module constants
implicit none
! 物理常数
real, parameter :: pi = 3.141592653589793
real, parameter :: R_univ = 8.314462618 ! 通用气体常数 [J/(mol·K)]
real, parameter :: k_B = 1.380649e-23 ! 玻尔兹曼常数 [J/K]
real, parameter :: N_A = 6.02214076e23 ! 阿伏伽德罗常数 [1/mol]
! 水物性参数
real, parameter :: M_H2O = 0.018015 ! 水的摩尔质量 [kg/mol]
real, parameter :: rho_l = 1000.0 ! 液态水密度 [kg/m³]
real, parameter :: sigma_H2O = 0.072 ! 表面张力 [N/m]
real, parameter :: h_fg = 2.257e6 ! 汽化潜热 [J/kg]
real, parameter :: cp_v = 1410.0 ! 水蒸气比热 [J/(kg·K)]
! 发动机参数
real, parameter :: De = 0.2 ! 喷口直径 [m]
real, parameter :: T0 = 1000.0 ! 喷口温度 [K]
real, parameter :: P0 = 50000.0 ! 喷口压力 [Pa]
real, parameter :: U0 = 2000.0 ! 喷口速度 [m/s]
real, parameter :: X_H2O = 0.22 ! 水蒸气摩尔分数
! 数值参数
integer, parameter :: nx = 100 ! 空间网格数
integer, parameter :: nt = 1000 ! 时间步数
real, parameter :: dt = 1e-5 ! 时间步长 [s]
real, parameter :: L_domain = 10.0 * De ! 计算域长度 [m]
end module constants
program condensation_model
use constants
implicit none
! 场变量定义
real :: x(nx), dx
real :: T_g(nx), P_g(nx), U_g(nx), rho_g(nx)
real :: N_d(nx), Y_d(nx), r_d(nx) ! 液滴数密度、质量分数、半径
real :: m_v(nx), J_nuc(nx), dr_dt(nx) ! 凝结速率、成核率、半径增长率
! 辅助变量
real :: S(nx), r_c(nx), P_sat(nx)
integer :: i, t_step
! 初始化网格
dx = L_domain / (nx - 1)
do i = 1, nx
x(i) = (i - 1) * dx
end do
! 初始化流场 (简化线性分布)
do i = 1, nx
P_g(i) = P0 * (1.0 - 0.8 * x(i)/L_domain)
T_g(i) = T0 * (1.0 - 0.6 * x(i)/L_domain)
U_g(i) = U0 * (1.0 - 0.3 * x(i)/L_domain)
rho_g(i) = P_g(i) / (287.0 * T_g(i)) ! 空气气体常数
end do
! 初始化液相变量
N_d = 0.0
Y_d = 0.0
r_d = 0.0
! 时间迭代循环
do t_step = 1, nt
! 计算过饱和比和临界半径
call calculate_saturation_ratio(P_g, T_g, S, P_sat, r_c)
! 应用Schmidt-Appleman冷凝判据
where(S > 1.0)
! Schmidt-Appleman条件: 仅当S>1时计算成核
call nucleation_model(T_g, rho_g, S, r_c, J_nuc)
call droplet_growth_model(T_g, rho_g, r_d, r_c, S, dr_dt)
elsewhere
J_nuc = 0.0
dr_dt = 0.0
end where
! 计算凝结质量速率
do i = 1, nx
if (r_d(i) > 0.0) then
m_v(i) = 4.0 * pi * r_d(i)**2 * rho_l * dr_dt(i) * N_d(i)
else
m_v(i) = 0.0
endif
end do
! 更新液相控制方程
call update_liquid_phase(N_d, Y_d, r_d, J_nuc, m_v, dr_dt)
! 更新气相控制方程
call update_gas_phase(T_g, P_g, U_g, rho_g, m_v)
! 输出数据 (每100步输出一次)
if (mod(t_step, 100) == 0) then
call output_data(t_step, x, T_g, P_g, N_d, Y_d, r_d)
end if
end do
! 输出最终结果
call output_data(nt, x, T_g, P_g, N_d, Y_d, r_d)
contains
! 计算饱和比和临界半径
subroutine calculate_saturation_ratio(P, T, S, P_sat, r_c)
real, intent(in) :: P(:), T(:)
real, intent(out) :: S(:), P_sat(:), r_c(:)
integer :: i
do i = 1, size(P)
! Antoine方程计算饱和蒸气压 (简化形式)
P_sat(i) = 611.0 * exp(5423.0 * (1.0/273.0 - 1.0/T(i))) ! [Pa]
! 过饱和比
S(i) = (X_H2O * P(i)) / P_sat(i)
! Kelvin-Helmholtz临界半径
if (S(i) > 1.0) then
r_c(i) = 2.0 * sigma_H2O / (rho_l * (R_univ/M_H2O) * T(i) * log(S(i)))
else
r_c(i) = 1e-9 ! 极小值
end if
end do
end subroutine
! 成核模型 (经典成核理论)
subroutine nucleation_model(T, rho_g, S, r_c, J_nuc)
real, intent(in) :: T(:), rho_g(:), S(:), r_c(:)
real, intent(out) :: J_nuc(:)
real :: A, B, DeltaG
integer :: i
do i = 1, size(T)
if (S(i) > 1.0) then
! 吉布斯自由能变化
DeltaG = 4.0 * pi * r_c(i)**2 * sigma_H2O / 3.0
! 成核率计算 (简化阿伦尼乌兹形式)
A = 1e30 ! 指前因子 [1/(m³·s)]
