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Research Article

An inverse problem to simulate the transport of chloride in concrete by time–space fractional diffusion model

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Pages 2429-2445 | Received 21 Aug 2020, Accepted 28 Mar 2021, Published online: 19 Apr 2021

Abstract

In this paper, we proposed a fractional diffusion model to simulate the movement of chloride in concrete. In such complex porous structure some of the free chlorides, which are affected by the surrounding heterogeneous physical environment, will be bounded physically and chemically. Furthermore, experiments reveal that the interesting heavy-tailed phenomena appear in diffusion process. The time and spatial fractional derivatives are introduced to explain the anomalous diffusion and the dependence of medium properties. The numerical research shows that present model could better fit the experimental data and the diffusion of chloride in concrete is time-dependent and space-dependent.

2010 Mathematics Subject Classifications:

1. Introduction

The chloride penetration, which will bring about the steel corrosion in the concrete, is one of the crucial factors to destroy the persistence of concrete structures and bring about the attenuation of concrete service life [Citation1–3]. In practical situation, the individual components used in concrete mixture, heterogeneous pore structure, combination and absorption of chloride ions, electrochemical reaction and many other factors will affect the transport of chloride in the concrete, and then Fick law may be not suitable to describe its movement. Furthermore, experiments also have confirmed that in saturated porous medium the random movement of the fluid particle will no longer satisfy Gaussian distribution [Citation4,Citation5]. Therefore, it is necessary for us to turn to new theories to detect the diffusion and reaction behaviours of chloride in concrete.

During the process of transport, besides the free chloride (Cf), the total chlorides (CT) in concrete still include two parts: physically-bound chloride (Sp) and chemically-bound chloride (Sc) [Citation6,Citation7]. The introduction of bound chlorides into transport model can help us forecast the chloride entering more accurately. Early studies have shown that binding reactions occur in the diffusion process of free chloride ions [Citation8–11], but the components of binding chloride have not been discussed clearly. Later, some experiments have revealed that C-S-H gels could adsorb some of free chloride ions, which would cause physical reaction, and the irreversible chemical combination also happened with other ions and substances [Citation12–15].

In fact, concrete is a kind of heterogeneous and anisotropic complex porous medium, and according to pore diameter, its pores can be divided into three types: capillary pores, gel pores and stomata, where occurs reaction, diffusion, capillary suction and permeability [Citation16]. Due to the anisotropy, heterogeneous and complexity of the medium property, many works have shown that the propagation of gas and liquid in concrete does not follow Fick law and Gaussian distribution [Citation17–20]. Fractional derivative has been used to describe anomalous transport of many materials in porous media and complex environment, such as oil, biology, rock, hydrodynamics, rheology, viscoelasticity, electrical conduction of biological system, and so on [Citation21–30]. A diffusion model with time fractional derivative has been constructed to simulate the transport of sodium chloride in a single crack and free chloride ions in concrete [Citation31,Citation32]. Furthermore, some semi-analytical and numerical methods have been used to solve this kind of diffusion equation [Citation33,Citation34]. The error and stability of the numerical method are also studied [Citation34–38]. However, the chemical reaction and spatial characteristics of free chloride ions in pores have not been considered.

Motivated by above works, the fractional time–space diffusion model is proposed to simulate the transport of chloride in concrete. This paper is organized as follow: firstly we give the description of the establishment of fractional diffusion model. According to the discretization scheme in Section 3, the optimization algorithm based on modified hybrid Nelder–Mead simplex search and particle swarm optimization method (MH-NMSS- PSO) [Citation39–42] is used to search for the unknown fractional derivative parameters to fit the experimental data in Section 4. Finally, the sensitivity analysis of different physical parameters in this problem is discussed.

2. Model description

As shown in Figure , concrete is a complex heterogeneous porous material. Once the free chloride ions solution diffuse into it, chemical reaction will arise between some of them and cement pastes until the concentration of chemically-bound chlorides reach threshold at one position. The remaining free chlorides will move forth and some of them will adhere to the hole surface physically. The other free chloride ions will move forward again and maybe meet some holes unconnected each other, which induces the delay of the diffusion and results in the heavy-tailed phenomena [Citation22]. Then the modified Fick law is introduced to describe the influence of time and space [Citation7]: (1) 0t0xJ(x,τ)dxdτ=0t0xk(x,x;t,τ)Cf(x,τ)dxdτ,(1) where Cf is the concentration of free chlorides and J is the flux. Here we assume that k(x,x;t,τ)=kx(x,x)kt(t,τ).

