fixed a coding mistake that lead to
a missbehavior in the time evolution of the reservoir
This commit is contained in:
@@ -73,10 +73,12 @@ class Ausgleichsbecken_class:
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# sets the level in the reservoir and should only be called during initialization
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if self.level == '--':
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self.level = initial_level
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self.volume = self.update_volume()
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else:
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raise Exception('Initial level was already set once. Use the .update_level(self,timestep) method to update level based on net flux.')
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def set_level(self,level):
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self.level = level
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def set_influx(self,influx):
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# sets influx to the reservoir in m³/s
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# positive influx means that liquid flows into the reservoir
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@@ -95,15 +97,14 @@ class Ausgleichsbecken_class:
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def set_pressure(self,pressure):
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# sets the static pressure present at the outlet of the reservoir
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# units are used to convert and display the pressure
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self.pressure = pressure
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def set_steady_state(self,ss_influx,ss_level,display_pressure_unit):
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# set the steady state (ss) condition in which the net flux is zero
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# set pressure acting on the outflux area so that the level stays constant
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ss_outflux = ss_influx
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ss_influx_vel = ss_influx/self.area
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ss_outflux_vel = ss_outflux/self.area_outflux
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ss_influx_vel = abs(ss_influx/self.area)
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ss_outflux_vel = abs(ss_outflux/self.area_outflux)
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ss_pressure = self.density*self.g*ss_level+self.density*ss_outflux_vel*(ss_influx_vel-ss_outflux_vel)
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self.set_influx(ss_influx)
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@@ -115,6 +116,7 @@ class Ausgleichsbecken_class:
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def get_info(self, full = False):
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new_line = '\n'
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p = pressure_conversion(self.pressure,self.pressure_unit,self.pressure_unit_print)
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outflux_vel = self.outflux/self.area_outflux
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if full == True:
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@@ -129,7 +131,7 @@ class Ausgleichsbecken_class:
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f"Volume in reservoir = {self.volume:<10} {self.volume_unit_print} {new_line}"
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f"Current influx = {self.influx:<10} {self.flux_unit_print} {new_line}"
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f"Current outflux = {self.outflux:<10} {self.flux_unit_print} {new_line}"
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f"Current outflux vel = {round(self.outflux_vel,3):<10} {self.velocity_unit_print} {new_line}"
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f"Current outflux vel = {round(outflux_vel,3):<10} {self.velocity_unit_print} {new_line}"
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f"Current pipe pressure = {round(p,3):<10} {self.pressure_unit_print} {new_line}"
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f"Simulation timestep = {self.timestep:<10} {self.time_unit_print} {new_line}"
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f"Density of liquid = {self.density:<10} {self.density_unit_print} {new_line}"
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@@ -142,7 +144,7 @@ class Ausgleichsbecken_class:
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f"Volume in reservoir = {self.volume:<10} {self.volume_unit_print} {new_line}"
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f"Current influx = {self.influx:<10} {self.flux_unit_print} {new_line}"
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f"Current outflux = {self.outflux:<10} {self.flux_unit_print} {new_line}"
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f"Current outflux vel = {round(self.outflux_vel,3):<10} {self.velocity_unit_print} {new_line}"
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f"Current outflux vel = {round(outflux_vel,3):<10} {self.velocity_unit_print} {new_line}"
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f"Current pipe pressure = {round(p,3):<10} {self.pressure_unit_print} {new_line}"
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f"----------------------------- {new_line}")
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@@ -157,9 +159,6 @@ class Ausgleichsbecken_class:
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def get_current_outflux(self):
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return self.outflux
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def get_current_volume(self):
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return self.volume
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def get_current_pressure(self):
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return self.pressure
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@@ -174,19 +173,14 @@ class Ausgleichsbecken_class:
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# cannot set new level directly in this method, because it gets called to calcuate during the Runge Kutta
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# to calculate a ficticious level at half the timestep
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net_flux = self.influx-self.outflux
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delta_V = net_flux*timestep
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new_level = (self.volume+delta_V)/self.area
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delta_level = net_flux*timestep/self.area
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new_level = (self.level+delta_level)
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return new_level
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def update_volume(self):
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# sets volume in reservoir based on self.level
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return self.level*self.area
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def update_pressure(self):
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influx_vel = self.influx/self.area
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outflux_vel = self.outflux/self.area_outflux
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influx_vel = abs(self.influx/self.area)
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outflux_vel = abs(self.outflux/self.area_outflux)
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p_new = self.density*self.g*self.level+self.density*outflux_vel*(influx_vel-outflux_vel)
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return p_new
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def timestep_reservoir_evolution(self):
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@@ -209,8 +203,10 @@ class Ausgleichsbecken_class:
