Multi-Effect Evaporator
Evaporation is carried out in cascade of evaporators. The set-up was invented by Norbert Rillieux which aims to lower the cost of production by utilizing the steam produced per effect and use it to heat the succeeding vessel.
Rillieux Principle:
One pound of steam will evaporate about as many pounds of water as there are effects in series. Hence, a pound of steam will evaporate about 4 pounds of water in a quadruple-effect evaporator.
Over-all Heat Transfer in Series: |
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q = UoA ![]() ![]() ![]() ![]() ![]() ![]() |
q – heat transfer rate![]() Uo – Over-all Heat Transfer Coefficient ![]() Tsn – temperature of the steam ejected at the last effect |
Example 4:
A three-effect evaporator in series with forward feed is to concentrate solution with 7% solute content to 35%.
a. If feed rate is 1000 kg/hr, determine the total amount of vapor produced.
b. What must be the minimum operating pressure in the vapor space of the last effect to enable the operation? Saturated steam passes through the first effect at a temperature of 120 oC. The total boiling point rise along the cascade of evaporators is 50 oC.
Solution:
OMB:
F = 1000 kg/hr
xf = 0.07
xl = 0.35
Ts = 120 oC = 393.15K
BPR = 50 oC = 50 K
OMB:
F = L + VT
1000 = VT + L eq. 1
Solute Balance:
xfF = xlL
0.07(1000) = 0.35L
L = 200 kg/h
Therefore, V = 8000 – 320 = 7680 kg/h
a: Substituting derived values to equation 1:
1000 = VT + 200
VT = 800 kg/hr
b: In order for the heat transfer operation to proceed, the driving force should be greater than zero.
T > 0
Ts – Ts3 – BPR > 0
393.15 – Ts3 – 50 > 0
Ts3 < 343.15K
p of Steam at T = 343.15K: | |
Thermodynamic Properties of Water: 8th Perry’s Handbook, T 2 – 30, p. 2-413 | |
T(K) | p(MPa) |
---|---|
340 | 0.027188 |
350 | 0.041682 |
343.15 | – |
Evaluate the Pressure at T = 343.15 by interpolating. Refer to this example of interpolation.
p = 0.0318 MPa = 0.3138 atm = 238.52 mmHg