Material and Energy Balances: cram pack

Formula sheets, the key method steps for every topic and 8 practice problems, with full solutions at the back.

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1Formulas and methods

Mass balance

Steady state
in = out
Total balance
ṁ1 + ṁ2 = ṁ3
Component balance
ṁ1x1 + ṁ2x2 = ṁ3x3
Evaporator
F·xF = P·xP, W = F − P

Energy balance

Sensible heat
Q = ṁ·cp·ΔT
Latent heat
Q = ṁ·hfg
Mixing
ΣṁcpTin = ΣṁcpTout
Water
cp ≈ 4.18 kJ/(kg·K)

Ideal gas law

Ideal gas law
pV = nRT
Gas constant
R = 8.314 J/(mol·K)
Combined gas law
p1V1/T1 = p2V2/T2
Moles
n = m/M
Temperature
T[K] = T[°C] + 273.15

Stoichiometry

Moles
n = m/M
Concentration
c = n/V
Mole ratio
use the coefficients of the balanced equation
Limiting reactant
the one that runs out first
Percent yield
actual / theoretical × 100%

Method

  1. Write and balance the chemical equation.
  2. Convert the given mass to moles: n = m/M.
  3. Use the coefficients as the mole ratio to find the moles of the substance you want.
  4. Convert back to mass with m = n·M. With two reactants, find the limiting reactant first.

2Practice problems

1.Mass balanceMedium
MixerStream 1850 kg/h · 30% sugarStream 2ṁ₂ = ? · 5% sugarProduct25% sugar

How much of stream 2 must be added each hour to stream 1 so that the blended product contains 25% sugar? Find ṁ2.

ṁ1 = 850 kg/hx1 = 30 %x2 = 5 %x3 = 25 %
ṁ2 = kg/h
2.Mass balanceHard
EvaporatorFeed F1100 kg/h · 15% saltProduct PP = ? · 55%Vapour W (pure water)0% salt

An evaporator concentrates a salt solution by boiling off pure water. Find the product flow P in kg/h.

F = 1100 kg/hxF = 15 %xP = 55 %
P = kg/h
3.Energy balanceMedium
hot sidecold sidelight oil · 130 °C70 °Cwater · 25 °Ct = ? °C

Hot light oil cools water in a counter-flow heat exchanger with no heat loss. Find the water outlet temperature tout.

ṁh = 0.5 kg/scp,h = 2.1 kJ/(kg·K)Th: 130 → 70 °Cṁc = 1 kg/scp,c = 4.18 kJ/(kg·K)tin = 25 °C
tout = °C
4.Energy balanceHard
hot sidecold sidelight oil · 140 °C90 °Cwater · 25 °C40 °C · ṁ = ?10% lost

Hot light oil heats water in an exchanger that loses 10% of the heat released by the hot stream to the surroundings. Find the water flow rate ṁc needed.

ṁh = 2 kg/scp,h = 2.1 kJ/(kg·K)Th: 140 → 90 °Ct: 25 → 40 °Ccp,c = 4.18 kJ/(kg·K)loss = 10 %
ṁc = kg/s
5.Ideal gas lawMedium
80 g of ArP = 700 kPaT = 95 °CV = ?

What volume V does 80 g of Ar occupy at 700 kPa and 95 °C? Treat it as an ideal gas.

m = 80 gM = 39.95 g/molP = 700 kPaT = 95 °CR = 8.314 J/(mol·K)
V = L
6.Ideal gas lawHard
O₂, M = 32 g/molP = 250 kPaT = 170 °Cρ = ?

Find the density ρ of O₂ at 250 kPa and 170 °C, treating it as an ideal gas.

M = 32 g/molP = 250 kPaT = 170 °CR = 8.314 J/(mol·K)
ρ = kg/m³
7.StoichiometryMedium
m(X)n(X)n(H2​O)m(H2​O)÷ M(X)× 2/ν× M(H2​O)

16 g of CH4 and 8 g of O2 react according to CH4 + 2O2 → CO2 + 2H2O. What mass m of H2O can form?

