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Process Heat Transfer
Project B Page 1
Department of Engineering
Chemical Engineering
Course: Process Heat Transfer Course Code: ENCH3113
Project A: Design of Double Pipe Heat Exchanger
Student Name: ID:
Ability to design the chemical engineering system/component considering the global,
cultural, social and economic factors
Metrics Grades Marks
Design of system using given data
Identifying the constraints and employing it in the design
Evidence of considering health and safety measures related to
the design
Evidence environmental evaluation of design
Total Marks: Out of 15 ( max)
Remarks___________________________________________________________________
___________________________________________________________________________
___________________________________________________________________________
___________________________________________________________________________
___________________________________________________________________________
___________________________________________________________________________
___________________________________________________________________________
___________________________________________________________________________
_________________________________________________________________________
Signature of the Instructor
Process Heat Transfer
Project B Page 2
Design of shell and tube Heat Exchanger
A 1-2 shell-and-tube heat exchanger is used to cool condensed steam at a rate of 105 kg/h
from X ◦C to Y ◦C using cooling water available at Z ◦C. The operating conditions do not
permit exit temperatures of cooling water exceeding 40°C. Select a counter flow heat
exchanger with ¾ 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; 1 mark
(ii) Corrected LMTD 1 mark
(iii)Total number of tubes; 1 mark
(iv)Tube side Reynolds number; 1 mark
(v) Inside heat transfer coefficient; 2 marks
(vi) Shell side Reynolds number 1 mark
(vii)Shell side heat transfer coefficient; 2 marks
(viii)Overall heat transfer coefficient; 2 marks
(ix)Inside heat transfer area 1 mark
(x)Actual heat transfer area 1 mark
(xi)Actual design overall heat transfer
coefficient
2 marks
Total Marks 15 Marks
The contents of the report (typed in A4 paper or neatly written using standard formatting)
i. Present your design with emphasis on identifying the design problem and
constraints
ii. Discuss the health, safety and environmental issues related to the design.
General Instructions
1. This Project is to be submitted by individual student
2. The hard copy of the report should be submitted before the end of 11th
Week, Spring
2024.
Guidelines
Process Heat Transfer
Project B Page 3
1. Report should be typed in A4 sheet; Number of Pages: 3-5
2. Margin 1 inch on all sides
3. Times new roman, 12 Font, 1.5 Spacing
4. Page Numbers to be provided
5. Name of the Table is on Top
6. Name of the Figure at Bottom
Reference Style: AIChE Reference Guidelines
Books
Eckhoff, R. K., “Dust Explosions in the Process Industries,” 3rd ed., Gulf Professional
Publishing, Houston, TX (2003). 2. Rothenberg, G., “Catalysis: Concepts and Green
Applications,” Wiley-VCH, Weinheim, Germany (2008)
Meeting Papers and Presentations/online resources with date of access
Benin, A., et al., “Metal Organic Frameworks (MOFs) for CO2 Capture,” presented at the
