SlideShare a Scribd company logo
Tagliatela College of Engineering
EASC1112 – Methods of Engineering Analysis
TO: EASC 1112 Students
FROM: EASC1112 Instructor
Subject: Project 2, Optimum Pipe Insulation
A long pipe is to be installed to transport steam from a boiler to
another part of the plant. Insulation is needed on the pipe for
both safety and economic reasons. You are to develop a
spreadsheet to calculate the surface temperature of the insulated
pipe and to model the heat loss to the surrounding air as a
function of the thickness of insulation on the outside of the
pipe. Your model should allow for variation in the key
parameters to explore the effect of various changes. Using data
generated by your model, select the best insulation thickness to
maximize the present value of net savings in comparison to an
un-insulated pipe. Provide appropriate plots and data tables to
support your decision and to show the financial penalty for
using a different insulation thickness.
Heat Loss Calculation
The steam pipe is to be made from schedule 40 steel with a
diameter in the range of 2 to 3.5 inches (nominal pipe size).
The pipe will be encased in fiberglass insulation with an
aluminum sheet cladding to protect from weather. Heat loss
for this case can be modeled using a combination of convection
and conduction heat transfer rate equations. Heat from the
steam is transferred to the inside wall of the pipe by forced
convection, then through each of three layers by conduction
(pipe wall, insulation, cladding) and finally from the outside of
the cladding to the surrounding air by natural convection. The
governing equations are shown below to calculate heat
transferred per unit length of pipe:
View of pipe looking along axis
QS = rate of heat lost by steam to inside pipe wall
Aluminum Cladding
Q1, Q2, Q3 = rates of heat transferred through pipe wall,
insulation, aluminum cladding, respectively
r2
r1
r4
r3
Fiberglass Insulation
Steel Pipe
STEAM
QA=rate of heat lost to air
The heat transfer rate equations include constants for the
thermal conductivity of the materials and heat transfer
coefficients for the convective situations. Values for these will
be fixed for the analysis.
The temperatures of the steam and the air will be fixed values,
but the temperatures at each surface will be dependent on the
thickness of insulation and size of the pipe. The subscripts used
for the temperatures correspond to radial distances from the
center of the pipe. The radii values will be fixed for a
particular case of pipe size and insulation thickness, but will be
varied as part of the optimization work. The intermediate
temperatures, to be found by simultaneous solution of the
equation set, are:
T1 = temperature of the inside wall of the pipe, at distance r1
from the pipe center axis
T2 = temperature of the outside pipe wall and the inside of the
insulation, distance r2
T3=temperature of the outside of the insulation and inside of
the aluminum cladding, distance r3
T4 = temperature of the outside surface of the cladding, exposed
to the air, at distance r4
Average steady-state conditions will be used for the analysis of
each case, thus the rate of heat lost from the steam must equal
the rate of heat transferred through each layer and ultimately
the rate of heat lost from the outside cladding to the air. Thus
four linear equations can be obtained by setting QA = Q1,
Q1=Q2, etc. The resulting equations can be solved using matrix
techniques to find the unknown temperatures. Any one of the
heat rate equations can then be used to find the heat loss rate.
The constants (h's , k's, π and numbers) and the parameters
(radii values) become the coefficients, and are shown in the
equations above as C1 through C4. For a given case, these will
be easily calculated. Terms containing the steam and air
temperature are also constants (shift to the right side of
equation). For example, setting QS = Q1 and Q1 = Q2 results
in the following:
Similar equations result from setting Q2 = Q3 and Q3 = QA.
Your spreadsheet should have a data section for setting the pipe
diameter and insulation thickness along with values for the
constants, such as steam and air temperatures, thermal
conductivity values, cost information, etc. Develop the model
such that entry of a pipe diameter and an insulation thickness
results in determination of the 4 temperatures and the rate of
heat loss for the full pipe length.
Analysis of Insulation Thickness
Using your model, determine the optimum insulation thickness
for different pipe diameters to achieve a maximum net present
value of savings. Savings here is defined as the dollar value of
energy NOT lost as a result of the insulation. To calculate this
you must first determine the heat that would be lost if the pipe
was not insulated. Simply subtract the heat loss for a particular
insulation thickness from the bare pipe heat loss to determine
the energy savings. The cost to insulate the pipe includes both
the material cost and the installation labor. A net installed cost
is found by multiplying the material cost by an installation
factor to account for labor and other installation expenses. Data
is provided at the end of this memo for physical properties, cost
information etc.
