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Heat transfer and thermal systems

Adiabatic mixing temperature of two streams

Temperature after steady adiabatic mixing of two streams of heat-capacity rates C = ṁcp (W/K).

Ref
HTS-47
Rev
v1
Field
Heat transfer and thermal systems
Result
Tout [K]

The temperature after steady adiabatic mixing of two streams is the heat-capacity-rate-weighted average, Tout = (C₁T₁ + C₂T₂)/(C₁ + C₂), with C = ṁcp. It follows from an energy balance with constant cp, and it assumes no heat loss, reaction, phase change or enthalpy of mixing. The stream with the larger heat-capacity rate dominates.

Temperature after steady adiabatic mixing of two streams of heat-capacity rates C = ṁcp (W/K). Assumes constant cp, no heat loss, reaction, phase change or enthalpy of mixing.

Calculator

Solve for
K
W/K
1100,000
K
2501,000
W/K
1100,000
K
2501,000
  • Total heat-capacity rate, C₁ + C₂600 W/K
  • Heat gained by stream 2, C₂(Tout − T₂)8,000 W
  • Weight of stream 1, C₁/(C₁ + C₂)0.3333

What drives the result

Each variable is moved across its typical range while the others stay at the values above. The longest bar is the key driver.

Mixed temperature (K) current value 320 K
T2Temperature of stream 2Key driver
287787
T1Temperature of stream 1
283533
C1Heat-capacity rate of stream 1
300360
C2Heat-capacity rate of stream 2
300360
  • The two streams leave mixed at 320 K, 33.3 % of the way from stream 2 to stream 1.
  • Stream 2 gains 8,000 W, exactly what stream 1 loses, which confirms the energy balance.
Chart data as tables

Ranked variables

VariableTypical rangeLowest resultHighest resultSwing (K)Local stepChange in result
T2 Temperature of stream 2250 to 1,000 K286.7786.7500+10%+6.25 %
T1 Temperature of stream 1250 to 1,000 K283.3533.3250+10%+3.75 %
C1 Heat-capacity rate of stream 11 to 100,000 W/K300.1359.859.61+10%+0.403 %
C2 Heat-capacity rate of stream 21 to 100,000 W/K300.1359.759.58+10%−0.391 %

Sweep of Heat-capacity rate of stream 2

Heat-capacity rate of stream 2 (W/K)Mixed temperature (K)
1359.7
4.217358.8
17.78355.1
74.99343.6
316.2323.2
1,334307.8
5,623302.1
23,710300.5
100,000300.1

Sweep one variable

Mixed temperature (K)Hover, touch, or use the arrow keys on the chart
300310320330340350360 110100100010k100k Heat-capacity rate of stream 2 (W/K), log scale now 320

Variables and how each one contributes

Tout

Mixed temperature

Result · K

What the equation gives you. Everything else feeds it.

C1

Heat-capacity rate of stream 1

W/K · typical 1 to 100,000

The heat-capacity rate ṁcp of stream 1, in W/K. A larger rate pulls the result towards T₁. Raising it by 10 % (to 220) moves the result by +0.403 %, from 320 to 321.3 K.

T1

Temperature of stream 1

K · typical 250 to 1,000

The temperature of stream 1, in K. Raises the mixed temperature in proportion to its weight. Raising it by 10 % (to 396) moves the result by +3.75 %, from 320 to 332 K.

C2

Heat-capacity rate of stream 2

W/K · typical 1 to 100,000

The heat-capacity rate ṁcp of stream 2, in W/K. A larger rate pulls the result towards T₂. Raising it by 10 % (to 440) moves the result by −0.391 %, from 320 to 318.8 K.

T2

Temperature of stream 2

K · typical 250 to 1,000

The temperature of stream 2, in K. Raises the mixed temperature in proportion to its weight. Raising it by 10 % (to 330) moves the result by +6.25 %, from 320 to 340 K.

Worked example with the values above

  1. Weighted sum: C₁T₁ + C₂T₂ = 200 × 360 + 400 × 300 = 192,000 W.
  2. Total: C₁ + C₂ = 600 W/K.
  3. Tout = 192,000 / 600 = 320 K.

Assumptions and limits

  • Constant properties in each phase, a single melting temperature and no losses unless stated.
  • Steady or quasi-steady balances, with absolute temperatures where logarithms or powers are used.

Common mistakes

  • Forgetting the latent heat term, or counting it twice.
  • Using °C in an entropy or radiation formula.
  • Using these simple formulas when the Stefan number is not small.

Statistics and uncertainty

Latent heats and specific heats are tabulated to a few per cent, but real storage materials melt over a range and lose heat, so real systems typically deliver 5 % to 20 % less than the ideal values.

Where it is used

  • Sizing thermal storage, ice banks and phase-change units.
  • Checking exchanger data, mixing streams and cooling times.

Maths you need

  • Latent heat: energy per kilogram to change phase
  • Heat-capacity rate: C = ṁcp
  • Second law: entropy generation cannot be negative

Related formulas

Practise this formula