{ "cells": [ { "cell_type": "code", "execution_count": 37, "metadata": {}, "outputs": [], "source": [ "#imports\n", "import numpy as np\n", "import matplotlib.pyplot as plt" ] }, { "cell_type": "code", "execution_count": 38, "metadata": {}, "outputs": [], "source": [ "#define constants\n", "\n", "g = 9.81 # gravitational acceleration [m/s²]\n", "\n", "L = 100 # length of pipeline [m]\n", "rho = 1000 # density of water [kg/m³]\n", "D = 1 # pipe diameter \n", "Q0 = 2 # initial flow in whole pipe [m³/s]\n", "h = 20 # water level in upstream reservoir [m]\n", "n = 10 # number of pipe segments in discretization\n", "nt = 150 # number of time steps\n", "f_coeff = 0.1 # lambda = 0.01 Friction loss coefficient [m]\n", "c = 400 # propagation velocity of the pressure wave\n", "\n" ] }, { "cell_type": "code", "execution_count": 39, "metadata": {}, "outputs": [], "source": [ "# preparing the discretization and initial conditions\n", "\n", "dx = L/n # length of each pipe segment\n", "dt = dx/c # timestep according to method of characterisitics\n", "nn = n+1 # number of nodes\n", "pl_vec = np.arange(0,nn*dx,dx) # pl = pipe-length. position of the nodes on the pipeline\n", "t_vec = np.arange(0,(nt)*dt,dt) # time vector\n", "\n", "v0 = Q0/(D**2/4*np.pi)\n", "p0 = (rho*g*h-v0**2*rho/2)\n", "\n", "# storage vectors for old parameters\n", "v_old = np.full(nn,v0)\n", "p_old = p0-(f_coeff*pl_vec/D*rho/2*v0**2) # ref Wikipedia: Rohrreibungszahls\n", "\n", "# storage vectors for new parameters\n", "v_new = np.zeros_like(v_old)\n", "p_new = np.zeros_like(p_old)\n", "\n", "# storage vector for time evolution of parameters at node nn (at reservoir)\n", "p_nn = np.zeros_like(t_vec)\n", "v_nn = np.zeros_like(t_vec)\n", "\n" ] }, { "cell_type": "code", "execution_count": 40, "metadata": {}, "outputs": [], "source": [ "%matplotlib qt\n", "# time loop\n", "\n", "fig = plt.figure()\n", "ax1 = fig.add_subplot(111)\n", "lo1, = ax1.plot(pl_vec,np.full_like(pl_vec,p0),marker='.')\n", "ax1.set_ylim([-20*p0,20*p0])\n", "\n", "for it in range(nt):\n", " # set boundary conditions\n", " v_new[-1] = 0 # in front of the instantaneously closing valve, the velocity is 0\n", " p_new[0] = p0 # hydrostatic pressure from the reservoir\n", "\n", " # calculate the new parameters at first and last node\n", " v_new[0] = v_old[1]+1/(rho*c)*(p0-p_old[1])-f_coeff*dt/(2*D)*abs(v_old[1])*v_old[1]\n", " p_new[-1] = p_old[-2]+rho*c*v_old[-2]-rho*c*f_coeff*dt/(2*D) *abs(v_old[-2])*v_old[-2]\n", "\n", " # calculate parameters at second to second-to-last nodes \n", " #equation 2-30 plus 2-31 (and refactor for v_i^j+1) in block 2\n", "\n", " for i in range(1,nn-1):\n", " v_new[i] = 0.5*(v_old[i-1]+v_old[i+1])+0.5/(rho*c)*(p_old[i-1]-p_old[i+1]) \\\n", " -f_coeff*dt/(4*D)*(abs(v_old[i-1])*v_old[i-1]+abs(v_old[i+1])*v_old[i+1])\n", "\n", " p_new[i] = 0.5*rho*c*(v_old[i-1]-v_old[i+1])+0.5*(p_old[i-1]+p_old[i+1]) \\\n", " -rho*c*f_coeff*dt/(4*D)*(abs(v_old[i-1])*v_old[i-1]-abs(v_old[i+1])*v_old[i+1])\n", " \n", " lo1.set_xdata(pl_vec)\n", " lo1.set_ydata(p_new)\n", " ax1.set_title(str(t_vec[it]))\n", " fig.canvas.draw()\n", " plt.pause(0.05)\n", "\n", " # store parameters of node 0 (at reservoir)\n", " p_nn[it] = p_old[-1]\n", " v_nn[it] = v_old[-1]\n", "\n", " # prepare for next loop\n", " p_old = p_new\n", " v_old = v_new\n", "\n", "\n", "\n" ] }, { "cell_type": "code", "execution_count": 42, "metadata": {}, "outputs": [ { "data": { "text/plain": [ "[]" ] }, "execution_count": 42, "metadata": {}, "output_type": "execute_result" } ], "source": [ "plt.plot(v_nn)" ] } ], "metadata": { "kernelspec": { "display_name": "Python 3.8.13 ('Georg_DT_Slot3')", "language": "python", "name": "python3" }, "language_info": { "codemirror_mode": { "name": "ipython", "version": 3 }, "file_extension": ".py", "mimetype": "text/x-python", "name": "python", "nbconvert_exporter": "python", "pygments_lexer": "ipython3", "version": "3.8.13" }, "orig_nbformat": 4, "vscode": { "interpreter": { "hash": "84fb123bdc47ab647d3782661abcbe80fbb79236dd2f8adf4cef30e8755eb2cd" } } }, "nbformat": 4, "nbformat_minor": 2 }