Optimization work requires an objective to be maximized or
minimized. In this project the "objective function" is the
present value of savings over a 5 year period using a specific
interest rate with monthly compounding. The installed cost of
insulating the pipe occurs at time zero (present) and is negative,
so this is subtracted from the present value of 5 years of
savings. Varying the insulation thickness will affect this value,
so you can determine if there is an optimum which maximizes
the present value. You should also be aware of safety concerns
associated with a long run of steam pipe. In particular you
should assure that the outside surface temperature is no higher
than 50oC.
Report Requirements
At present, the diameter of the steam pipe has not determined,
but it will be between 2 and 3 ½ inch schedule 40 steel pipe.
Dimensions for standard steel pipe are available in the literature
and should be used in this project. After creating the
spreadsheet model, you should run simulations for cases in
which you vary the insulation thickness from 0.1 to 6.0 cm.
Prepare plots showing surface temperature, installed cost,
annual savings and net present value as a function of insulation
thickness. Create other plots as you deem necessary to justify
your design decisions regarding the insulation thickness. A full
analysis of this type should be performed for one pipe diameter.
In addition, you should determine the optimum thickness and
required thickness to achieve an acceptable surface temperature
for all pipe sizes in the range given above. Note that nominal
pipe sizes in this range are incremented in ½ inch steps. For
each pipe size, recommend an insulation thickness.
Your memo should give an overview of the project, discuss your
approach, present results and discuss methods used and
assumptions made. Tables and plots should appear in the memo
to with explanation to make your points. Your concluding
paragraph should include a discussion of what you learned in
doing the project. Your spreadsheet should, of course, be well-
documented and well-organized to show clearly how the work
was done. The spreadsheet should include the following
features:
· List of pipe diameters using the data validation methods
· Retrieval of dimensions for pipes from a table keyed to the
selected pipe size (use Vlookup)
· Scroll bar to set the insulation thickness
· Key results copied to tables, with accompanying graphs for
key results
· Use Solver to vary thickness to maximize present value of net
savings
· Any additional functional features you wish to include to
make the simulation tool more useful
The project is due per your instructors directions, with a paper
submission of the memo and attached printout of the
spreadsheet. The spreadsheet should also be submitted via
Blackboard. Required data is found on the next page.
Input data for use in project
Properties of pipe, insulation and outer cladding material
Financial Analysis Parameters
Item
Material
k, thermal conductivity
density
cost
*Install Factor
Energy cost
Annual Interest Rate
Period of analysis
W/m-C
kg/m3
$/kg
$/$
$/kWh
percent
years
Pipe
steel
43
7800
NA
5
$0.04
3.0%
5
insulation
fiber glass
0.055
64.1
30
Per month
months
Outer Layer
aluminum
206
2700
40
0.25%
60
0.5 mm thick
* Installed cost = (total material cost) x installation factor
Heat Transfer Coefficients W
m2-oC
Other Parameters
From steam to inside pipe wall
From outside pipe cladding to air
Steam Temperature
Air Temperature
Pipe Length
hS
hA
C
C
Meter
50
5
150
10
50
Properties of Standard Steel Pipe
Schedule 40
Pipe Diameters
Wall thickness
Pipe
OD, cm
ID, cm
cm
2
6.033
5.25
o.39
2.5
7.303
6.271
0.52
3
8.89
7.792
0.55
3.5
10.16
9.012
0.57
r1
r1
(
)
(
)
(
)
(
)
(
)
(
)
(
)
(
)
(
)
0
C
:
Solution
Matrix
for
Rearranged
Flow
Heat
State
-
Steady
3
3
2
3
2
1
2
3
2
3
2
1
2
2
1
1
2
2
1
2
1
2
1
2
1
1
1
=
+
-
-
+
-
=
-
=
=
-
+
+
-
=
-
=
T
C
T
C
C
T
C
T
T
C
T
T
C
Q
Q
T
C
T
C
T
C
T
T
C
T
T
C
Q
Q
S
S
S
(
)
(
)
(
)
(
)
(
)
(
)
(
)
(
)
(
)
(
)
(
)
(
)
(
)
(
)
(
)
(
)
(
)
(
)
A
A
a
A
s
s
s
S
T
T
C
T
T
r
h
Q
T
T
C
r
r
T
T
k
Q
T
T
C
r
r
T
T
k
Q
T
T
C
r
r
T
T
k
Q
T
T
C
T
T
r
h
Q
-
=
-
=
-
=
-
=
-
=
-
=
-
=
-
=
-
=
-
=
4
5
4
4
4
3
4
3
4
4
3
3
3
3
2
3
2
3
3
2
2
2
2
1
2
1
2
2
1
1
1
1
1
1
1
2
ln
2
ln
2
ln
2
2
pipe
steam
of
length
meter
per
-
Layer
Each
for
Rate
Transfer
Heat
p
p
p
p
p
Alaboudi 1
UNIVERSITY OF NEW HAVEN
Tagliatela College of Engineering
TO: Professor
FROM: Abdullah Alaboudi
November 10, 2016
EASC 1112 Project 2: Optimum Pipe Insulation
Summery:
A team contains three students were tasked to design and
develop a spreadsheet to calculate the surface temperature of
the installed pipe. The team needs to concern the heat loss from
the steam transported through a pipe from a boiler to another
part of the plant. The team’s aim was to determined the best
insulation thickness and pipe size to maximized the value of net
saving and camper with the un-insulated pipe to find the
financial penalty by using different insulation thickness. The
present value cost was to be operated for five years. The team
decided to pick the 2.5 pipe size as the best choice
economically, and it terms of energy loss.
