Question: For the problem given with minimum approach temperature difference, Amin = 10 C, carry out the Energy Integration Analysis using Pinch Technology by determining the

For the problem given with minimum approach temperature difference, Amin = 10 C, carry out the Energy Integration Analysis using Pinch Technology by determining the following:

(a) Net amount of heat available in the streams based on I law

(b)Shift of temperature scales with net heat in respective intervals.

(c)Construction of cascade diagram

(d)Pinch temperature and minimum hot & cold utility requirement.

(e)Number of heat exchangers based on I law analysis.

(f)Number of heat exchangers based on Il law analysis.

(g)Hot end design.

(h)Cold end design.

Heat exchanger network for the (I)maximum energy recovery (MER).

Stream

Condition

Hot

Cold

FC.

Source

(kW/AC) (W/m? C) Temperature (C)

0.4

120

0.55

160

0.75

0.65

Target

Temperature (C)

100

115

Assume the supply temperature of hot & cold utility are 300 C and 15 C respectively. Heat transfer coefficient of hot utility and kW/m2 C.

For the problem given with minimum approach temperature difference, Amin =

10 C, carry out the Energy Integration Analysis using Pinch Technology by

For the problem given with minimum approach temperature difference, Tmo=10C, canty out the Energy thtegration Analysis usma, Pinco Technology by detemining the followng (a) Net amount of heat available in the streams based on I law (b) Shin of temperature scales with net heat in respective intervals: (c) Construction of cascade diagram (d) Pinch temperature and minimum hot & cold utility requirement. (e) Number of heat exchangers based on 1 law analysis. (f) Number of heat exchangers based on It law analysis. (g) Hot end design. (h) Cold end design (i) Heat exchanger network for the maximum energy recovery (MER). Assume the supply temperature of hot \& cold utility are 300C and 15C respectively Heat transfer coefficient of hot utiity and kW/m2C. [20] For the problem given with minimum approach temperature difference, Tmo=10C, canty out the Energy thtegration Analysis usma, Pinco Technology by detemining the followng (a) Net amount of heat available in the streams based on I law (b) Shin of temperature scales with net heat in respective intervals: (c) Construction of cascade diagram (d) Pinch temperature and minimum hot & cold utility requirement. (e) Number of heat exchangers based on 1 law analysis. (f) Number of heat exchangers based on It law analysis. (g) Hot end design. (h) Cold end design (i) Heat exchanger network for the maximum energy recovery (MER). Assume the supply temperature of hot \& cold utility are 300C and 15C respectively Heat transfer coefficient of hot utiity and kW/m2C. [20]

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