Accepted Manuscript Title: Determination of energy saving and optimum insulation thicknesses of the heating piping systems for different insulation materials Author: Muhammet Kayfeci PII: DOI: Reference:
S0378-7788(13)00699-3 http://dx.doi.org/doi:10.1016/j.enbuild.2013.11.017 ENB 4618
To appear in:
ENB
Received date: Accepted date:
21-9-2012 1-11-2013
Please cite this article as: M. Kayfeci, Determination of energy saving and optimum insulation thicknesses of the heating piping systems for different insulation materials, Energy and Buildings (2013), http://dx.doi.org/10.1016/j.enbuild.2013.11.017 This is a PDF file of an unedited manuscript that has been accepted for publication. As a service to our customers we are providing this early version of the manuscript. The manuscript will undergo copyediting, typesetting, and review of the resulting proof before it is published in its final form. Please note that during the production process errors may be discovered which could affect the content, and all legal disclaimers that apply to the journal pertain.
1
Research Highlights
2
An optimization model is performed depending on LCC analysis for heating system pipe
3
line. Energy saving, annual cost and payback periods are calculated.
5
The highest value of energy saving reached in 250 mm DN for EPS insulation.
6
The OIT vary between 0.66 and 0.146 m depending on pipe sizes and insulation materials.
us
cr
ip t
4
Ac ce
pt
ed
M
an
7
1 Page 1 of 30
7
Determination of energy saving and optimum insulation thicknesses of the
8
heating piping systems for different insulation materials
9
Muhammet Kayfeci
11
Department of Energy Systems Engineering, Faculty of Technology, Karabuk University,
12
TR-78050, Karabuk, Turkey
13
+903704338200/1089 (off), +904338204 (fax),
[email protected]
14
[email protected] (email)
cr
15
ip t
10
Abstract – Large amounts of heat losses occur in pipelines of district heating system. If
17
these lines become insulated, a significant energy savings would be obtained. In this study, by
18
using life cycle cost analysis (LCCA) method, the optimum insulation thickness, energy
19
savings, annual costs and payback period were estimated for various pipe diameters and
20
insulation materials of the heating systems in Isparta/Turkey and in the regions with different
21
degree-day values. As a fuel, natural gas was used in the study. In consequence of the
22
calculations, the optimum insulation thickness was found vary between 0.048 and 0.134 m,
23
the energy-saving was found vary between 10.84 $/m and 49.78 $/m; and the payback period
24
was found vary between 0.74 and 1.29 years. According to these results, EPS insulation
25
material with a nominal diameter (DN) of 250 mm provides the highest energy savings, while
26
the lowest value was found to be in fiberglass insulation material with DN 50 mm. As a
27
result, heating systems, selection of suitable pipe diameters and insulation materials with
28
optimum thicknesses provide significant economic advantages and savings.
29
Keywords: Heating; pipe insulation; optimum insulation thickness; energy saving.
31 32
an
M
ed
pt
Ac ce
30
us
16
1. Introduction
In many countries, the energy required for space heating in buildings has the highest
33
share of all which is about 40% of total energy consumed in the residential sector and this
34
energy transport with pipe networks. Increasing energy demand and environmental
35
consciousness all over the world have made it imperative that energy sources should be used a
36
lot more efficiently. The most important part of the energy strategy of any country is energy
37
saving. Because of the limited energy-sources and environmental pollution arising from the
38
use of fuels, energy saving has become compulsory [1]. It is clear from the above data that
39
effective thermal protection in residential sector plays an important role towards the reduction 2 Page 2 of 30
40
of energy consumption for space heating. Using proper insulation in pipe network is perhaps
41
the most effective way of energy conservation in district heating applications. Insulation
42
reduces fuel consumption, undesirable emissions from the burning of fossil fuels. Insulation
43
as a single investment pays for itself many times over during the life cycle of a pipe network. Most of the available studies focus on insulating heating and cooling buildings [2-5]
45
and insulated piping line [6-14], because of the large potential for energy savings. However,
46
most of these studies consider uniform insulation thickness. For example, Öztürk and Karabay
47
[10] presented a computer code that calculates optimum pipe diameters and insulation
48
thickness for district heating networks. The code includes a thermo economic optimization
49
model. In this model, exergy destruction and exergy loss costs of piping network are
50
considered as operation cost and piping and insulation costs considered as investment costs.