Challenges:
1. Set up the equations.
2. Conflict schedules between team members.
3. Excel deleted some of the work, and it cost more time to
re-do it.
Discussion:
The issue was to figure the heat loss (Q), the radius in each
layer, (R), temperatures (T), and the (C’s). The first thing the
team has done was rearranging the given equations to solve by
using matrix. After that, the team solves for the heat loss since
the team found the temperatures by the inverse of the
coefficient. To begin, the properties of pipe and the material
were sorted out, including the thickness of each layer. In this
data chart, the costs of every material, steel, protection, and
aluminum, were set by taking the mass, material cost, and
establishment expense (Appendix I). The following step was to
focus on the different parameters and the inverse of
coefficients. For instance, the temperature of the air, steam, and
the length of the funnel (Appendix II). The budgetary
parameters and the financial analysis were sorted to be the
vitality expense and the interest rate from month to month or
year to year. (Appendix III). Moreover, the properties of a
standard steel pipe including the pipe size, outside, inside
dimeter and well thickness, which involve finding the different
temperature (Appendix IV). After solving for the various
temperatures by using taking the coefficient and solve using
matrix (Appendix V) and (Appendix VI). The team had to do the
same method to solve with out insulation by doing the same
methods (Appendix VII). The Q’s comparisons for networks
were utilized to find the temperature for each thickness forms
the protected pipe. To calculate the radiuses and convert to be
cm by using offset equation (Appendix VIII) The team used the
annual saving, cost, heat loss, and the present value of a Y and
the insulation thickness as an X to show the changes as the
insulation thickness changes (Appendix XI) (Appendix XII)
(Appendix XIII) (Appendix XIV). By using Solver, the team
was able to identify the best insulation thickness in each pipe
(Appendix XV).
Conclusion:
Project 2 in EASC 1112 course, was a very enjoyable project,
and made the team think in terms of saving energy and money
as well by using the given methods. Each member of the team
contributed and did their best to get the work done nicely and
accurately. For the final result, the team identified that pipe 2.5
with 3.57 insulation thickness was the best choice for the pipe
to be installed.
Appendices:
Appendix I: Properties of pipe, insulation and outer cladding
material
Appendix II: Heat Transfer Coefficients and Other Parameters
Chart.
Appendix III: Financial Analysis Parameters Chart
Appendix IV: properties of stander steel Pipe.
Appendix V: Matrix of Temperatures Chart
Appendix VI: Matrix Q with Insulation Chart
Appendix VII: Matrix Q without Insulation Chart
Appendix VIII: Pipe size and the radius
Appendix IX: Off sit equation for Pipe size
Appendix X: Off sit equation for insulation thickness
Appendix XI: Surface Temperature versus Insulation Thickness
Graph
Appendix XII: Annual Savings versus Insulation Thickness
Graph
Appendix XIII: Installed Cost versus Insulation Thickness
Graph
Appendix XIV: Present Value versus Insulation Thickness
Graph
Appendix XV: Best insulation thickness of each pipe.
Appendix I: Properties of pipe, insulation and outer cladding
material
Appendix II: Heat Transfer Coefficients and Other Parameters
Chart.
Appendix III: Financial Analysis Parameters Chart
Appendix IV: properties of stander steel Pipe
Appendix V: Matrix of Temperatures Chart
Appendix VI: Matrix Q with Insulation Chart
Appendix VII: Matrix Q without Insulation Chart.
Appendix VIII: Pipe size and the radius.