Suppose the diffusion kernel function of space and time is negative power law function: (2) kx(x,x)=DeεΓ(2β)(xx)β1,kt(t,τ)=1Γ(α)(tτ)1α,(2) where De is the effective diffusion coefficient, ε is porosity.

Deriving x and t on both sides at the same time and according to the fractional derivative definition of Riemann–Liouville and Caputo [Citation43–45], Equation (Equation1) can be simplified as: (3) J(x,t)=Deε1αt1αβ1xβ1Cf(x,t),0<α1,1<β2.(3) The mass diffusion equation of chloride in concrete is [Citation46]: (4) CTt=J,(4) where CT is the content of chloride ions. According to Refs. [Citation14,Citation47], the total ions are divided as three parts: (5) CT=Cf+Sp+Sc.(5) In general, Sc is a constant. The relationship between free chloride ions and physically-bound chloride satisfies the following linear binding isotherm [Citation48]: Sp=pCf, where p also is a constant.

Therefore, in order to balance the dimension, λ1 and λ2 are introduced to the mass diffusion equation, and then mass diffusion equation with fractional derivative can be written as: (6) λ1ααCf(x,t)tα=λ2βDeε(1+p)βCf(x,t)xβ,(6) where λ1 and λ2 are constants with dimensions s11/α and mm12/β, respectively.

It is assumed that there is no free chloride ions inside concrete at the beginning and the concentration of free chloride ion exposed to the external environment is Cs. Free chloride ions can migrate in the concrete continuously. In addition, the concentration and change of free chloride in deep position of concrete are very small. The initial and boundary conditions are (7) x0:Cf(x,t)|t=0=0,(7) (8) t>0:Cf(x,t)|x=0=Cs,Cf(x,t)|x=+=0.(8)

3. Numerical method

3.1. Difference scheme

To solve this problem, the diffusion equation is discretized. Let xi=ih,tj=jτ(i=0,1,2,,M,j=0,1,2,,N), where (xi,tj)[0,X)×[0,120] and X represents infinity, and τ=120N, h=XM are the time and space steps, respectively.

Theorem 1

When the time fractional order is α(0<α<1), the time Caputo fractional derivative can be discretized into the difference scheme by L1 interpolation, as shown below [Citation49]: (9) αf(tk)tα=ταΓ(2α)n=0k1an(α)[f(tkn)f(tkn1)]+O(τ2α)=ταΓ(2α)[a0(α)f(tk)n=1k1(akn1(α)akn(α))f(tn)ak1(α)f(t0)]+O(τ2α),(9) where the coefficient is expressed by a0(α)=1,an(α)=(n+1)1αn1α,n=1,2,,N.

Theorem 2

When the order of the spatial fractional order is β(1<β<2), the space Riemann–Liouville fractional derivative can be discretized by Grunwald–Letnikov algorithm as following [Citation50]: (10) βxβC(xi,tk+1)=1hβj=0i+1ωjβC(xi+1j,tk+1)+O(hs),(10) In this formula, there are different forms of ωjβ for different weight coefficient s. We select s as 1, and ωjβ=(1)jβ(β1)(βj+1)j!,(j=0,1,).

According to Equations (Equation9) and (Equation10), the following discretization format can be obtained: (11) αCfijτα=ταΓ(2α)[a0(α)Cfijn=1j1(ajn1(α)ajn(α))Cfinaj1(α)Cfi0],(11) (12) βCfijηβ=1hβk=0i+1ωkβCfi+1kj.(12) Then the discretization scheme about mass diffusion equation with fractional derivative and initial boundary conditions can be written as: (13) λ1αr1[a0(α)Cfijn=1j1(ajn1(α)ajn(α))Cfinaj1(α)Cfi0]=λ2βDer2ε(1+p)k=0i+1ωkβCfi+1kj,(13) (14) Cfi0=0,Cf0j=Cs,CfMj=0,(14) where r1=ταΓ(2α),r2=1hβ.

3.2. Existence and uniqueness of solutions

Lemma 1

The coefficients aj(α), ωjβ(j=0,1,2,) satisfy [Citation45]:

  1. a0(α)=1,aj(α)>0,j=1,2,,

  2. aj(α)>aj+1(α),j=0,1,,

  3. ω0β=1,ω1β=β<0,ωjβ>0,j=2,3,,

  4. j=0ωjβ=0, and for i=1,2,, we have j=0iωjβ<0.

Theorem 3

If the coefficient ωjβ satisfies:

(1)

ω1β=β<0, and ωjβ>0 when j1,

(2)

j=0i+1ωjβ0, then the solution of difference scheme (Equation13) and (Equation14) exists and is unique.

Proof.