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ynp1 = yn + dt/6*(FODE_function(Y1,h,A,A_a,p,rho,g)+2*FODE_function(Y2,h_hs,A,A_a,p_hs,rho,g)+ \
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2*FODE_function(Y3,h_hs,A,A_a,p_hs,rho,g)+ FODE_function(Y4,h,A,A_a,p,rho,g))
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self.outflux = ynp1*A_a
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self.level = self.update_level(dt)
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self.volume = self.update_volume()
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self.pressure = self.update_pressure()
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new_outflux = ynp1*A_a
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new_level = self.update_level(dt)
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new_pressure = self.update_pressure()
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self.set_outflux(new_outflux)
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self.set_level(new_level)
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self.set_pressure(new_pressure)
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@@ -2,7 +2,7 @@
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"cells": [
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{
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"cell_type": "code",
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"execution_count": 13,
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"execution_count": 1,
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"metadata": {},
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"outputs": [],
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"source": [
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@@ -21,7 +21,7 @@
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},
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{
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"cell_type": "code",
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"execution_count": 14,
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"execution_count": 2,
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"metadata": {},
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"outputs": [],
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"source": [
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@@ -51,7 +51,7 @@
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},
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{
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"cell_type": "code",
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"execution_count": 15,
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"execution_count": 3,
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"metadata": {},
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"outputs": [],
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"source": [
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@@ -71,20 +71,20 @@
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"\n",
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"# for while loop\n",
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"total_min_level = 0.01 # m\n",
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"total_max_time = 1 # s\n",
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"total_max_time = 100 # s\n",
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"\n",
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"nt = int(total_max_time//simulation_timestep)"
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]
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},
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{
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"cell_type": "code",
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"execution_count": 16,
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"execution_count": 4,
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"metadata": {},
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"outputs": [],
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"source": [
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"%matplotlib qt\n",
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"\n",
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"V = Ausgleichsbecken_class(area_base, area_outflux, critical_level_low, critical_level_high,simulation_timestep)\n",
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"V = Ausgleichsbecken_class(area_base,area_outflux,critical_level_low,critical_level_high,simulation_timestep)\n",
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"# V.set_initial_level(initial_level) \n",
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"# V.set_influx(initial_influx)\n",
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"# V.set_outflux(initial_outflux)\n",
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@@ -119,7 +119,7 @@
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},
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{
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"cell_type": "code",
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"execution_count": 17,
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"execution_count": 5,
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"metadata": {},
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"outputs": [],
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"source": [
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@@ -149,7 +149,7 @@
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},
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{
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"cell_type": "code",
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"execution_count": 18,
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"execution_count": 6,
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"metadata": {},
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"outputs": [
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{
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@@ -158,7 +158,7 @@
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"10.1"
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]
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},
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"execution_count": 18,
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"execution_count": 6,
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"metadata": {},
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"output_type": "execute_result"
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}
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@@ -118,8 +118,8 @@ class Druckrohrleitung_class:
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ss_v0 = np.full(self.n_seg+1,ss_flux/self.A)
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# the static pressure is given by static state pressure of the reservoir, corrected for the hydraulic head of the pipe and friction losses
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ss_v_in_res = ss_flux/area_reservoir
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ss_v_out_res = ss_flux/self.A
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ss_v_in_res = abs(ss_flux/area_reservoir)
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ss_v_out_res = abs(ss_flux/self.A)
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ss_pressure_res = self.density*self.g*(ss_level_reservoir)+self.density*ss_v_out_res*(ss_v_in_res-ss_v_out_res)
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ss_pressure = ss_pressure_res+(self.density*self.g*h_vec)-(self.f_D*pl_vec/self.dia*self.density/2*ss_v0**2)
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File diff suppressed because it is too large
Load Diff
100
Untertweng.ipynb
100
Untertweng.ipynb
@@ -2,7 +2,7 @@
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"cells": [
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{
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"cell_type": "code",
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"execution_count": null,
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"execution_count": 1,