The team uses the Offset equation to make the pipe size and
insulation thickness changeable as a shortcut. Offset equation is
shown in the pictures shown below.
Appendix IX: Off sit equation for Pipe size
Appendix X: Off sit equation for insulation thickness
Appendix XI: Surface Temperature versus Insulation Thickness
Graph
Appendix XII: Annual Savings versus Insulation Thickness
Graph
Appendix XIII: Installed Cost versus Insulation Thickness
Graph
Appendix XIV: Present Value versus Insulation Thickness
Graph
Appendix XV: Best insulation thickness of each pipe.
The picture displayed below shows a chart with calculation.
The picture displayed below shows the 5 years’ payment.

More Related Content

PPTX
Computer Simulation of a Heat Exchanger using Aspen
PDF
A Thesis on Design Optimization of Heat Sink in Power Electronics
PDF
Comparative CFD Analysis of Shell and Serpentine Tube Heat Exchanger
PDF
IRJET- Thermal Analysis on Solar Air Heater Duct
PDF
REPORT-MSD
PDF
Thermal Performance Analysis for Optimal Passive Cooling Heat Sink Design
DOCX
Experimentation on heat pipe and cfd analysis for performance enhancement
DOCX
Experimentation on heat pipe and cfd analysis for performance enhancement
Computer Simulation of a Heat Exchanger using Aspen
A Thesis on Design Optimization of Heat Sink in Power Electronics
Comparative CFD Analysis of Shell and Serpentine Tube Heat Exchanger
IRJET- Thermal Analysis on Solar Air Heater Duct
REPORT-MSD
Thermal Performance Analysis for Optimal Passive Cooling Heat Sink Design
Experimentation on heat pipe and cfd analysis for performance enhancement
Experimentation on heat pipe and cfd analysis for performance enhancement

Similar to Tagliatela College of EngineeringEASC1112 – Methods of Engineeri.docx (20)

PDF
Advanced CFD_Numerical_Analysis
PDF
Heat pipe with fins thermal analysis
PDF
Analysis of Double Pipe Heat Exchanger With Helical Fins
PDF
ECONOMIC INSULATION FOR INDUSTRIAL PIPING
PDF
Current Heat Pipe Technology
PDF
Portfolio Po-Chun Kang
PDF
IRJET- Experimental Analysis of Circular Perforated Fin Arrays by Forced Conv...
PDF
Review Paper on Experimental Analysis of Vortex Tube
PDF
Insulation and Refractories
PDF
Piping heat loss
PDF
Piping heat loss
PDF
Ijmet 06 07_006
PDF
EVALUATION OF ENERGY LOSS IN GEOTHERMAL PIPING SYSTEM [IIGCE 2016] (Repaired)
PDF
Experimental Investigation of Natural Convection Heat Transfer Enhancement fr...
PDF
Numerical Analysis of Inverted Notched Fin Array Using Natural Convection
PDF
IRJET- Study of Heat Transfer Characteristics for the Flow of Air over a Heat...
PDF
28-shaw_presentation.ashx
PPTX
Thermal chapter 4 (2).pptx for chemical engineering student
PDF
PRACTICAL ISSUES ASSOICATED WITH THE USE OF INFRARED THERMOGRAPHY FOR DETECTI...
PDF
Encit2018
Advanced CFD_Numerical_Analysis
Heat pipe with fins thermal analysis
Analysis of Double Pipe Heat Exchanger With Helical Fins
ECONOMIC INSULATION FOR INDUSTRIAL PIPING
Current Heat Pipe Technology
Portfolio Po-Chun Kang
IRJET- Experimental Analysis of Circular Perforated Fin Arrays by Forced Conv...
Review Paper on Experimental Analysis of Vortex Tube
Insulation and Refractories
Piping heat loss
Piping heat loss
Ijmet 06 07_006
EVALUATION OF ENERGY LOSS IN GEOTHERMAL PIPING SYSTEM [IIGCE 2016] (Repaired)
Experimental Investigation of Natural Convection Heat Transfer Enhancement fr...
Numerical Analysis of Inverted Notched Fin Array Using Natural Convection
IRJET- Study of Heat Transfer Characteristics for the Flow of Air over a Heat...
28-shaw_presentation.ashx
Thermal chapter 4 (2).pptx for chemical engineering student
PRACTICAL ISSUES ASSOICATED WITH THE USE OF INFRARED THERMOGRAPHY FOR DETECTI...