Difference scheme (Equation13) can be rewritten as: (15) Cfijrk=0i+1ωkβCfi+1kj=aj1(α)Cfi0+n=1j1(ajn1(α)ajn(α))Cfin,×1iM1,1jN,(15) where r=λ2βDer2λ1αr1ε(1+p).

For i = 0, the coefficient matrix A of Equations (Equation14) and (Equation15) obeys l=1M|A0l|=0<1=|A00|.

For i = M, l=0M1|AMl|=0<1=|AMM|.

For i0 and iM, according to conditions (1)–(2) and Lemma 1, we have rω1β=rβ>rk=0,k1i+1ωkβ>0, that is, |1rω1β|=1rω1β>rk=0,k1i+1ωkβ.

So coefficient matrix A is strictly diagonally dominant matrices. Matrix A is invertible, so the solution of the difference scheme (Equation13) and (Equation14) exists and is unique.

3.3. Stability of the difference method

Next, we discuss the stability of the difference method.

Theorem 4

Assume Cfij is the numerical solution of Equations (Equation13) and (Equation14), then (16) ||Cfj||||Cf0||,j=1,2,.(16)

Proof.

For j = 1, assume ||Cf1||=|Cfi01|=max0iM|Cfi1|. By Lemma 1, we have k=0i0+1ωkβ<0. Hence, ||Cf1||=|Cfi01||(1rk=0i0+1ωkβ)Cfi01||Cfi01rk=0i0+1ωkβCfi0+1k1|=|a0(α)Cfi00|=|Cfi00|||Cf0||For j = 2, assume ||Cf2||=|Cfi02|=max0iM|Cfi2|. By Lemma 1, we have k=0i0+1ωkβ<0. Hence, ||Cf2||=|Cfi02||(1rk=0i0+1ωkβ)Cfi02||Cfi02rk=0i0+1ωkβCfi0+1k2|=|a1(α)Cfi00+(a0(α)a1(α))Cfi01|a1(α)|Cfi00|+(a0(α)a1(α))|Cfi01|a1(α)||Cf0||+(a0(α)a1(α))||Cf1||a1(α)||Cf0||+(a0(α)a1(α))||Cf0||||Cf0||For j>2, we prove similar to the above steps.

Suppose that ||Cfj||=|Cfi0j|=max0iM|Cfij|, then ||Cfj||=|Cfi0j||(1rk=0i0+1ωkβ)Cfi0j||Cfi0jrk=0i0+1ωkβCfi0+1kj|=|aj1(α)Cfi00+n=1j1(ajn1(α)ajn(α))Cfi0n|aj1(α)|Cfi00|+n=1j1(ajn1(α)ajn(α))|Cfi0n|aj1(α)||Cf0||+n=1j1(ajn1(α)ajn(α))max1kj1||Cfk||aj1(α)||Cf0||+n=1j1(ajn1(α)ajn(α))||Cf0||=||Cf0||Hence, Theorem 4 is proved.

Let Cf~ij(i=0,1,,M;j=0,1,,N) be the approximate solution of Equation (Equation15), the error eij=Cf~ijCfij(i=0,1,,M;j=0,1,,N) satisfies (17) eijrk=0i+1ωkβei+1kj=aj1(α)ei0+n=1j1(ajn1(α)ajn(α))ein.(17) Apply Theorem 4, we obtain (18) ||Ej||||E0||,j=1,2,,N,(18) where ||Ej||=max0iM|eij|. The following conclusion is obtained.

Theorem 5

The fractional implicit difference method of Equation (Equation13) is unconditionally stable.

3.4. Convergence of difference method

The convergence of the difference scheme is discussed as follows.

Let Cf(xi,tj)(i=1,2,,M1;j=1,2,,N) be the exact solution of Equation (Equation6) at point (xi,tj). Then, (19) Cf(xi,tj)rk=0i+1ωkβCf(xi+1k,tj)=aj1(α)Cf(xi,t0)+n=1j1(ajn1(α)ajn(α))Cf(xi,tn)+Rij,(19) The error between the exact solution and the numerical solution is defined as ρij=Cf(xi,tj)Cfij(i=1,2,,M1;j=1,2,,N), Rj=(R1j,R2j,,RM1j)T, and subtract Equations (Equation15) from (Equation19), we obtain (20) ρijrk=0i+1ωkβρi+1kj=aj1(α)ρi0+n=1j1(ajn1(α)ajn(α))ρin+Rij,×1iM1,1jN,(20) with initial and boundary conditions (21) ρi0=0,i=0,1,,M,(21) (22) ρ0j=ρMj=0,j=0,1,,N,(22) where truncation error Rij satisfies |Rij|Cτα(τ2α+h), and C is a positive constant.