51
Kalyon and Şahin [11] optimum insulation thickness of a pipe subjected to convective heat
52
transfer that minimizes the heat loss is studied using the control theory approach and steepest
53
descent method. As a constraint to the problem, the amount of insulation material is assumed
54
to be fixed. A circular pipe through which fluid is transported from one end to the other is
55
considered. Variations of the bulk temperature of the
56
outer surface of the insulation are evaluated. Keçebaş et al. [12] presented, optimum
57
insulation thickness of pipes used in district heating pipeline networks, energy savings over a
58
lifetime of 10 years, and payback periods are calculated for the five different pipe sizes and
59
four different fuel types in the city of Afyonkarahisar/Turkey. For this reason, an optimization
60
model is performed depending on Life Cycle Cost Analysis (LCCA) via P1-P2 method.
61
Wechsatol et al. [13] investigated the optimal geometric layout of schemes for distributing hot
62
water uniformly over an area. The amount of insulation material, the volume of all the pipes,
63
and the amount of pipe wall material were the main constraints in their work. Zaki and Al-
64
Turki [14] calculated the optimum thickness of insulation material for a pipeline using
65
different layers of material of different properties and cost.
cr
us
an
M
pt
ed
fluid as well as the temperatures of the
Ac ce
66
ip t
44
Turkey is divided into four climatic zones depending on average temperature degree-
67
days of heating. Climatic conditions are the major factors governing the heat load
68
requirements of the buildings. Valid for a base temperature of 15 °C and an interior ambient
69
temperature of 20 °C, HDD values are less than 1500 for the first region, and greater than
70
4500 for the fourth region [15]. Isparta is third climatic zone in Turkey [16].
71
In this study is to provide a methodology for predicting thermal performance of five
72
different insulation materials used in heating pipe systems. Firstly, the thickness, energy
73
saving, payback period, annual fuel consumption for insulation in heating pipelines is 3 Page 3 of 30
74
determined depending on LCCA analysis via P1-P2 method by considering the heat
75
conductivity and price of the insulation material, average temperature in the region, fuel price
76
for the heating and factors related to regulations, and the results obtained are evaluated.
77 78
2. Analysis
79
2.1. The structure of the heating system pipes Heat gain, heat loss and temperature change of transfer pipe lines for heating systems
81
are significantly influenced by insulation, surrounding environment – ambient air for above
82
ground pipe or soil for underground pipe, and pipe structure. Consider the circular pipe
83
through which a given fluid is transported from one end to the other as shown in Fig. 1 for
84
unit length. The assumptions are a constant environmental and hot fluid temperature and
85
constant thermodynamic properties at an appropriate mean temperature. Besides, the hot fluid
86
for a heating system is pumped through the pipe with a constant velocity under steady-state
87
steady-flow control volume conditions.
an
us
cr
ip t
80
In this study, the insulation materials properties given in Table 1 such as foam board,
89
XPS, rock wool, EPS and fiberglass as insulation materials are chosen for the heating piping
90
system. The pipe materials for piping system of heating are taken as stainless steel pipe, the
91
properties of which are given in Table 2. Another parameters used in calculation are given in
92
Table 3.
ed
M
88
94
pt
93
2.2. Heat loss through heating system pipe network I calculate optimum heating system pipe insulation thickness considering heat losses
96
from throughout pipe surface. Heat loss from heating system pipe can be calculated by the
97
following heat conduction equation.
98
Q p U A(Tf To ) U A T
99
where U is the overall heat transfer coefficient of pipe layers, To is the temperature of ambient
100
air, Tf is the average design temperature of inside hot fluid. The annual heat loss can be
101
determined by
102
Q A 86,400 HDD U
Ac ce
95
(1)
(2)
103
Where HDD is the heating degree days of analyzed city. The annual energy
104
requirement for heating can be calculated by dividing heat loss to the efficiency of the heating
105
system, ηs,
4 Page 4 of 30
86,400 HDD U s
106
Ew
107
The total internal resistance of un-insulated heating piping system is giving by
(3)
r ln 1 r0 1 1 h i A i 2Lk 1 h o A o
108
R p ,un ins
109
and the total internal resistance of insulated heating piping system is giving by
ip t
(5)
r r ln 1 ln 2 r0 r 1 1 1 h i A i 2Lk1 2Lk ins h o Ao
R p,ins
111
Here, kins is the heat transfer coefficient of insulation materials and it must be kept in mind
112
that the outside surface area of the last layer of piping system is A o 2 L r2 . Furthermore,
113
the convection heat transfer coefficients for the inside and outside surfaces of piping system,
114
respectively, hi and ho are calculated as [18].
