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. Author manuscript; available in PMC: 2023 Feb 13.
Published in final edited form as: Chem Eng Res Des. 2018 Jun;134:140–153. doi: 10.1016/j.cherd.2018.03.017
Measured variables
M F1 API mass hold-up of Feeder 1 (kg)
M F2 Excipient mass hold-up of Feeder 2 (kg)
ω F1 Screw rotation speed of Feeder 1 (rpm)
ω F2 Screw rotation speed of Feeder 2 (rpm)
F B1,out Outlet mass flow rate of Blender 1 (kg/h)
C B1,out Outlet API concentration of Blender 1
ω B1 Agitator rotation speed of Blender 1 (rpm)
Unmeasured Variables
F F1 Mass flow rate of Feeder 1 (kg/h)
F F2 Mass flow rate of Feeder 2 (kg/h)
F B1,in Inlet mass flow rate of Blender 1 (kg/h)
C B1,in Inlet API concentration of Blender 1
M B1,n Mass hold-up of compartment n (kg)
F B1,n Outlet mass flow rate of compartment n (kg/h)
C B1,n Outlet API concentration of compartment n
Constants
ωF*, ωB1* Normal rotation speeds (rpm)
MF*, MB1,n* Normal mass hold-ups (kg)
σ*, δ* Variances of noise of state variables
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