Chapter : Process Modelling Flashcards
what makes process modelling different from process analysis
the task involves process analysis with dynamics so there may be accumulation,generation and consumption terms so the models may comprise of differential equations
derive the mass balance
notes
derive volumetric balance
notes
how do we find a differential equation for the level in the tank from the mass balance
from the mass balance we can relate mass to volume through density formula. following that we can relate volume to level through the volume formula. therefore M= Aph
what is constant in the mass balance
flowrates, mass , level are not constant because they are functions of time. so density and area is the only constants
how is mass related to volume
density formula M= p x V
how is volume related to level
V = A x h
how is mass related
M = A x p x h
what is the control system based on for slide 7 and 8
the differential level equation because level is the controlled variable
what is the rate of change of stored heat
heat inflow - heat outflow
derive the heat balance
in notes
why does Fin=Fout
because volume is constant
why is hcond negligible compared to hst
the specific enthalpy of the condensate is negligible compared to the specific enthalpy of steam because the value is much smaller
what does the final heat balance equation relate
it relates the temperature inside the tank with the flow rate of steak and our disturbances
what are the potential disturbances for the heat equation
the temperature of steam may be subject to disturbances
the flowrate of steam may be subject to disturbances
the model may be wrong because steam can create foulingwhich leads to suboptimal performance heat exchange
why does the component balance using mass fraction and mass flowrate not have independent equations
because the mass fractions both add to unity
xA+xB=1
why does the component balance using concentrations and volumetric flow rate not have independent equations
becuase in a binary mixture CA+CB = p if the concentrations are in kg/m^3