115
hiD 0.023 Re 0.8 Pr 0.4 kf
116
and
117
h o 11.581 d
118
where kf is the heat transfer coefficient of fluid in the inside of pipe. Eq. In here, d=D+2δ, and
119
Tms the mean outside surface temperature of piping system.
us
U U un ins U ins
Ac ce
122
125
(7)
(8)
The difference between the overall heat transfer coefficients of un-insulated and insulated piping systems can be written as
124
an
M
2 Tms To 546.30.181 Tms To 0.266 1 2.86 Vair 0.5
ed
0.2
121
123
(6)
pt
120
cr
110
1
R p, un ins
1
(9)
R p ,ins
The effect of the outside radius of insulated piping system on the thermal transmission
efficiency can be obtained by differentiating Eq. (9) and the result is as follow 1 1 2Lk ins r2 2Lh o r2 2
U r2 r r ln 1 ln 2 r0 r1 1 1 h i A i 2Lk 1 2Lk ins h o A o
2
(10)
5 Page 5 of 30
Besides, the heat loss load between the un-insulated and insulated piping systems may
126 127
be obtained from following equation
128
Q save Q un ins Q ins U T U un ins U ins T
(11)
129 130
2.3. Optimization of hot fluid pipe insulation thickness and energy saving In this study, determination of the amount energy cost calculated using P1-P2 method.
132
This method is a practical and can be used for optimization the insulation thickness of hot
133
fluid pipe system. The annual total energy cost, Cf, is given
134
Cf
135
where Hu is lower heating value of the fuel given J/m3 and CF is fuel cost in $/m3. The annual
136
fuel consumption is
137
mf
138
There mf is annual fuel consumption in m3/m year [12]. The total investment cost of
139
insulation is given by the following equation
140
C ins C I V
141
where CI is the cost of insulation material in $/m3 and V, in m3 is the volume of material used
142
in insulation.
us
cr
86,400 HDD U C F H u s
ip t
131
(13)
(14)
ed
M
an
86,400 HDD U H u s
(12)
The first cost of insulation may be treated as capital investment. It is possible to
144
calculate the present worth of the net amount of energy savings via insulation using a well
145
known method known as the P1-P2 method [19]. P1 has relation with inflation rate d, interest
146
rate i, and lifetime N. P2 is the ratio of the life cycle expenditures incurred because of the
147
additional capital investment to the initial investment. The equations for P1 is defined as [20]
148
P1
149
P2 1 P1M s R v 1 d N
150
where Ms is the ratio of the annual maintenance and operation cost to the original first cost, Rv
151
is the ratio of the resale value to the first cost. P2 can be taken as 1 if the maintenance and
152
operation cost is zero. If the increase rate is equal to discount rate, P1 is calculated from
153
P1
Ac ce
pt
143
N 1 1 i 1 if i≠d (d i) 1 d
(15) (16)
N if i=d 1 i
(17)
6 Page 6 of 30
The total cost of heating with the insulated piping system can be calculated by the
154 155
following equations
156
Ct P1Cf P2 Cins
The net energy cost savings over the lifetime for heating from using insulation
157
material, S, can be formulated with P1-P2 method as
S 159
86,400 P1 HDD U CF P2 CI V H u s
ip t
158
(18)
(19)
The outside radius of insulated piping system can be determined by maximizing Eq.
