduce the durability of structures, above the permissible limit, have a pH value of at least 4 and contain no more than 5.6 g/L of mineral salts, including no more than 2.7 g/L sulfates. In addition, the water should be free of sludge and oil flakes, as well as organic matter of more than 15 mg/L.
Building theoretical models
Sea water is a highly corrosive environment containing a large amount of dissolved salts and causing chemical corrosion of both concrete itself and steel reinforcement in reinforced concrete structures. The aggressive marine environment has a significant impact on the durability of concrete and reinforced concrete structures of hydraulic structures of the coastal zone. At the same time, in reinforced concrete, the penetration of liquid aggressive media through capillary pores causes cracking and peeling of the protective concrete layer above the surface of the reinforcing bars, which leads to corrosion of the reinforcement [
27,
28,
29,
30].
To experimentally determine the chemical composition of seawater at different depths in the coastal zone, in the area of Halong port in the north of Vietnam, samples were taken (
Figure 2), the results of chemical analysis of which are presented in
Table 9.
Table 9 shows that the content of solutes in seawater tends to increase in the bottom layer, especially the content of
Ca2+ ions. This is due to the fact that Halong Bay rests on a limestone base, as a result of which the seawater of the bottom layer, dissolving calcium-containing rocks, has a higher concentration of
Ca2+ ions.
For the most part, all offshore hydraulic structures are made of concrete or reinforced concrete, complex composite materials, the viability, performance, and durability of which to a decisive extent depend on the structure of structures, their physicochemical, structural, mechanical, and operational properties. An important influence is exerted by the salinity of sea water, the presence of salts of inorganic substances in it and the presence of biological microorganisms in different climatic seasons. From the point of view of the theories of physicochemical hydrodynamics and heat and mass transfer, the nature of the interaction of the composite of a hydraulic structure with the components of seawater is determined by the laws of chemical kinetics and diffusion in the bulk of concrete and at the solid-liquid interface, as well as by the laws of mass transfer (in this case, the transfer substances from the interface into the volume of the sea water basin).
To develop effective methods for protecting concrete from leaching by a marine environment containing a range of different ingredients that have a significant effect on the rate of decomposition of highly basic compounds and the removal of decomposition products into the marine environment, it is necessary to develop mathematical models of unsteady mass conductivity (diffusion in a solid) under non-uniform arbitrary initial conditions and combined boundary conditions of the 2nd and 3rd kind. Particular attention should be paid to taking into account the nonlinearity of the coefficients of mass conductivity and mass transfer.
In accordance with the classification of Professor V.M. Moskvin [
31], the simplest form of development of corrosion processes in concrete is leaching. In this case, the aggressive component does not penetrate deep into the material of the concrete (reinforced concrete) structure. The rate of the process is determined by the diffusion of calcium hydroxide from the pores of the inner layers of the structure to the external solid-liquid interface, and then by mass transfer from the interface to the liquid mass.
In this case, it is assumed that the target component, which is free calcium hydroxide in the processes of corrosion of cement concrete, is removed from the surface of a concrete or reinforced concrete structure by a liquid medium as a result of convective mass transfer. If the medium is stationary, then the mass transfer will be characterized by natural convection, and if the surface of the structure is washed with a liquid at a certain speed of its movement, then there is a forced flow of the liquid. In both cases, the mass transfer of the target component will be determined by two processes: mass conductivity from the inner layers to the interface and mass transfer from the interface to the liquid phase [
32,
33,
34,
35,
36,
37,
38,
39].
The model of the problem of mass transfer with initial and boundary conditions for an unbounded plate concrete (reinforced concrete) can be schematically illustrated in
Figure 3.
The problem of mass transfer of calcium hydroxide from a concrete structure into an aqueous substance can be formulated by the following system of Equations (1)–(4):
where:
C0 is the initial concentration of free calcium hydroxide in concrete, in terms of calcium oxide, kg CaO/kg concrete;
C(x,τ) is the concentration of free calcium hydroxide in concrete at the moment
τ at any point with the coordinate
x, in terms of calcium oxide, kg CaO/kg concrete;
k is coefficient of mass conductivity in the solid phase (diffusion), m
2/s;
β is mass transfer coefficient in a liquid medium, m/s;
Cp is the equilibrium concentration of the transferred component on the surface of a solid; kg CaO/kg concrete;
δ is wall thickness of the structure, m.
The Equation (1) is the differential equation of non-stationary mass transfer in the body of a reinforced concrete structure. The Equation (2) defines the initial condition of the process: the distribution of calcium hydroxide concentrations at the time instant taken as the initial one. The Equations (3) and (4) expressions define the conditions at the interface. The Equation (3), called the condition of the 2nd kind, also called the “non-penetration condition”, determines the fact that calcium hydroxide does not diffuse into the internal premises of the hydraulic structure located on the left from enclosing concrete (reinforced concrete) construction. The Equation (4) characterizes the interaction of the surface layer of the structure with a liquid medium. This is a condition of the 3rd kind, also called “Newton’s condition”.
The use of dimensionless variables allows you to go to the following Equation (5):
where:
is the dimensionless concentration of the transferred component across the concrete thickness;
is dimensionless coordinate;
is Fourier mass transfer criterion;
is Bio mass transfer criterion.
In this case, the system of Equations (1)–(4), also called the “boundary value problem of non-stationary mass transfer”, is transformed to the from:
The purpose of solving this boundary value problem is to find a function
that allows one to calculate the concentration profiles of the transferred component over the thickness of the structure, which also change over time. This is the so-called “direct problem of the dynamics of the mass transfer process” [
40]. The solution to the abovementioned problems is indicated in the [
32,
41].
where
is the roots of the characteristic Equation (11):
Some results of calculations by Equation (10) are shown in
Figure 4.