Proposition 1

||Yj||C¯τα(τ2α+h), where Yj=(ρ1j,ρ2jρM1j), ||Yj||=max1iM1|ρij| and C¯ is a constant.

Proof.

Similar to the proof of stability. For j = 1, assume ||Y1||=|ρi01|=max0iM|ρi1|. Hence, ||Y1||=|ρi01||(1rk=0i0+1ωkβ)ρi01||ρi01rk=0i0+1ωkβρi0+1k1|=|a0(α)ρi00+Ri0j|=|ρi00+Ri01|C1τα(τ2α+h).Thus, ||Y1||C1(a0(α))1τα(τ2α+h).

For j>1, using (aj(α))1(ak(α))1(k=0,1,,j), we prove similar to the above steps. ||Yj||=|ρi0j||(1rk=0i0+1ωkβ)ρi0j||ρi0jrk=0i0+1ωkβρi0+1kj|=|aj1(α)ρi00+n=1j1(ajn1(α)ajn(α))ρi0n+Ri0j|n=1j1(ajn1(α)ajn(α))|ρi0n|+C1τα(τ2α+h)[aj1(α)+n=1j1(ajn1(α)ajn(α))](aj1(α))1C1τα(τ2α+h)=C1(aj1(α))1τα(τ2α+h).Because limj(aj(α))1jα=limjjα(j+1)1αj1α=limjj1(1+1j)1α1=limjj1(1α)j1=11α, there exists a constant C2 for which ||Yj||C2jατα(τ2α+h).

Furthermore, jτ is finite, the following theorem is proved.

Theorem 6

Let Cfij be the numerical solution of Equation (Equation13), and Cf(xi,tj) is the exact solution of Equation (Equation6) at point (xi,tj). Then exists a constant C3 for which (23) |CfijCf(xi,tj)|C3(τ2α+h),1iM1,1jN.(23)

4. Parameters estimation

Here MH-NMSS-PSO- is used to estimate the unknown parameters α, β, λ1, λ2 to satisfy the experimental data. This method, which is proposed by Fan [Citation51] and extended by Liu [Citation50,Citation52,Citation53], is a combination of NMSS and PSO, and can find the global optimum with faster convergence speed. Furthermore, it does not need the derivatives of the function under exploration [Citation51]. Let (α,β,λ1,λ2)=(p1,p2,p3,p4)R4, where (α,β,λ1,λ2)[0,1]×[1,2]×(0,1]×(0,1].

Here we assume that the numerical solutions for Equations (Equation13) and (Equation14) at the point of P=(p1,p2,p3,p4) could have best agreement with the experimental data [Citation54]. The better point can be evaluated until the stop condition is satisfied [Citation55]: (24) g(P)=gmin=minPR4g(P)=minPR4j=0N(Cf(tj)Cfj)2N+1(24) where Cf(tj) is the experimental data in the time of tj, Cfj is the numerical solution at time tj, and N is the number of experimental data. Therefore, the parameters of four variables can be estimated by MH-NMSS-PSO, which is summarized in Algorithm 1.

In MH-NMSS-PSO- algorithm, 3m particles is initialized: Pi=(p1,i,p2,i,,pm,i),i=1,2,,3m, where pj,i is the value of parameter pj(j=1,2,m) and is expressed with a random number Rand(0,1) as: (25) pj,i=pj(min)+Rand×(pj(max)pj(min)),i=1,2,,3m+1;j=1,2,,m.(25) The initial velocity of 2m particles in PSO is defined as: (26) Vj,i=(Vj(max)Vj(min))/Lj,i=m+2,,3m+1;j=1,2,,m(26) where Lj is an integer, m is the number of unknown variables.

And velocities and positions of particles in PSO algorithm is updated by: (27) Vj,inew=w×Vj,iold+C1×Rand1×(Pbj,iPj,iold)+C2×Rand2×(PgjPj,iold)Pj,inew=Pj,iold+Vj,inew,j=1,2,,m;i=m+2,,3m+1(27) where w,C1 and C2 are coefficients given by Fan et al. [Citation51].

In addition, stop condition is added as the number of iteration has not reach the maximum number of iterations: (28) S=[i=1m+1(g¯gi)2m+1]1/2<ε¯(28) where gi=g(Pi)=gi=gi(p1,i,p2,i,,pm,i),g¯=i=1m+1gim+1 and ε¯ is a settled minimum value.

Figure 1. Schematic diagram of chlorides diffusion in concrete. 

Figure 1. Schematic diagram of chlorides diffusion in concrete. 