Encit2018
Ad

More from ssuserf9c51d (20)

DOCX
Muslims in the Golden Age is the theme for the research project. You.docx
DOCX
Multiple Sources of MediaExamine the impact of multiple sour.docx
DOCX
Multicultural Event WrittenPlease choose and research a cult.docx
DOCX
Multi-Party NegotiationFor this Essay, you will explore the co.docx
DOCX
Music has long been used by movements seeking social change.  In the.docx
DOCX
MSW Advanced Clinical Concentration -Student Learning AgreementW.docx
DOCX
Multimedia Instructional MaterialsStaying current on technolog.docx
DOCX
Murray Bowen is one of the most respected family theorists in th.docx
DOCX
Mrs. Thomas is a 54, year old African American widow, mother and gra.docx
DOCX
Multiple Source Essay, Speculating about CausesProposing a Solution.docx
DOCX
Multiyear Plans Please respond to the followingDo you.docx
DOCX
Multinational Financial ManagementDetermine key reasons wh.docx
DOCX
Murder CasePreambleAn organization system administrator .docx
DOCX
Multimodal Personal Narrative – Develop a multimodal document to bot.docx
DOCX
Multigenre ProjectEN101O Fall 2019 Dr. WalterA Multigenre Pr.docx
DOCX
Multimedia activity Business OrganizationVisit the Choose Your .docx
DOCX
Multicultural PerspectiveToday’s classrooms are diverse and .docx
DOCX
Muhammad Ali, how did his refusal to go into the army affect his.docx
DOCX
MS 113 Some key concepts that you need to know to navigate th.docx
DOCX
Much has been made of the new Web 2.0 phenomenon, including social n.docx
Muslims in the Golden Age is the theme for the research project. You.docx
Multiple Sources of MediaExamine the impact of multiple sour.docx
Multicultural Event WrittenPlease choose and research a cult.docx
Multi-Party NegotiationFor this Essay, you will explore the co.docx
Music has long been used by movements seeking social change.  In the.docx
MSW Advanced Clinical Concentration -Student Learning AgreementW.docx
Multimedia Instructional MaterialsStaying current on technolog.docx
Murray Bowen is one of the most respected family theorists in th.docx
Mrs. Thomas is a 54, year old African American widow, mother and gra.docx
Multiple Source Essay, Speculating about CausesProposing a Solution.docx
Multiyear Plans Please respond to the followingDo you.docx
Multinational Financial ManagementDetermine key reasons wh.docx
Murder CasePreambleAn organization system administrator .docx
Multimodal Personal Narrative – Develop a multimodal document to bot.docx
Multigenre ProjectEN101O Fall 2019 Dr. WalterA Multigenre Pr.docx
Multimedia activity Business OrganizationVisit the Choose Your .docx
Multicultural PerspectiveToday’s classrooms are diverse and .docx
Muhammad Ali, how did his refusal to go into the army affect his.docx
MS 113 Some key concepts that you need to know to navigate th.docx
Much has been made of the new Web 2.0 phenomenon, including social n.docx
Ad

Recently uploaded (20)

PDF
FORM 1 BIOLOGY MIND MAPS and their schemes
PDF
Trump Administration's workforce development strategy
PDF
MBA _Common_ 2nd year Syllabus _2021-22_.pdf
PDF
احياء السادس العلمي - الفصل الثالث (التكاثر) منهج متميزين/كلية بغداد/موهوبين
PDF
Τίμαιος είναι φιλοσοφικός διάλογος του Πλάτωνα
PPTX
Share_Module_2_Power_conflict_and_negotiation.pptx
PDF
Computing-Curriculum for Schools in Ghana
PDF
AI-driven educational solutions for real-life interventions in the Philippine...
PDF
Paper A Mock Exam 9_ Attempt review.pdf.
PDF
advance database management system book.pdf
PPTX
History, Philosophy and sociology of education (1).pptx
PPTX
20th Century Theater, Methods, History.pptx
PDF
Chinmaya Tiranga quiz Grand Finale.pdf
PPTX
Introduction to pro and eukaryotes and differences.pptx
PDF
Hazard Identification & Risk Assessment .pdf
PDF
Empowerment Technology for Senior High School Guide
PPTX
A powerpoint presentation on the Revised K-10 Science Shaping Paper
PPTX
202450812 BayCHI UCSC-SV 20250812 v17.pptx
PPTX
ELIAS-SEZIURE AND EPilepsy semmioan session.pptx
PDF
Black Hat USA 2025 - Micro ICS Summit - ICS/OT Threat Landscape
FORM 1 BIOLOGY MIND MAPS and their schemes
Trump Administration's workforce development strategy
MBA _Common_ 2nd year Syllabus _2021-22_.pdf
احياء السادس العلمي - الفصل الثالث (التكاثر) منهج متميزين/كلية بغداد/موهوبين
Τίμαιος είναι φιλοσοφικός διάλογος του Πλάτωνα
Share_Module_2_Power_conflict_and_negotiation.pptx
Computing-Curriculum for Schools in Ghana
AI-driven educational solutions for real-life interventions in the Philippine...
