A tomato-juice evaporator takes in juice at the rate of 1200 kg/h. If the concentrated juice contains 35% of solids and the hourly rate of removal of water is 960 kg, (a) calculate the moisture content of the original juice, (b) the quantity of steam needed per hour for heating if the evaporator works at a pressure of 25 kPa. Assume no heat losses. Assume saturated steam at 50% quality is used to heat the evaporator at a temperature of 125 oC. Condensate exits at 125 oC.
A tomato-juice evaporator takes in juice at the rate of 1200 kg/h. If the concentrated juice...
3-9. 10,000 kg / h of a 20% NaOH solution are treated in a simple evaporator and must be concentrated to 50% by weight. The steam used as the heating medium is saturated steam at 4 at overpressure. An absolute pressure of 150 mm Hg is maintained in the evaporation chamber. The integral coefficient of heat transmission is 2,500 Kcal / m2.h.C. If the supply enters the evaporator at 20 ° C, calculate: a) The heating surface. b) The hourly...
Tomato juice having a concentration of 12 wt% solids is being concentrated to 25% solids in a film-type evaporator. The maximum allowable temperature for the tomatojuice is 135 °F, which will be the temperature of the product. The feed enters at 100 °F. Saturated steam at 25 psia is used for heating. The overall heat-transfercoefficient U is 600 btu/h·ft2·°F and the area A is 50 ft2. The heat capacity of the feed cP is estimated as 0.95 btu/lbm·°F. Neglect any...
Please help with this question regarding the design of a
forward-feed double effect evaporator. Will really appreciate
it.
(I've edited by typing out the questions, so the question is now
clearer.)
Please provide a proposal for the design of a forward-feed
double effect evaporator (Figure 1), for which operating conditions
are given below.
Figure 1: Schematic diagram of forward-feed
double effect evaporator
Configuration: Forward-feed double effect evaporator
Number of effects: 2
Feed:
Feed material: Aqueous high molecular weight solution
Flow...
Please help with this question regarding the design of a
forward-feed double effect evaporator. Will really appreciate
it.
(I've edited by typing out the questions, so the question is now
clearer.)
Please provide a proposal for the design of a forward-feed
double effect evaporator (Figure 1), for which operating conditions
are given below.
Figure 1: Schematic diagram of forward-feed
double effect evaporator
Configuration: Forward-feed double effect evaporator
Number of effects: 2
Feed:
Feed material: Aqueous high molecular weight solution
Flow...
1. There are several evaporators, including agitated film evaporator, long-tube evaporator, short-tube evaporator, and horizontal-tube evaporator. For (a) juice and (b) paste, suggest proper evaporator and explain why you select it. 2. A double-effect forward-feed evaporator is used to evaporate a sugar solution containing Swt solids to a concentrated solution of 25 wt%. The boiling-point rise (BPR) of the solution (independent of pressure) can be estimated from BPRC-1.5x + 6x", where x is wt% of sugar in solution. Saturation steam...
Separation Process Problem 1 [30 marks] A double-effect forward-feed evaporator is used to concentrate a 5 wt% aqueous NaCl solution to a final concentration of 25 wt% The feed enters the first effect at a temperature of 40°C. Saturated steam at a pressure of 2 bar (absolute) is fed to the first effect at a rate of 1500 kg/h, and the vapour from this effect is used to supply heat to the second effect. The overall heat transfer coefficient in...
Q1
a) Company A designed a heat pump to
supply heat into a library in Canada during
winter, so that the library can maintain to be at 20°C. The heat
pump utilizes
12,000 L/min of Refrigerant-134a as the working fluid and absorb
heat from an
industrial water stream. The water stream enters the evaporator at
50°C and exits
at 25°C. The refrigerant enters the evaporator at 10°C with 90%
moisture content
and leaves at 20°C. There is no pressure drop in...
1. Exhaust gas at 400 C and 1 bar from i engines flows at the rate of 125 mol s into a waste-heat boiler where saturated steam in generated at a pressure of 1200 kPa. Water enters the boiler at 20 C (Ta) and the exhaust gases are cooled to within 10°C of the steam temperature. The heat capacity of the exhaust gases is C/R-3.341.12x10 T/K. The steam flows into an adiabatic turbine and exhausts at a pressure of 25...