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"metadata": {},
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"outputs": [],
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"source": [
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@@ -17,7 +17,7 @@
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},
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{
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"cell_type": "code",
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"execution_count": null,
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"execution_count": 2,
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"metadata": {},
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"outputs": [],
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"source": [
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@@ -26,7 +26,7 @@
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"#Turbine\n",
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"Q_nenn = 0.85 # m³/s\n",
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"p_nenn = pressure_conversion(10.6,'bar','Pa')\n",
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"closing_time = 30 #s\n",
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"closing_time = 5 #s\n",
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"\n",
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"# physics\n",
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"g = 9.81 # gravitational acceleration [m/s²]\n",
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@@ -38,14 +38,14 @@
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"A_pipe = D**2/4*np.pi # pipeline area\n",
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"h_pipe = 105 # hydraulic head without reservoir [m] \n",
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"alpha = np.arcsin(h_pipe/L) # Höhenwinkel der Druckrohrleitung \n",
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"n = 200 # number of pipe segments in discretization\n",
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"n = 50 # number of pipe segments in discretization\n",
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"# consider replacing Q0 with a vector be be more flexible in initial conditions\n",
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"# Q0 = Q_nenn # initial flow in whole pipe [m³/s]\n",
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"# v0 = Q0/A_pipe # initial flow velocity [m/s]\n",
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"f_D = 0.014 # Darcy friction factor\n",
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"c = 500. # propagation velocity of the pressure wave [m/s]\n",
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"# consider prescribing a total simulation time and deducting the number of timesteps from that\n",
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"nt = 20000 # number of time steps after initial conditions\n",
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"nt = 2500 # number of time steps after initial conditions\n",
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"\n",
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"# derivatives of the pipeline constants\n",
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"dx = L/n # length of each pipe segment\n",
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@@ -69,7 +69,7 @@
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"critical_level_high = np.inf # for yet-to-be-implemented warnings[m]\n",
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"\n",
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"# make sure e-RK4 method of reservoir has a small enough timestep to avoid runaway numerical error\n",
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"nt_eRK4 = 1000 # number of simulation steps of reservoir in between timesteps of pipeline \n",
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"nt_eRK4 = 100 # number of simulation steps of reservoir in between timesteps of pipeline \n",
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"simulation_timestep = dt/nt_eRK4\n",
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"\n",
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"\n"
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@@ -77,7 +77,7 @@
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},
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{
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"cell_type": "code",
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"execution_count": null,
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"execution_count": 3,
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"metadata": {},
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"outputs": [],
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"source": [
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@@ -90,7 +90,7 @@
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"pipe = Druckrohrleitung_class(L,D,n,alpha,f_D)\n",
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"pipe.set_pressure_propagation_velocity(c)\n",
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"pipe.set_number_of_timesteps(nt)\n",
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"pipe.set_steady_state(initial_flux,initial_level,pl_vec,h_vec)\n",
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"pipe.set_steady_state(initial_flux,initial_level,area_base,pl_vec,h_vec)\n",
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"\n",
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"initial_pressure_turbine = pipe.get_current_pressure_distribution()[-1]\n",
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"\n",
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@@ -105,7 +105,7 @@
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},
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{
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"cell_type": "code",
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"execution_count": null,
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"execution_count": 4,
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"metadata": {},
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"outputs": [],
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"source": [
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@@ -142,7 +142,7 @@
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},
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{
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"cell_type": "code",
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"execution_count": null,
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"execution_count": 5,
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"metadata": {},
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"outputs": [],
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"source": [
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@@ -170,21 +170,20 @@
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},
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{
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"cell_type": "code",
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"execution_count": null,
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"execution_count": 6,
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"metadata": {},
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"outputs": [],
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"source": [
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"# loop through time steps of the pipeline\n",
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"for it_pipe in range(1,pipe.nt+1):\n",
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"\n",
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" if t_vec[it_pipe]>20:\n",
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" if V.get_current_influx() > 0:\n",
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" V.set_influx(np.max([V.get_current_influx()-initial_flux*5*1e-3,0.]))\n",
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" if it_pipe == 250:\n",