Paper A Mock Exam 9_ Attempt review.pdf.
advance database management system book.pdf
History, Philosophy and sociology of education (1).pptx
20th Century Theater, Methods, History.pptx
Chinmaya Tiranga quiz Grand Finale.pdf
Introduction to pro and eukaryotes and differences.pptx
Hazard Identification & Risk Assessment .pdf
Empowerment Technology for Senior High School Guide
A powerpoint presentation on the Revised K-10 Science Shaping Paper
202450812 BayCHI UCSC-SV 20250812 v17.pptx
ELIAS-SEZIURE AND EPilepsy semmioan session.pptx
Black Hat USA 2025 - Micro ICS Summit - ICS/OT Threat Landscape

Tagliatela College of EngineeringEASC1112 – Methods of Engineeri.docx

  • 1. Tagliatela College of Engineering EASC1112 – Methods of Engineering Analysis TO: EASC 1112 Students FROM: EASC1112 Instructor Subject: Project 2, Optimum Pipe Insulation A long pipe is to be installed to transport steam from a boiler to another part of the plant. Insulation is needed on the pipe for both safety and economic reasons. You are to develop a spreadsheet to calculate the surface temperature of the insulated pipe and to model the heat loss to the surrounding air as a function of the thickness of insulation on the outside of the pipe. Your model should allow for variation in the key parameters to explore the effect of various changes. Using data generated by your model, select the best insulation thickness to maximize the present value of net savings in comparison to an un-insulated pipe. Provide appropriate plots and data tables to support your decision and to show the financial penalty for using a different insulation thickness. Heat Loss Calculation The steam pipe is to be made from schedule 40 steel with a diameter in the range of 2 to 3.5 inches (nominal pipe size). The pipe will be encased in fiberglass insulation with an aluminum sheet cladding to protect from weather. Heat loss for this case can be modeled using a combination of convection and conduction heat transfer rate equations. Heat from the steam is transferred to the inside wall of the pipe by forced convection, then through each of three layers by conduction (pipe wall, insulation, cladding) and finally from the outside of the cladding to the surrounding air by natural convection. The governing equations are shown below to calculate heat transferred per unit length of pipe:
  • 2. View of pipe looking along axis QS = rate of heat lost by steam to inside pipe wall Aluminum Cladding Q1, Q2, Q3 = rates of heat transferred through pipe wall, insulation, aluminum cladding, respectively r2 r1 r4 r3 Fiberglass Insulation Steel Pipe STEAM QA=rate of heat lost to air The heat transfer rate equations include constants for the thermal conductivity of the materials and heat transfer coefficients for the convective situations. Values for these will be fixed for the analysis. The temperatures of the steam and the air will be fixed values, but the temperatures at each surface will be dependent on the thickness of insulation and size of the pipe. The subscripts used for the temperatures correspond to radial distances from the center of the pipe. The radii values will be fixed for a particular case of pipe size and insulation thickness, but will be varied as part of the optimization work. The intermediate temperatures, to be found by simultaneous solution of the
  • 3. equation set, are: T1 = temperature of the inside wall of the pipe, at distance r1 from the pipe center axis T2 = temperature of the outside pipe wall and the inside of the insulation, distance r2 T3=temperature of the outside of the insulation and inside of the aluminum cladding, distance r3 T4 = temperature of the outside surface of the cladding, exposed to the air, at distance r4 Average steady-state conditions will be used for the analysis of each case, thus the rate of heat lost from the steam must equal the rate of heat transferred through each layer and ultimately the rate of heat lost from the outside cladding to the air. Thus four linear equations can be obtained by setting QA = Q1, Q1=Q2, etc. The resulting equations can be solved using matrix techniques to find the unknown temperatures. Any one of the heat rate equations can then be used to find the heat loss rate. The constants (h's , k's, π and numbers) and the parameters (radii values) become the coefficients, and are shown in the equations above as C1 through C4. For a given case, these will be easily calculated. Terms containing the steam and air temperature are also constants (shift to the right side of equation). For example, setting QS = Q1 and Q1 = Q2 results in the following: Similar equations result from setting Q2 = Q3 and Q3 = QA. Your spreadsheet should have a data section for setting the pipe diameter and insulation thickness along with values for the constants, such as steam and air temperatures, thermal conductivity values, cost information, etc. Develop the model such that entry of a pipe diameter and an insulation thickness
