Steady-state and unsteady-state mass balances, steady-state and unsteady-state energy balances, recycle and bypass processes, and reactive systems including combustion, with conversion, yield, and extent of reaction.
6 concepts
The steady-state total and component mass balance, degrees-of-freedom analysis, tie components, and a disciplined recipe for solving multi-unit flowsheets.
Accumulation = in − out + generation. Per unit time for a defined control volume; in kg/s (or mol/s for a species).
Mass or mole fractions in any single stream sum to unity — one usable equation per stream.
An inert that enters and leaves in one stream each directly links the two stream flows
For species, only of the (total +
Evaporator concentration with a solids balance
Problem. A feed of of an aqueous solution containing dissolved solids by mass is concentrated in an evaporator to a product containing solids. Find the product mass flow and the water evaporated.
Distillation overall balance
Problem. A distillation column is fed of a benzene–toluene mixture that is benzene. The distillate is benzene and the bottoms is benzene. Find the distillate and bottoms molar flow rates.
Dryer with a bone-dry-solid tie component
Problem. Wet solids enter a dryer at containing water by mass. The dried product contains water. Find the product rate and the water removed.
The accumulation = in − out − consumption ODE for filling, draining, and well-mixed tanks, and the first-order concentration response derived straight from the balance.
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The open-system first law on enthalpy, choosing reference states, sensible and latent heat from heat capacity, and coupling energy to the material balance.
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The transient open-system energy balance for heating and cooling a stirred tank, the thermal time constant, and lumped-capacitance response derived from the ODE.
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Overall versus single-pass conversion, recycle ratio, bypass fraction, purge to limit inert build-up, and choosing the control volume that isolates the unknown.
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The extent of reaction, conversion versus yield versus selectivity, element balances, and complete versus incomplete combustion with excess air and air-fuel ratio.
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Total mass is conserved even with reaction; accumulation and net generation of total mass are zero.
For each species : mass (or mole) of in = out. is the fraction of in stream .
Convert a stream between mass basis (, mass fraction) and mole basis (, mole fraction ) using molar masses .