python - 带 GEKKO 的 MPC 中的变量边界

Question

我正在尝试使用 MPC 和 GEKKO 实现恒温器控制。

状态变量(温度)应在预先指定的下限和上限温度值范围内，temp_low和 temp_upper在下面的代码中。

两者的界限在一天中都不同:每小时一个值。

目标函数是使用加热的成本。价格也随日变化，TOU以下。 T_external是在微分方程中起作用的房间外部温度。

如何实现它以使其优化？

这是我的尝试:

from gekko import GEKKO
import numpy as np

m = GEKKO(remote=False)
m.time = np.linspace(0,23,24)

#initialize variables
T_external = [50.,50.,50.,50.,45.,45.,45.,60.,60.,63.,64.,45.,45.,50.,52.,53.,53.,54.,54.,53.,52.,51.,50.,45.]
temp_low = [55.,55.,55.,55.,55.,55.,55.,68.,68.,68.,68.,55.,55.,68.,68.,68.,68.,55.,55.,55.,55.,55.,55.,55.]
temp_upper = [75.,75.,75.,75.,75.,75.,75.,70.,70.,70.,70.,75.,75.,70.,70.,70.,70.,75.,75.,75.,75.,75.,75.,75.]
TOU = [0.05,0.05,0.05,0.05,0.05,0.05,0.05,200.,200.,200.,200.,200.,200.,200.,200.,200.,200.,200.,200.,200.,200.,0.05,0.05,0.05]

b = m.Param(value=1.)
k = m.Param(value=0.05)
T_e = m.Param(value=T_external)

u = m.MV(value=[0]*24, lb=[0.0]*24, ub=[1.]*24)
u.STATUS = 1  # allow optimizer to change

# Controlled Variable
T = m.SV(value=[60]*24, lb=temp_low, ub=temp_upper)

m.Equation(T.dt() == k*(T_e-T) + b*u)

m.Obj(np.dot(TOU,u))

m.options.IMODE = 6
m.solve(debug=True)

当我运行这个时，我得到:

@error: Model Expression
 *** Error in syntax of function string: Missing operator

Position: 4                   
 0.0,0.0,0.0,0.0,0.0,0.0,0.0,0.0,0.0,0.0,0.0,0.0,0.0,0.0,0.0,0.0,0.0,0.0,0.0,0.0,0.0,0.0,0.0,0.0
    ?

Answer 1

Gekko 需要将约束作为不等式表达式，其中变量 T相比于上TH或更低 TL值。如果您有 b=1. ，这导致了一个不可行的解决方案，因为加热器的功率不足以将温度保持在上限和下限内。我将值更改为 b=10以获得可行的解决方案。

from gekko import GEKKO
import numpy as np

m = GEKKO(remote=False)
m.time = np.linspace(0,23,24)

#initialize variables
T_external = [50.,50.,50.,50.,45.,45.,45.,60.,60.,63.,\
              64.,45.,45.,50.,52.,53.,53.,54.,54.,\
              53.,52.,51.,50.,45.]
temp_low = [55.,55.,55.,55.,55.,55.,55.,68.,68.,68.,68.,\
            55.,55.,68.,68.,68.,68.,55.,55.,55.,55.,55.,55.,55.]
temp_upper = [75.,75.,75.,75.,75.,75.,75.,70.,70.,70.,70.,75.,\
              75.,70.,70.,70.,70.,75.,75.,75.,75.,75.,75.,75.]
TOU_v = [0.05,0.05,0.05,0.05,0.05,0.05,0.05,200.,200.,200.,200.,\
         200.,200.,200.,200.,200.,200.,200.,200.,200.,200.,0.05,\
         0.05,0.05]

b = m.Param(value=10.)
k = m.Param(value=0.05)
T_e = m.Param(value=T_external)
TL = m.Param(value=temp_low)
TH = m.Param(value=temp_upper)
TOU = m.Param(value=TOU_v)

u = m.MV(lb=0, ub=1)
u.STATUS = 1  # allow optimizer to change

# Controlled Variable
T = m.SV(value=60)

m.Equations([T>=TL,T<=TH])
m.Equation(T.dt() == k*(T_e-T) + b*u)

m.Minimize(TOU*u)

m.options.IMODE = 6
m.solve(disp=True,debug=True)

一个可能更好的解决方案是通过将限制重新定义为错误来设置软约束。您可以 minimize the error to stay within the limits .即使不能保持在限制范围内，优化器也会尽其所能将不可行性降到最低。这也允许您 trade-off multiple objectives同时，例如在舒适性和成本之间。

from gekko import GEKKO
import numpy as np

m = GEKKO(remote=False)
m.time = np.linspace(0,23,24)

#initialize variables
T_external = [50.,50.,50.,50.,45.,45.,45.,60.,60.,63.,\
              64.,45.,45.,50.,52.,53.,53.,54.,54.,\
              53.,52.,51.,50.,45.]
temp_low = [55.,55.,55.,55.,55.,55.,55.,68.,68.,68.,68.,\
            55.,55.,68.,68.,68.,68.,55.,55.,55.,55.,55.,55.,55.]
temp_upper = [75.,75.,75.,75.,75.,75.,75.,70.,70.,70.,70.,75.,\
              75.,70.,70.,70.,70.,75.,75.,75.,75.,75.,75.,75.]
TOU_v = [0.05,0.05,0.05,0.05,0.05,0.05,0.05,200.,200.,200.,200.,\
         200.,200.,200.,200.,200.,200.,200.,200.,200.,200.,0.05,\
         0.05,0.05]

b = m.Param(value=10.)
k = m.Param(value=0.05)
T_e = m.Param(value=T_external)
TL = m.Param(value=temp_low)
TH = m.Param(value=temp_upper)
TOU = m.Param(value=TOU_v)

u = m.MV(lb=0, ub=1)
u.STATUS = 1  # allow optimizer to change

# Controlled Variable
T = m.SV(value=60)

# Soft constraints
eH = m.CV(value=0)
eL = m.CV(value=0)

eH.SPHI=0; eH.WSPHI=100; eH.WSPLO=0  ; eH.STATUS = 1
eL.SPLO=0; eL.WSPHI=0  ; eL.WSPLO=100; eL.STATUS = 1

m.Equations([eH==T-TH,eL==T-TL])

m.Equation(T.dt() == k*(T_e-T) + b*u)

m.Minimize(TOU*u)

m.options.IMODE = 6
m.solve(disp=True,debug=True)

import matplotlib.pyplot as plt
plt.subplot(2,1,1)
plt.plot(m.time,temp_low,'k--')
plt.plot(m.time,temp_upper,'k--')
plt.plot(m.time,T.value,'r-')
plt.ylabel('Temperature')
plt.subplot(2,1,2)
plt.step(m.time,u.value,'b:')
plt.ylabel('Heater')
plt.xlabel('Time (hr)')
plt.show()