Evaporation of Sugar Solution in a Multiple-Effect Evaporator. A triple-effect evaporator with forward feed is...
Please could you answer all sub questions. A forward feed triple - effect evaporator is required to concentrate a 10% pineapple juice mixture from 5 to 70% using steam at 200 kN/m2 (gauge). The feed enters at 2 000 kg/hr at 303 K and the first effect is operated at 105 kN/m2 (gauge). Additional information: 1. The BPR's can be estimated from the following equation: BPR (°C) = 1,78 X + 6,22 X2: 2. The heat capacity of the solution...
Boiling Points in a Triple-Effect Evaporator. A solution with a negligible boiling- point rise is being evaporated in a triple-effect evaporator using saturated steam at 121.1°C (394.3 K). The pressure in the vapor of the last effect is 25.6 kPa abs. The heat-transfer coefficients are U1 = 2840, U2 = 1988, and U3 = 1420 W/m² · K, the areas are equal. Estimate the boiling point in each of the evaporators. Ans. T1 = 108.6°C (381.8 K)
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...
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...
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...
Q1. A double-effect evaporator is being used (in forward mode) to concentrate a sodium chloride solution from 4 to 20 weight %. The solution enters the first effect at 298K at a rate of 3000 kg/h, and saturated steam at a pressure of 1.5 bars is fed into a tube bundle in the Ist effect. The steam condenses at 1.5 bars and the condensate is withdrawn at the saturation temperature corresponding to this pressure. The pressure at the second effect...