2008 AIChE Spring National Meeting, New Orleans, LA (Apr. 7–9, 2008).
Process Heat Transfer
Project B Page 4
No Student Id No. X (Condensed
Steam Inlet)
Y (Condensed
Steam Outlet)
Z (Cooling
Water Inlet)
1 2019298064 110 70 30
2 2019298130 109 69 29
3 2020298005 108 68 28
4 2020298015 107 67 27
5 2020298021 106 66 26
6 2020298042 105 65 25
7 2020298065 104 64 24
8 2020298077 103 63 23
9 2020298080 102 62 22
10 2020298085 101 61 21
11 2020298086 100 60 20
12 2020298089 99 59 19
13 2020298090 98 58 18
14 2020298109 97 57 17
15 2020298115 96 56 16
16 2020298144 95 55 15
17 2020298146 94 54 14
18 2020298158 93 53 13
19 2020298162 92 52 12
20 2020298163 91 51 11
21 2020298173 90 50 10
22 2020298177 89 49 9
23 2020298181 88 48 8
24 2020298184 87 47 7

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Project process heat transfer , design a shell and tube

  • 1. Process Heat Transfer Project B Page 1 Department of Engineering Chemical Engineering Course: Process Heat Transfer Course Code: ENCH3113 Project A: Design of Double Pipe Heat Exchanger Student Name: ID: Ability to design the chemical engineering system/component considering the global, cultural, social and economic factors Metrics Grades Marks Design of system using given data Identifying the constraints and employing it in the design Evidence of considering health and safety measures related to the design Evidence environmental evaluation of design Total Marks: Out of 15 ( max) Remarks___________________________________________________________________ ___________________________________________________________________________ ___________________________________________________________________________ ___________________________________________________________________________ ___________________________________________________________________________ ___________________________________________________________________________ ___________________________________________________________________________ ___________________________________________________________________________ _________________________________________________________________________ Signature of the Instructor
  • 2. Process Heat Transfer Project B Page 2 Design of shell and tube Heat Exchanger A 1-2 shell-and-tube heat exchanger is used to cool condensed steam at a rate of 105 kg/h from X ◦C to Y ◦C using cooling water available at Z ◦C. The operating conditions do not permit exit temperatures of cooling water exceeding 40°C. Select a counter flow heat exchanger with ¾ 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; 1 mark (ii) Corrected LMTD 1 mark (iii)Total number of tubes; 1 mark (iv)Tube side Reynolds number; 1 mark (v) Inside heat transfer coefficient; 2 marks (vi) Shell side Reynolds number 1 mark (vii)Shell side heat transfer coefficient; 2 marks (viii)Overall heat transfer coefficient; 2 marks (ix)Inside heat transfer area 1 mark (x)Actual heat transfer area 1 mark (xi)Actual design overall heat transfer coefficient 2 marks Total Marks 15 Marks The contents of the report (typed in A4 paper or neatly written using standard formatting) i. Present your design with emphasis on identifying the design problem and constraints ii. Discuss the health, safety and environmental issues related to the design. General Instructions 1. This Project is to be submitted by individual student 2. The hard copy of the report should be submitted before the end of 11th Week, Spring 2024. Guidelines
  • 3. Process Heat Transfer Project B Page 3 1. Report should be typed in A4 sheet; Number of Pages: 3-5 2. Margin 1 inch on all sides 3. Times new roman, 12 Font, 1.5 Spacing 4. Page Numbers to be provided 5. Name of the Table is on Top 6. Name of the Figure at Bottom Reference Style: AIChE Reference Guidelines Books Eckhoff, R. K., “Dust Explosions in the Process Industries,” 3rd ed., Gulf Professional Publishing, Houston, TX (2003). 2. Rothenberg, G., “Catalysis: Concepts and Green Applications,” Wiley-VCH, Weinheim, Germany (2008) Meeting Papers and Presentations/online resources with date of access Benin, A., et al., “Metal Organic Frameworks (MOFs) for CO2 Capture,” presented at the 2008 AIChE Spring National Meeting, New Orleans, LA (Apr. 7–9, 2008).
  • 4. Process Heat Transfer Project B Page 4 No Student Id No. X (Condensed Steam Inlet) Y (Condensed Steam Outlet) Z (Cooling Water Inlet) 1 2019298064 110 70 30 2 2019298130 109 69 29 3 2020298005 108 68 28 4 2020298015 107 67 27 5 2020298021 106 66 26 6 2020298042 105 65 25 7 2020298065 104 64 24 8 2020298077 103 63 23 9 2020298080 102 62 22 10 2020298085 101 61 21 11 2020298086 100 60 20 12 2020298089 99 59 19 13 2020298090 98 58 18 14 2020298109 97 57 17 15 2020298115 96 56 16 16 2020298144 95 55 15 17 2020298146 94 54 14 18 2020298158 93 53 13 19 2020298162 92 52 12 20 2020298163 91 51 11 21 2020298173 90 50 10 22 2020298177 89 49 9 23 2020298181 88 48 8 24 2020298184 87 47 7