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THERE ARE SOME CODES FOR NUMERİCAL APPROACH THAT DEFİNES DİSCRETZATİON AND DEVELOPMENT OF THE CODE İT EXPLAİNS HOW THE FOLLOWİNG MATLAB CODES ARE CREATED
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To develop an explicit scheme to solve the advection-diffusion equation numerically, we can use a finite difference approximation. Let's start by discretizing the equation in both time and space. Discretization in Time: We'll use a forward difference approximation for the time derivative: 𝜕𝑐/𝜕𝑡 ≈ (𝑐ᵢⱼ⁺¹ - 𝑐ᵢⱼ) / Δ𝑡 Discretization in Space: We'll use a centered difference approximation for the spatial derivatives: 𝜕²𝑐/𝜕𝑥² ≈ (𝑐ᵢ⁺¹ⱼ - 2 𝑐ᵢⱼ + 𝑐ᵢ⁻¹ⱼ) / Δ𝑥² 𝜕𝑐/𝜕𝑥 ≈ (𝑐ᵢ⁺¹ⱼ - 𝑐ᵢ⁻¹ⱼ) / (2Δ𝑥) Now, substitute these approximations into the advection-diffusion equation: (𝑐ᵢⱼ⁺¹ - 𝑐ᵢⱼ) / Δ𝑡 = 𝐷 (𝑐ᵢ⁺¹ⱼ - 2 𝑐ᵢⱼ + 𝑐ᵢ⁻¹ⱼ) / Δ𝑥² - 𝑈 (𝑐ᵢ⁺¹ⱼ - 𝑐ᵢ⁻¹ⱼ) / (2Δ𝑥) - 𝑘𝑐ᵢⱼ Where i represents the spatial index (along x-axis) and j represents the temporal index (along t-axis). Now, rearrange the equation to solve for the unknown concentration at the next time step, cᵢⱼ⁺¹: cᵢⱼ⁺¹ = cᵢⱼ + (Δ𝑡 / Δ𝑥²) * D * (cᵢ⁺¹ⱼ - 2cᵢⱼ + cᵢ⁻¹ⱼ) - (Δ𝑡 / (2Δ𝑥)) * U * (cᵢ⁺¹ⱼ - cᵢ⁻¹ⱼ) - Δ𝑡 * k * cᵢⱼ Now, we can proceed with the numerical simulation using the given parameters and the derived explicit scheme. a) Steady Condition: In the steady-state condition, the concentration does not change with time. We can solve the equation iteratively until the solution converges to a steady state. In this case, we'll simulate until the change in concentration between two consecutive time steps is below a certain threshold. Initialize parameters and variables: Length of the tank (L) = 10 m
Diffusion coefficient (D) = 100 m²/min Velocity in the x-direction (U) = 1 m/min Reaction rate (k) = 0.15 min⁻¹ Inflow concentration (c_inflow) = 100 mg/m³ Initial concentration (c_initial) = 0 mg/m³ Time step size (Δt) = 0.005 min Spatial step size (Δx) = 1 m Threshold for convergence ( User continue ChatGPT Threshold for convergence (convergence_threshold) = 1e-6 mg/m³ Determine the number of spatial and temporal grid points: Number of spatial grid points (N_x) = L / Δx Number of temporal grid points (N_t) = T / Δt, where T = 100 min Initialize the concentration matrix: Create a matrix C of size (N_x + 1) x (N_t + 1) to store concentration values at each grid point. Set the initial concentration values: C[:, 0] = c_initial Perform the explicit time-stepping iteration until convergence: Set the maximum number of iterations (max_iterations) to prevent an infinite loop. Initialize the iteration counter (iteration) to 0. Initialize the change in concentration (delta_c) to a large value (e.g., convergence_threshold + 1). Start the iteration loop:
% Parameters L = 10; % Length of the tank (m) D = 100; % Diffusion coefficient (m^2/min) U = 1; % Velocity in the x-direction (m/min) k = 0.15; % Reaction rate (min^-1) c_inflow = 100; % Inflow concentration (mg/m^3) c_initial = 0; % Initial concentration (mg/m^3) T = 100; % Total simulation time (min) dt = 0.005; % Time step size (min) dx = 1; % Spatial step size (m) % Derived parameters Nx = L / dx; % Number of spatial grid points Nt = T / dt; % Number of temporal grid points % Initialize concentration matrix C = zeros(Nx+1, Nt+1); C(:, 1) = c_initial; % Perform explicit time-stepping iteration convergence_threshold = 1e-6; % Convergence threshold max_iterations = 10000; % Maximum number of iterations delta_c = convergence_threshold + 1; % Initialize change in concentration iteration = 0; % Iteration counter while delta_c > convergence_threshold && iteration < max_iterations delta_c = 0; for j = 1:Nt for i = 2:Nx C(i, j+1) = C(i, j) + (dt / dx^2) * D * (C(i+1, j) - 2 * C(i, j) + C(i-1, j)) ...