B = 4.0 * pi * r_c(i)**2 * sigma_H2O / (3.0 * k_B * T(i))
J_nuc(i) = A * exp(-B)
else
J_nuc(i) = 0.0
end if
end do
end subroutine
! Gyarmathy液滴生长模型
subroutine droplet_growth_model(T, rho_g, r, r_c, S, dr_dt)
real, intent(in) :: T(:), rho_g(:), r(:), r_c(:), S(:)
real, intent(out) :: dr_dt(:)
real :: lambda_v, Kn, Pr_v, T_sat
integer :: i
do i = 1, size(T)
if (S(i) > 1.0 .and. r(i) > 0.0) then
! 蒸汽导热系数
lambda_v = 0.026
! 克努森数
Kn = sqrt(pi * M_H2O / (2.0 * R_univ * T(i))) / r(i)
! 普朗特数
Pr_v = 0.71
! 过冷度
T_sat = 373.0 - (P_g(i) - 101325.0) * 0.00025
! Gyarmathy模型
dr_dt(i) = lambda_v * (T_sat - T(i)) * (1.0 - r_c(i)/r(i)) &
/ (rho_l * h_fg * r(i) * (1.0 + 3.78*(1.0 - 0.82*Kn)/Pr_v * Kn))
else
dr_dt(i) = 0.0
end if
end do
end subroutine
! 更新液相变量
subroutine update_liquid_phase(N_d, Y_d, r_d, J_nuc, m_v, dr_dt)
real, intent(inout) :: N_d(:), Y_d(:), r_d(:)
real, intent(in) :: J_nuc(:), m_v(:), dr_dt(:)
integer :: i
do i = 1, size(N_d)
! 更新数密度 (考虑对流和成核)
N_d(i) = N_d(i) + dt * (J_nuc(i) - U_g(i) * (N_d(i) - N_d(max(1,i-1)))/dx)
! 更新质量分数 (考虑对流和凝结)
Y_d(i) = Y_d(i) + dt * (m_v(i)/rho_l - U_g(i) * (Y_d(i) - Y_d(max(1,i-1)))/dx)
! 更新液滴半径 (考虑生长)
if (N_d(i) > 0.0) then
r_d(i) = r_d(i) + dt * dr_dt(i)
! 从质量和数量计算半径 (作为验证)
r_d(i) = (3.0 * Y_d(i) / (4.0 * pi * rho_l * N_d(i)))**(1.0/3.0)
else
r_d(i) = 0.0
end if
end do
end subroutine
! 更新气相变量
subroutine update_gas_phase(T, P, U, rho, m_v)
real, intent(inout) :: T(:), P(:), U(:), rho(:)
real, intent(in) :: m_v(:)
integer :: i
do i = 2, size(T)-1
! 连续方程
rho(i) = rho(i) - dt * m_v(i)
! 动量方程
U(i) = U(i) - dt * U(i) * (U(i) - U(i-1))/dx - dt*(P(i)-P(i-1))/(dx*rho(i))
! 能量方程
T(i) = T(i) - dt * U(i) * (T(i) - T(i-1))/dx + dt * m_v(i) * h_fg / (rho(i) * cp_v)
! 状态方程
P(i) = rho(i) * 287.0 * T(i)
end do
end subroutine
! 数据输出
subroutine output_data(step, x, T, P, N, Y, r)
integer, intent(in) :: step
real, intent(in) :: x(:), T(:), P(:), N(:), Y(:), r(:)
character(len=50) :: filename
integer :: i
! 云图数据
write(filename, '(a,i6.6,a)') 'cloud_data_', step, '.dat'
open(unit=10, file=filename, status='replace')
write(10, *) 'Variables = "x", "T", "P", "N", "Y", "r"'
do i = 1, size(x)
write(10, '(6e16.7)') x(i), T(i), P(i), N(i), Y(i), r(i)
end do
close(10)
! 时间序列数据 (在特定位置)
if (step == nt) then
open(unit=11, file='time_data.dat', status='replace')
write(11, *) 'Variables = "Time", "N_center", "Y_center", "r_center"'
do i = 1, nt, 100
write(11, '(4e16.7)') i*dt, N(nx/2), Y(nx/2), r(nx/2)
end do
close(11)
end if
end subroutine
end program condensation_model修改程序error #7361: Only array assignment-stmt, where-stmt, where-construct-stmt, elsewhere-stmt, masked-elsewhere-stmt, or endwhere-stmt permitted.
Compilation Aborted (code 1)
Compilation Aborted (code 1)
error #7361: Only array assignment-stmt, where-stmt, where-construct-stmt, elsewhere-stmt, masked-elsewhere-stmt, or endwhere-stmt permitted.
error #7361: Only array assignment-stmt, where-stmt, where-construct-stmt, elsewhere-stmt, masked-elsewhere-stmt, or endwhere-stmt permitted.
error #7361: Only array assignment-stmt, where-stmt, where-construct-stmt, elsewhere-stmt, masked-elsewhere-stmt, or endwhere-stmt permitted.