161
(18) or minimizing Eq. (19). So the differential of S or Ct with respect to r2 is taken and set
162
equal to zero, then the optimum insulation thickness ins r2 r1 is obtained using MAPLE
163
technical computing software. Selecting P1 from cases of i≠d (Eq. (15)) or i=d (Eq. (17)), the
164
selected P1 into Eq. (19) is inserted and set equal to zero, then pay-back period Np can be
165
calculated [12].
an
us
cr
160
166
3. Results and Discussion
M
167
In heating system pipe insulation applications, the energy transmission requirement
169
does not decrease the same rate as well since the overall heat transfer coefficient does not
170
direct proportionally change with insulation thickness. Especially in cylindrical geometries,
171
insulation thickness and insulation cost increased non-linearly, while it caused small
172
decreases in the fuel cost. The total cost decreases initially and then increased gradually,
173
depending on the increases in the cost of insulation material. The insulation thickness that
174
gives the minimum value of the total cost curve is referred to as the optimum insulation
175
thickness. The changes in the fuel costs, insulation costs and total costs of a fiberglass
176
insulation material with a DN of 100 mm, depending on insulation thickness, are given in
177
Fig.2. As shown there, the optimum insulation thickness for a fiberglass material a DN of 100
178
mm was found to be 5.7 cm. Since the fuel costs are high in Turkey, optimum insulation
179
thicknesses usually increase depending on fuel costs. For DN 100 mm, the changes in total
180
lifetime energy savings of different insulation materials, depending on insulation thickness,
181
are shown comparatively in Fig.3; where, the energy saving for fiberglass insulation is 25.96
182
$/m, while the energy saving for EPS insulation is 28.45 $/m.
Ac ce
pt
ed
168
183
Total cost depends on insulation thickness, when it is minimum with a certain
184
thickness. Energy saving is also dependent on the thickness of insulation. Increase in
185
insulation thickness that exceeds investment cost provides increases in energy saving from 7 Page 7 of 30
fuel costs. In case of thicknesses more than a certain value, costs would exceed the saving, i.e.
187
the additional thickness of the insulation material would be no longer economic. With the
188
increase in insulation thickness, the optimum insulation thickness was obtained from the
189
point, at which the saving begins to decrease. The changes in the energy savings depending
190
on insulation thicknesses, which were obtained throughout life cycle by use of different
191
insulation materials with all DN values, are shown in Fig.4. As clearly seen in the chart,
192
energy savings increase in parallel with the increase in DN thickness; and the highest gain for
193
a total life of 10 years was obtained at DN 250 mm.
ip t
186
Changes in optimum insulation thicknesses of different insulating materials,
195
depending on DN, are shown in Fig. 5. With the increase in nominal pipe thickness, the
196
optimum insulation thickness increased as well. As clearly seen in the chart, the maximum
197
insulation thickness was obtained from DN 250 mm, when mineral wool was used as an
198
insulation material. This is because the heat transfer coefficient of the insulation material
199
consisting of mineral wool was high. Changes of energy savings for different insulation
200
materials are shown in Fig.6, according to the DN values. In parallel with the increase in DN,
201
the amount of savings for all insulation materials increased. The greatest saving was obtained
202
by use of EPS insulation material. When EPS insulation material is used, DN 50, 100, 150,
203
200 and 250 mm provided savings in the amount of 12.22, 22.28, 32.01, 40.75 and 49.78 $/m
204
respectively. In addition, increases in energy saving are observed in parallel with increases in
205
pipe diameters. Form the Figure, it can be understood that greater energy savings can be
206
obtained by means of pipes with big diameters in comparison with small diameters. For
207
different insulation materials, changes in payback period at optimum insulation thicknesses
208
are shown in Fig.7, according to DN values. Payback period varies depending on the initial
209
investment cost of the system. The longest payback period was found to be 1.29 years, for DN
210
250 mm and fiberglass insulation material.
us
an
M
ed
pt
Ac ce
211
cr
194
There are four different degree-day regions in Turkey, and the coldest one is the 4th
212
degree-day region. The calculations were made for the city of Isparta with the degree-day
213
value of 2607. Isparta is located in the 3rd degree-day region, and has a cold climate. In order
214
to enable the data obtained during the study to be used in different regions, the calculations
215
were expanded by using different degree-day values. For different insulation materials,
216
changes in optimum insulation thicknesses that depend on degree-day values are shown in
217
Fig. 8. The optimum insulation thickness increased in parallel with the increase in the degree-
218
day values and insulation cost. Energy saving is directly proportional to fuel cost and climate
219
conditions. Therefore, energy saving becomes more important in cold climates. For different 8 Page 8 of 30
insulation materials, the effect of degree-day values on energy saving is shown in Fig.9.