  • 4. results in determination of the 4 temperatures and the rate of heat loss for the full pipe length. Analysis of Insulation Thickness Using your model, determine the optimum insulation thickness for different pipe diameters to achieve a maximum net present value of savings. Savings here is defined as the dollar value of energy NOT lost as a result of the insulation. To calculate this you must first determine the heat that would be lost if the pipe was not insulated. Simply subtract the heat loss for a particular insulation thickness from the bare pipe heat loss to determine the energy savings. The cost to insulate the pipe includes both the material cost and the installation labor. A net installed cost is found by multiplying the material cost by an installation factor to account for labor and other installation expenses. Data is provided at the end of this memo for physical properties, cost information etc. Optimization work requires an objective to be maximized or minimized. In this project the "objective function" is the present value of savings over a 5 year period using a specific interest rate with monthly compounding. The installed cost of insulating the pipe occurs at time zero (present) and is negative, so this is subtracted from the present value of 5 years of savings. Varying the insulation thickness will affect this value, so you can determine if there is an optimum which maximizes the present value. You should also be aware of safety concerns associated with a long run of steam pipe. In particular you should assure that the outside surface temperature is no higher than 50oC. Report Requirements At present, the diameter of the steam pipe has not determined, but it will be between 2 and 3 ½ inch schedule 40 steel pipe. Dimensions for standard steel pipe are available in the literature and should be used in this project. After creating the spreadsheet model, you should run simulations for cases in which you vary the insulation thickness from 0.1 to 6.0 cm. Prepare plots showing surface temperature, installed cost,
  • 5. annual savings and net present value as a function of insulation thickness. Create other plots as you deem necessary to justify your design decisions regarding the insulation thickness. A full analysis of this type should be performed for one pipe diameter. In addition, you should determine the optimum thickness and required thickness to achieve an acceptable surface temperature for all pipe sizes in the range given above. Note that nominal pipe sizes in this range are incremented in ½ inch steps. For each pipe size, recommend an insulation thickness. Your memo should give an overview of the project, discuss your approach, present results and discuss methods used and assumptions made. Tables and plots should appear in the memo to with explanation to make your points. Your concluding paragraph should include a discussion of what you learned in doing the project. Your spreadsheet should, of course, be well- documented and well-organized to show clearly how the work was done. The spreadsheet should include the following features: · List of pipe diameters using the data validation methods · Retrieval of dimensions for pipes from a table keyed to the selected pipe size (use Vlookup) · Scroll bar to set the insulation thickness · Key results copied to tables, with accompanying graphs for key results · Use Solver to vary thickness to maximize present value of net savings · Any additional functional features you wish to include to make the simulation tool more useful The project is due per your instructors directions, with a paper submission of the memo and attached printout of the spreadsheet. The spreadsheet should also be submitted via Blackboard. Required data is found on the next page. Input data for use in project Properties of pipe, insulation and outer cladding material
  • 6. Financial Analysis Parameters Item Material k, thermal conductivity density cost *Install Factor Energy cost Annual Interest Rate Period of analysis W/m-C kg/m3 $/kg $/$ $/kWh percent years Pipe steel 43 7800 NA 5 $0.04 3.0% 5 insulation fiber glass 0.055 64.1 30
  • 7. Per month months Outer Layer aluminum 206 2700 40 0.25% 60 0.5 mm thick * Installed cost = (total material cost) x installation factor Heat Transfer Coefficients W m2-oC Other Parameters From steam to inside pipe wall From outside pipe cladding to air Steam Temperature Air Temperature Pipe Length hS hA
  • 8. C C Meter 50 5 150 10 50 Properties of Standard Steel Pipe Schedule 40 Pipe Diameters Wall thickness Pipe OD, cm ID, cm cm 2 6.033 5.25 o.39 2.5 7.303 6.271 0.52 3 8.89 7.792 0.55 3.5 10.16 9.012 0.57
  • 20. - Layer Each for Rate Transfer Heat p p p p p Alaboudi 1 UNIVERSITY OF NEW HAVEN Tagliatela College of Engineering TO: Professor FROM: Abdullah Alaboudi November 10, 2016 EASC 1112 Project 2: Optimum Pipe Insulation