5. Results and sensitivity analysis of parameters

Based on above discretization scheme and optimization algorithm, the correctness of fractional diffusion model is proved by experimental data from ordinary Portland cement (OPC) concrete, fly ash (FA) concrete and ground blast furnace (Slag) concrete [Citation14,Citation54], which is shown in Figure  and Table . Since concrete interior is full of aggregates and pores with different sizes, it is possible for the aggregates to block the pores. All of these make the diffusion to be spatial dependence. Furthermore, the values of parameters estimated in Table  also reveal that the surrounding environment has important influence on the transport of chloride in the concrete. In addition, the simulation result for the FA35-40 show that the diffusion is time-dependence. When maximum number of iterations is set to 500, the CPU time and the convergence rate for searching the global optimal parameters on a personal laptop with Intel(R) Core(TM) i5-5200U CPU is showed in Table .

Figure 2. The experimental data compared with present model.  

Figure 2. The experimental data compared with present model.  

Table 1. The estimated parameters according to related parameters from Ref. [Citation54].

Table 2. Convergence rate and CPU time of OPC-30 for the process of searching optimal parameters.

The influence of parameters on chloride diffusion in the OPC concrete with OPC 30 is shown in Figures . Figure (a) and (b) illustrates the distribution of chloride content in concrete at different depths and time. Once the diffusion begins, the concentration of chemically bound chloride reaches the saturation value immediately. With time going on, the chloride concentration will grow up and the diffusion will continue to move towards the depth of concrete. What's more, with the accumulation of physically-bound chloride, the total chloride concentration at the same depth also increases with the increasing time. In terms of diffusion rate, compared with the content at initial position, the total content of chloride will decrease because the free chloride ions will decrease with the increasing depth.

Figure 3. Influence of  t and depth on the chloride diffusion.

Figure 3. Influence of  t and depth on the chloride diffusion.

Figure (a) and (b) illustrates the effect of p on chloride diffusion. Figure (a) gives the total chloride ions distribution as time is 120 s. Since at the entrance the content of free chloride ions is a constant, the increasing p mean that much more chloride ions are absorbed on the pores at the initial position and during transport process. This leads to the dramatic change of the CT at the initial stage. Figure (b) depicts the distribution of chloride content at depths of 10 mm and 15 mm, respectively. On the whole, with the increasing time, the total chloride ions will be higher since the chloride ions are absorbed on the pores firstly near the entrance. Furthermore, the higher adsorption capacity means that chloride ions will be more easy to accumulate at the same place, and this also leads to higher CT as time is long enough.

Figure 4. Influence of p on the chloride diffusion. 

Figure 4. Influence of p on the chloride diffusion. 

The impact of initial concentration Cs and porosity ε on chloride diffusion is shown in Figures  and . It is very easy to explain that higher initial concentration of free chloride will result in the higher CT at the same place or the same time. The reduction of porosity coefficient means that there are many more pores to absorb the chloride ions, which cause the increase of CT.

Figure 5. Influence of  Cs on the chloride diffusion.  

Figure 5. Influence of  Cs on the chloride diffusion.  

Figure 6. Influence of ϵ on the chloride diffusion. 

Figure 6. Influence of ϵ on the chloride diffusion. 

Figure  illustrates the effects of fractional derivatives on chloride diffusion in concrete. As shown in Figure (a), at the same diffusion depth, the smaller α is, the less chloride concentration is. As shown in Figure (b), the impact of β on diffusion has two sides. The increase of fractional derivative is beneficial to the accumulation of CT in front of the intersection and the influence degree is more obvious, while the opposite is true after the intersection. It also reveals that the spatial fractional derivative can reflect the nonlocality of diffusion. In a word, fractional order can describe the diffusion of materials in porous complex media well, which is consistent with the characteristics of time dependence and spatial nonlocality.

Figure 7. Influence of fractional derivatives on the chloride diffusion. 

Figure 7. Influence of fractional derivatives on the chloride diffusion. 

6. Conclusions

This study presents a time-space fractional model to describe the transport of chloride ions in seven different types of concrete. It is noteworthy that free chloride ions are presented in three forms in concrete due to reaction, and the impact of porosity on diffusion is taken into account. The fitting results also show that the time fractional order α and the space fractional order β can explain spatial nonlocality well. What's more, the finite difference method and the optimization algorithm can be applied to the similar fractional problems and to find the optimal value.

Acknowledgements

The work is supported by National Natural Science Foundation of China (No. 12072024), the Fundamental Research Funds for the Central Universities.

Disclosure statement

No potential conflict of interest was reported by the author(s).

Additional information

Funding

The work is supported by National Natural Science Foundation of China (No. 12072024), the Fundamental Research Funds for the Central Universities.

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