221
Annual saving increases with degree-day values, while insulation cost and insulation heat
222
transfer coefficient decrease. For different materials, the effect of degree-day values on
223
payback period is shown in Fig.10. As shown in the figure, payback period decreases
224
according as degree-day values increases. It seems clearly that the payback period becomes
225
shorter in cold regions, by means of insulation cost. In order to prevent thermal energy loss in
226
heating system pipeline, and to reduce fuel consumption, the fluid must be kept in the pipe.
227
Thermal insulation is one of the most important ways to do this. As shown in Fig.11, the
228
annual fuel consumption decreased with the insulation application. The effect of insulation
229
thickness of insulating material on fuel consumption is clearly seen in the figure. Using
230
thermal insulation reduces use of energy and provides a significant fuel saving. When the
231
optimum insulation thickness was used in the pipelines, the fuel consumption increased
232
depending on the insulation thickness. For example, the fuel consumption for DN 100 mm
233
was found between 0.607 and 7.607 m3/m, depending on the insulation thickness. For all pipe
234
diameters, the highest fuel consumption occurred when rockwool insulation material was
235
used; and this material was followed by XPS, EPS and foamboard. The optimum insulation
236
thickness, energy saving and payback period values for different insulation materials with
237
different pipe diameters are given in Table 4. As shown in the table, the optimum insulation
238
thickness was found vary between 0.048 and 0.134 mm, depending on DN and the insulating
239
material, while the energy savings were found vary between 10.84 and 49.78 $/m. The lowest
240
energy saving was found at DN 50 mm for fiberglass insulation material, while the highest
241
energy saving was obtained when EPS insulation material with the value of DN 250 mm was
242
used.
244 245
cr
us
an
M
ed
pt
Ac ce
243
ip t
220
4. Conclusion
In this study the optimum insulation thickness of the heating system pipe, energy
246
savings over a lifetime of 10 years and payback periods are calculated for the five different
247
insulation materials for Isparta city of Turkey. The degree-days used in the study can also be
248
used in other countries having different degree-days. And this reason analysis results were
249
extended for this insulation materials can be chosen in different climatic zone on world. These
250
results show that energy cost savings are directly proportional to the cost of fuel, insulation
251
material and climatic conditions. It is seen that energy savings vary between 10.84 and 49.78
252
$/m depending on pipe DNs and insulation materials. The highest value of optimum 9 Page 9 of 30
insulation thicknesses is reached by using rock wool as insulation in 250 mm DN, whereas the
254
lowest optimum insulation thickness is obtained by using fiberglass as insulation in 50 mm
255
DN. The highest payback period value with 1.29 years in 250 mm DN found by using
256
fiberglass as insulations, while the lowest value with 0.74 years by using EPS as insulation in
257
50 mm DN. These results show that energy saving is more significant when a costly fuel is
258
used for heating system pipe network. The fiberglass is a better choice when the optimum
259
insulation thickness is an important consideration. The insulation material installed at its
260
optimum insulation thickness in the heating pipelines will not only reduce the heat loss from
261
the heating pipeline but also has economical and environmental advantages.
