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A 1 - 2 shell - and - tube heat exchanger is used to cool condensed steam at a rate of 1 0 5 kg

A 1-2 shell-and-tube heat exchanger is used to cool condensed steam at a rate of 105 kg/h from 90 c\deg to 50 c\deg using cooling water available at 10 c\deg The operating conditions do not permit exit temperatures of cooling water exceeding 40^{\circ}C. Select a counter flow heat exchanger with 32 inch OD tube, 16 BWG, triangular pitch and 8 feet long tube arrangement with a tube thickness of 0.083 inch. By referring to the data sheet and with suitable assumptions, Evaluate the following:
(i) Mass flow rate of water;
(ii) Corrected LMTD
(iii) Total number of tubes;
(iv) Tube side Reynolds number;
(v) Inside heat transfer coefficient;
(vi) Shell side Reynolds number
(vii) Shell side heat transfer coefficient;
(viii) Overall heat transfer coefficient;
(ix) Inside heat transfer area
(x) Actual heat transfer area
(xi) Actual design overall heat transfer coefficient
For the missing data or datasheet make assumptions for it here is my assumption
- The specific heat capacity of water is 4.18 kJ/kgK
- The thermal conductivity of the tube material is 16 W/mK (assuming stainless steel)
- The viscosity of water at the average temperature is 0.000653 kg/ms
- The density of water at the average temperature is 995 kg/m^3
- The Prandtl number of water at the average temperature is 5.83
Given data:
- Mass flow rate of condensed steam: 105 kg/h
- Inlet temperature of condensed steam: 90\deg C
- Outlet temperature of condensed steam: 50\deg C
- Inlet temperature of cooling water: 10\deg C
- Maximum outlet temperature of cooling water: 40\deg C
- Tube outer diameter: 3/2 inch (0.0127 m)
- Tube thickness: 0.083 inch (0.00211 m)
- Tube length: 8 feet (2.438 m)
- Tube pitch: triangular
Check if my assumptions suitable and solve according to that

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