  • 21. Summery: A team contains three students were tasked to design and develop a spreadsheet to calculate the surface temperature of the installed pipe. The team needs to concern the heat loss from the steam transported through a pipe from a boiler to another part of the plant. The team’s aim was to determined the best insulation thickness and pipe size to maximized the value of net saving and camper with the un-insulated pipe to find the financial penalty by using different insulation thickness. The present value cost was to be operated for five years. The team decided to pick the 2.5 pipe size as the best choice economically, and it terms of energy loss. Challenges: 1. Set up the equations. 2. Conflict schedules between team members. 3. Excel deleted some of the work, and it cost more time to re-do it. Discussion: The issue was to figure the heat loss (Q), the radius in each layer, (R), temperatures (T), and the (C’s). The first thing the team has done was rearranging the given equations to solve by using matrix. After that, the team solves for the heat loss since the team found the temperatures by the inverse of the coefficient. To begin, the properties of pipe and the material
  • 22. were sorted out, including the thickness of each layer. In this data chart, the costs of every material, steel, protection, and aluminum, were set by taking the mass, material cost, and establishment expense (Appendix I). The following step was to focus on the different parameters and the inverse of coefficients. For instance, the temperature of the air, steam, and the length of the funnel (Appendix II). The budgetary parameters and the financial analysis were sorted to be the vitality expense and the interest rate from month to month or year to year. (Appendix III). Moreover, the properties of a standard steel pipe including the pipe size, outside, inside dimeter and well thickness, which involve finding the different temperature (Appendix IV). After solving for the various temperatures by using taking the coefficient and solve using matrix (Appendix V) and (Appendix VI). The team had to do the same method to solve with out insulation by doing the same methods (Appendix VII). The Q’s comparisons for networks were utilized to find the temperature for each thickness forms the protected pipe. To calculate the radiuses and convert to be cm by using offset equation (Appendix VIII) The team used the annual saving, cost, heat loss, and the present value of a Y and the insulation thickness as an X to show the changes as the insulation thickness changes (Appendix XI) (Appendix XII) (Appendix XIII) (Appendix XIV). By using Solver, the team was able to identify the best insulation thickness in each pipe
  • 23. (Appendix XV). Conclusion: Project 2 in EASC 1112 course, was a very enjoyable project, and made the team think in terms of saving energy and money as well by using the given methods. Each member of the team contributed and did their best to get the work done nicely and accurately. For the final result, the team identified that pipe 2.5 with 3.57 insulation thickness was the best choice for the pipe to be installed. Appendices:
  • 24. Appendix I: Properties of pipe, insulation and outer cladding material Appendix II: Heat Transfer Coefficients and Other Parameters Chart. Appendix III: Financial Analysis Parameters Chart Appendix IV: properties of stander steel Pipe. Appendix V: Matrix of Temperatures Chart Appendix VI: Matrix Q with Insulation Chart Appendix VII: Matrix Q without Insulation Chart Appendix VIII: Pipe size and the radius Appendix IX: Off sit equation for Pipe size Appendix X: Off sit equation for insulation thickness Appendix XI: Surface Temperature versus Insulation Thickness Graph Appendix XII: Annual Savings versus Insulation Thickness Graph Appendix XIII: Installed Cost versus Insulation Thickness Graph Appendix XIV: Present Value versus Insulation Thickness Graph Appendix XV: Best insulation thickness of each pipe.
  • 25. Appendix I: Properties of pipe, insulation and outer cladding material Appendix II: Heat Transfer Coefficients and Other Parameters Chart. Appendix III: Financial Analysis Parameters Chart Appendix IV: properties of stander steel Pipe Appendix V: Matrix of Temperatures Chart Appendix VI: Matrix Q with Insulation Chart Appendix VII: Matrix Q without Insulation Chart. Appendix VIII: Pipe size and the radius.
  • 26. The team uses the Offset equation to make the pipe size and insulation thickness changeable as a shortcut. Offset equation is shown in the pictures shown below. Appendix IX: Off sit equation for Pipe size Appendix X: Off sit equation for insulation thickness Appendix XI: Surface Temperature versus Insulation Thickness Graph Appendix XII: Annual Savings versus Insulation Thickness Graph Appendix XIII: Installed Cost versus Insulation Thickness Graph Appendix XIV: Present Value versus Insulation Thickness Graph Appendix XV: Best insulation thickness of each pipe. The picture displayed below shows a chart with calculation.
  • 27. The picture displayed below shows the 5 years’ payment.