cr
ip t
253
Nomenclature
264
Ao
Outside surface area of nth layer of pipe (m2)
265
A
Total surface area of pipe (m2)
266
Ai
Inside surface area of pipe (m2)
267
Ao
Outside surface area of last layer of pipe (m2)
268
Cf
Annual energy cost ($)
269
CF
Fuel cost ($/m3)
270
CI
Cost of insulation material per unit volume ($/m3)
271
Cins
Total insulation cost ($)
272
Ct
Total cost of heating ($)
273
d
Increase rate (%)
274
Ew
Total annual energy requirement for heating
275
HDD Heating Degree-Days (°C-days)
276
hi
277
ho
278
Hu
279
i
280
kf
The heat transfer coefficient of fluid in the inside of pipe (W/m K)
281
kins
Thermal conductivity of insulation material (W/m K)
282
L
Length of pipe (m)
283
LCCA Life Cycle Cost Analysis
284
mf
The annual fuel consumption for heating
285
N
Lifetime (years)
pt
ed
M
an
us
263
Ac ce
262
Convection heat transfer coefficient for inside of pipe (W/m2 K) Convection heat transfer coefficient for outside of pipe (W/m2 K) Lower heating value of the fuel (J/m3) Discount rate (%)
10 Page 10 of 30
Np
Payback period (years)
287
QA
The annual heat loss (W)
288
Qp
Heat losses occurred from pipe (W)
289
Qsave
Pipe heat load between un-insulated and insulated piping systems (W)
290
Rp
Total internal resistance of piping system (K/W)
291
Rp,ins Internal resistance of insulated pipe (K/W)
292
Rp,un-ins Internal resistance of un-insulated pipe (K/W)
293
S
Energy savings ($)
294
Tf
Average design temperature of inside fluid (K)
295
Tb
The base temperature (K)
296
Tms
The mean outside surface temperature of piping system (K)
297
To
Design temperature of outside air (K)
298
Tsa
The solar-air temperature for each hour (K)
299
U
Overall heat transfer coefficient (W/m K)
300
Uins
Overall heat transfer coefficient of insulated pipe (W/m2 K)
301
Uun-ins Overall heat transfer coefficient of un-insulated pipe (W/m2 K)
302
V
The volume of insulation material (m3)
303
δins
Optimum insulation thickness (m)
304
ΔT
Difference between inside and outside design temperature (K)
305
ΔU
Difference between overall heat transfer coefficients of un-insulated and insulated
ηs
308 309
References
310
[1]
cr
us
an
M
Ö.A. Dombaycı, M. Gölcü, Y. Pancar, Optimization of insulation thickness for external walls using different energy-sources, Applied Energy 83 (2006) 921-928.
311 312
ed
The efficiency of the heating system
Ac ce
307
pt
pipes
306
ip t
286
[2]
A. Bolattürk, Optimum insulation thicknesses for building walls with respect to cooling
313
and heating degree-hours in the warmest zone of Turkey, Building and Environment 43
314
(2008) 1055-1064.
315
[3]
A. Kecebas, M. Kayveci, Effect on optimum insulation thickness, cost and saving of
316
storage design temperature in cold storage in Turkey, Energy Education Science and
317
Technology A 25 (2010) 117-127.
318
[4]
T.M.I. Mahlia, B.N. Taufiq, Ismail, H.H. Masjuki, Correlation between thermal 11 Page 11 of 30
319
conductivity and the thickness of selected insulation materials for building wall, Energy
320
and Buildings 39(2) (2007) 182-187.
321
[5]
Energy Conversion and Management 40 (1999) 13-21.
322 323
M.S. Soylemez, M. Unsal, Optimum insulation thickness for refrigeration applications.
[6]
A. Bahadori, H.B. Vuthaluru, A simple correlation for estimation of economic thickness of thermal insulation for process piping and equipment, Applied Thermal Engineering
325
30 (2010) 254-259. [7] [8]
E.M. Alawadhi, Thermal analysis of a pipe insulation with a phase change material: material selection and sizing, Heat Transfer Engineering, 29(7) (2008) 624-631.
329 330
cr
systems: a comparison study, Energy 31 (2006) 2094-2107.
327 328
İ.T. Öztürk, H. Karabay, E. Bilgen, Thermo-economic optimization of hot water piping
[9]
us
326
ip t
324
H. Chou, Optimization interior area thermal resistance model to analyze the heat transfer characteristics of the insulation pipe with arbitrary shape, Energy Conversion
332
and Management 44 (2003) 2915-2939.
an
331
[10] İ.T. Öztürk, H. Karabay, Thermo economic optimization of district heating network,
334
Processing of the First Int Exergy, Energy and Environment Symposium (IEEES-1)
335
İzmir/Turkey (2003) 311-317.