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" V.set_influx(0.)\n",
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"\n",
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"# for each pipeline timestep, execute nt_eRK4 timesteps of the reservoir code\n",
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" # set initial conditions for the reservoir time evolution calculted with e-RK4\n",
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" V.set_pressure = p_old[0]\n",
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" V.set_outflux = v_old[0]*area_outflux\n",
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" V.set_pressure(p_old[0])\n",
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" V.set_outflux(v_old[0]*area_outflux)\n",
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" # calculate the time evolution of the reservoir level within each pipeline timestep to avoid runaway numerical error\n",
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" for it_res in range(nt_eRK4):\n",
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" V.timestep_reservoir_evolution() \n",
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@@ -233,7 +232,24 @@
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},
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{
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"cell_type": "code",
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"execution_count": null,
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"execution_count": 7,
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"metadata": {},
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"outputs": [
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{
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"name": "stdout",
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"output_type": "stream",
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"text": [
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"0.0\n"
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]
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}
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],
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"source": [
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"print(V.get_current_influx())"
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]
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},
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{
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"cell_type": "code",
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"execution_count": 8,
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"metadata": {},
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"outputs": [],
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"source": [
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@@ -274,11 +290,57 @@
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"fig2.tight_layout()\n",
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"plt.show()"
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]
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},
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{
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"cell_type": "code",
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"execution_count": 9,
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"metadata": {},
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"outputs": [
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{
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"name": "stdout",
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"output_type": "stream",
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"text": [
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"The cuboid reservoir has the following attributes: \n",
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"----------------------------- \n",
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"Base area = 74.0 m² \n",
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"Outflux area = 0.636 m² \n",
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"Current level = 7.875725956447418 m\n",
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"Critical level low = 0.0 m \n",
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"Critical level high = inf m \n",
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"Volume in reservoir = -- m³ \n",
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"Current influx = 0.0 m³/s \n",
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"Current outflux = -0.1415386124341686 m³/s \n",
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"Current outflux vel = -0.222 m/s \n",
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"Current pipe pressure = 0.772 bar \n",
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"Simulation timestep = 0.0004052 s \n",
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"Density of liquid = 1000 kg/m³ \n",
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"----------------------------- \n",
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"\n",
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"9.22707730779877\n",
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"10.57842865915012\n",
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"11.92978001050147\n",
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"13.281131361852822\n",
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"14.632482713204173\n",
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"15.983834064555523\n",
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"17.335185415906874\n",
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"18.686536767258225\n",
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"20.037888118609576\n",
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"21.389239469960927\n"
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]
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}
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],
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"source": [
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"V.get_info(full=True)\n",
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"V.set_outflux(-10.)\n",
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"for i in range(10):\n",
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" V.level = V.update_level(10.)\n",
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" print(V.get_current_level())"
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]
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}
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],
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"metadata": {
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"kernelspec": {
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"display_name": "Python 3.8.13 ('Georg_DT_Slot3')",
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"display_name": "Python 3.8.13 ('DT_Slot_3')",
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"language": "python",
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"name": "python3"
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},
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@@ -297,7 +359,7 @@
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"orig_nbformat": 4,
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"vscode": {
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||||
"interpreter": {
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||||
"hash": "84fb123bdc47ab647d3782661abcbe80fbb79236dd2f8adf4cef30e8755eb2cd"
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"hash": "4a28055eb8a3160fa4c7e4fca69770c4e0a1add985300856aa3fcf4ce32a2c48"
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}
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||||
}
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||||
},
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||||
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Reference in New Issue
Block a user