M(CH4) = 16.04M(O2) = 32M(H2O) = 18.02 g/mol
m = g
8.StoichiometryHard
m(N2​)n(N2​)n(NH3​)m(NH3​)÷ M(N2​)× 2/1× M(NH3​)

In the reaction N2 + 3H2 → 2NH3, 10 g of N2 reacts completely (the other reactants are in excess) and 11.06 g of NH3 is collected. Find the percent yield Y.

M(N2) = 28.02 g/molM(NH3) = 17.03 g/molactual: 11.06 g
Y = %

3Solutions

1.Mass balance

Answer: ṁ2 = 212.5 kg/h

Steady-state mass balance: in = out for the total and for each component. Blending problems combine both.

Balances

Total: ṁ3 = ṁ1 + ṁ2
sugar: ṁ1x1 + ṁ2x2 = (ṁ1 + ṁ2)x3

Solve for ṁ2

ṁ2 = ṁ1(x1 − x3)/(x3 − x2) = 850·(30 − 25)/(25 − 5) = 212.5 kg/h

Answer

ṁ2 = 212.5 kg/h
2.Mass balance

Answer: P = 300 kg/h

Tie component: a component that passes through unchanged in one stream (here the solute) links the flows directly. Then the total balance gives the rest.

Solute balance

F·xF = P·xP → P = 1100·15/55 = 300 kg/h

Answer

P = 300 kg/h
3.Energy balance

Answer: tout = 40.07 °C

Exchanger energy balance: with no losses, ṁhcp,h(Th,in − Th,out) = ṁccp,c(tout − tin).

Heat released by the hot stream

Q = 0.5·2.1·(130 − 70) = 63 kW

Heat picked up by the water

tout = tin + Q/(ṁccp,c) = 25 + 63/(1·4.18) = 40.07 °C

Answer

tout = 40.07 °C
4.Energy balance

Answer: ṁc = 3.014 kg/s

Energy balance with losses: heat released = heat absorbed + heat lost.

Heat released

Qh = 2·2.1·(140 − 90) = 210 kW

Heat that reaches the water

Qc = (1 − 0.1)·210 = 189 kW

Water flow rate

ṁc = Qc/(cp,c·Δt) = 189/(4.18·15) = 3.014 kg/s

Answer

ṁc = 3.014 kg/s
5.Ideal gas law

Answer: V = 8.756 L

Ideal gas law: PV = nRT, with n = m/M.

Moles

n = 80/39.95 = 2.003 mol
T = 95 + 273.15 = 368.1 K

Volume

V = nRT/P = 2.003·8.314·368.1/700 = 8.756 L

Answer

V = 8.756 L
6.Ideal gas law

Answer: ρ = 2.171 kg/m³

Ideal gas density: ρ = PM/(RT).

Rearrange the gas law

PV = (m/M)RT → ρ = m/V = PM/(RT)
T = 170 + 273.15 = 443.1 K

Density

ρ = 250·32/(8.314·443.1) = 2.171 kg/m³

Answer

ρ = 2.171 kg/m³
7.Stoichiometry

Answer: m = 4.505 g

Stoichiometry: a balanced equation counts particles, not grams. Convert mass to moles with n = m/M, use the coefficients of the equation as the mole ratio, then convert back with m = n·M. With two reactants, the limiting reactant is the one that runs out first and fixes how much product forms.

Moles of each reactant

n(CH4) = 16/16.04 = 0.9975 mol
n(O2) = 8/32 = 0.25 mol

Limiting reactant

0.9975/1 = 0.9975, 0.25/2 = 0.125 → O2

Mass of product

n(H2O) = 0.125·2 = 0.25 mol
m = 0.25·18.02 = 4.505 g

Answer

m = 4.505 g
8.Stoichiometry

Answer: Y = 90.99 %

Stoichiometry: a balanced equation counts particles, not grams. Convert mass to moles with n = m/M, use the coefficients of the equation as the mole ratio, then convert back with m = n·M. With two reactants, the limiting reactant is the one that runs out first and fixes how much product forms.

Theoretical yield

n(N2) = 10/28.02 = 0.3569 mol
m = 0.3569·2/1·17.03 = 12.16 g

Percent yield

Y = 11.06/12.16·100 = 90.99%

Answer

Y = 90.99%

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