337
[11] M. Kalyon, A.Z. Sahin, Application of optimal control theory in pipe insulation,
ed
336
M
333
Numerical Heat Transfer Part A-Applications 41 (2002) 391-402. [12] A. Keçebaş, M.A. Alkan, M. Bayhan, Thermo-economic analysis of pipe insulation for
339
district heating piping systems, Applied Thermal Engineering 31(17–18) (2011) 3929-
340
3937.
pt
338
[13] W. Wechsatol, S. Lorente, A. Bejan, Tree-shaped insulated designs for the uniform
342
distribution of hot water over an area, International Journal of Heat Mass Transfer 44
343
(2001) 3111-3123.
344 345 346 347 348 349
Ac ce
341
[14] G. Zaki, A. Al-Turki, Optimization multi layer thermal insulation for pipelines, Heat Transfer Engineering 21(4) (2000) 63-70. [15] A.K. Dağsöz, Degree-day values in Turkey, National energy saving policy, heat insulation in buildings, Izocam, Istanbul;1995 (in Turkish). [16] Turkish Standard Number 825 (TS 825), 1999. Official Gazette Number 23725 (in Turkish).
350
[17] A. Ucar, F. Balo, Effect of fuel type on the optimum thickness of selected insulation
351
materials for the four different climatic regions of Turkey, Applied Energy 86 (2009)
352
730-736. 12 Page 12 of 30
353
[18] J.P. Holman, Heat transfer, 7th ed. New York: McGraw-Hill Book Co.; 1992.
354
[19] J.A. Duffie, W.A. Beckman, Solar engineering of thermal processes, New York: Wiley,
355
1980.
356
[20] N. Sisman, E. Kahya, N. Aras, H. Aras, Determination of optimum insulation
357
thicknesses of the external walls and roof (ceiling) for Turkey’s different degree-day
358
regions, Energy Policy 35 (2007) 5151-5155.
Ac ce
pt
ed
M
an
us
cr
ip t
359
13 Page 13 of 30
359
FIGURES CAPTION
360
Figure 1. Heating systems pipe cross section.
361
Figure 2. Effect of insulation thickness on the costs for the fiberglass insulation material at
362
the NPS 100 mm. Figure 3. The comparison of energy savings in all the insulation material for 100 mm of NPS
364
Figure 4. The comparison of energy saving according to insulation thickness for all the NPS
369 370 371 372 373
cr
us
368
insulation materials.
Figure 6. Comparison of energy savings over the lifetime versus nominal pipe size types for
an
367
Figure 5. Effect of optimum insulation thickness on nominal pipe size types for different
different insulation materials.
Figure 7. Comparison of payback period versus nominal pipe size types for different
M
366
by using fiberglass as insulation materials.
insulation materials.
Figure 8. Optimum insulation thickness of heating piping versus DD values for different insulation materials.
ed
365
ip t
363
Figure 9. Annual saving of heating piping versus DD values for different insulation materials.
375
Figure 10. Payback period of heating piping versus DD values for different insulation
377 378 379
Ac ce
376
pt
374
materials.
Figure 11. The effect of the insulation thickness on the annual fuel consumption by insulation materials for a nominal pipe size of 100 mm.
380 381 382
14 Page 14 of 30
TABLE CAPTIONS
383
Table 1. Thermal conductivity and price values of insulation materials [3,17].
384
Table 2. Some properties of stainless steel pipes (ANSI B 36.10) used in heating pipelines.
385
Table 3. The parameters used in calculations.
386
Table 4. Optimum insulation thickness, energy saving and payback period for different
387
ip t
382
insulation materials and DN (Natural gas fuel).
cr
388
Ac ce
pt
ed
M
an
us
389
15 Page 15 of 30
389 390
Table 1. Thermal conductivity and price values of insulation materials [3,17]. Insulation materials Conductivity (W/mK) Price ($/m3) Foam board 0.027 193 XPS 0.031 224 Rockwool 0.040 95 EPS 0.028 155 Fiberglass 0.033 350
ip t
391 392
Ac ce
pt
ed
M
an
us
cr
393
16 Page 16 of 30
Table 2. Some properties of stainless steel pipes (ANSI B 36.10) used in heating pipelines. Outer Wall Unit Conductivity Nominal diameter diameter, r1 thickness, t weight mm inch mm mm kg/m W/mK 50 2 60.3 3.91 5.44 54 100 4 114.3 6.02 16.07 54 150 6 168.3 7.11 28.26 54 200 8 219.1 8.18 42.55 54 250 10 273.1 9.27 60.24 54
ip t
393 394
395
cr
396
Ac ce
pt
ed
M
an
us
397
17 Page 17 of 30
Table 3. The parameters used in calculations. Parameter Value Heating degree-days 2607 °C-days Fuel Natural gas Price, CF 0.5022 $/m3 Hu 34.485 x 106 J/kg Insulation materials See Table 1 Pipes See Table 2 Interest rate, i 4% Inflation rate, d 5% Lifetime, N 10 years
Ac ce
pt
ed
M
an
us
cr
399 400
ip t
397 398
18 Page 18 of 30
Table 4. Optimum insulation thickness, energy saving and payback period for different insulation materials and DN (Natural gas fuel). 50 0.090 Optimum insulation thickness (m) Rockwool EPS 0.068 Foam board 0.060 XPS 0.058 Fiberglass 0.048
Nominal pipe sizes (mm) 100 150 200 0.108 0.119 0.128 0.080 0.088 0.093 0.071 0.078 0.082 0.069 0.076 0.080 0.057 0.063 0.066
250 0.134 0.097 0.086 0.084 0.069
ip t
Insulation
Rockwool EPS Foam board XPS Fiberglass
11.63 12.22 12.08 11.53 10.84
21.49 22.28 22.05 21.24 20.18
31.03 32.01 31.74 30.71 29.45
39.56 40.75 40.48 39.30 37.98
48.32 49.78 49.56 48.25 47.01
Payback period (years)
Rockwool EPS Foam board XPS Fiberglass
0.77 0.74 0.81 0.93 1.15
0.75 0.75 0.81 0.93 1.18
0.75 0.75 0.83 0.95 1.21
0.76 0.77 0.85 0.98 1.25
0.77 0.79 0.87 1.01 1.29
an
Ac ce
pt
ed
M
402 403
cr
Energy saving ($/m)
us
400 401
19 Page 19 of 30
pt
ed
M
an
us
Figure 1. Hot water pipe cross section.
Ac ce
404 405 406
cr
ip t
403
20 Page 20 of 30
us
pt
ed
M
an
Figure 2. Effect of insulation thickness on the costs for the fiberglass insulation material at the DN 100 mm.
Ac ce
407 408 409 410
cr
ip t
406
21 Page 21 of 30
pt
ed
M
an
Figure 3. The comparison of energy savings in all the insulation material for 100 mm of DN.
Ac ce
411 412 413
us
cr
ip t
410
22 Page 22 of 30
pt
ed
M
an
Figure 4. The comparison of energy saving according to insulation thickness for all the NPS by using fiberglass as insulation materials.
Ac ce
414 415 416 417 418
us
cr
ip t
413
23 Page 23 of 30
pt
ed
M
an
Figure 5. Effect of optimum insulation thickness on nominal pipe size types for different insulation materials.
Ac ce
419 420 421 422
us
cr
ip t
418
24 Page 24 of 30
pt
ed
M
an
Figure 6. Comparison of energy savings over the lifetime versus nominal pipe size types for different insulation materials.
Ac ce
423 424 425 426
us
cr
ip t
422
25 Page 25 of 30
pt
ed
M
an
Figure 7. Comparison of payback period versus nominal pipe size types for different insulation materials.
Ac ce
427 428 429 430
us
cr
ip t
426
26 Page 26 of 30
pt
ed
M
an
Figure 8. Optimum insulation thickness of heating piping versus DD values for different insulation materials.
Ac ce
431 432 433 434
us
cr
ip t
430
27 Page 27 of 30
pt
ed
M
an
Figure 9. Annual saving of heating piping versus DD values for different insulation materials.
Ac ce
435 436 437
us
cr
ip t
434
28 Page 28 of 30
pt
ed
M
an
Figure 10. Payback period of heating piping versus DD values for different insulation materials.
Ac ce
438 439 440 441 442
us
cr
ip t
437
29 Page 29 of 30
pt
ed
M
an
Figure 11. The effect of the insulation thickness on the annual fuel consumption by insulation materials for a nominal pipe size of 100 mm.
Ac ce
443 444 445 446 447
us
cr
ip t
442
30 Page 30 of 30