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International Journal of Research in Engineering and Science (IJRES)
ISSN (Online): 2320-9364, ISSN (Print): 2320-9356
www.ijres.org Volume 2 Issue 4 ǁ April. 2014 ǁ PP.44-52
www.ijres.org 44 | Page
Design With Solid works Software and Planning Calculation
Analysis of Fire Tube Boiler With Lpg-Fuel For Oyster
Mushroom Small Industries In Pacet, Mojokerto, East Java,
Indonesia
Liza Rusdiyana1
, Sri Bangun S.2
, Denny M.E. Soedjono3
, Eddy Widiyono4
,
Suhariyanto5
1
Department of 3 Diplome of Mechanical Engeneering, Industrial Engeneering Faculty, Institute of
Technology Ten Nopember, Surabaya, 60111,Indonesia
2
Department of 3 Diplome of Mechanical Engeneering, Industrial Engeneering Faculty, Institute of
Technology Ten Nopember, Surabaya, 60111,Indonesia
3
Department of 3 Diplome of Mechanical Engeneering, Industrial Engeneering Faculty, Institute of
Technology Ten Nopember, Surabaya, 60111,Indonesia
4
Department of 3 Diplome of Mechanical Engeneering, Industrial Engeneering Faculty, Intitute of
Technology Ten Nopember, Surabaya, 60111,Indonesia
5
Department of 3 Diplome of Mechanical Engeneering, Industrial Engeneering Faculty, Intitute of
Technology Ten Nopember, Surabaya, 60111,Indonesia
ABSTRACT: Steam boilers (boilers) is a closed vessel made of steel that is used to generate steam. In the
modern era many industries such as household scale industries for the manufacture of oyster mushroom spawn
to use aid as a supplier of steam boilers are used as a sterilization process baglog. Annually, the number of
requests oyster mushroom spawn have been increases, so the boiler is very significant equipment to increase the
number of baglog production as oyster mushroom growing media.To help to fulfill the small
industryrequiremets for oyster mushroom nursery,plannedatype offire tubeboilerthatcanhelpthe availability
ofsteam ina lowscalewithsteamoutputcapacity of70kg/ h, temperature120℃,
pressure1.5barandusingmaterialsLPGfuelas a source ofheatenergy.From the results of this design, fire tube
boiler have efficiency of 0.934 % . The kettle body is made from asphalt drums pertamina with the Cold Rolled
Steel materials. Used asphalt drums because of its availability in the market more easier to obtained easily and
the dimensions of asphalt drum capable of holding for temperature and pressure have been determined . As for
the pipe material using Carbon Steel Tubing Boilers ASME SA - 178A GRADE A / SA - 214 (Plain Carbon).
Keywords: Boiler, Fire-tube,Significant, Fuel,AsphaltDrum, Oyster Mushroom
I. PREFACE
Sterilizationof baglog as oyster mushroom mediais one of thevery important
processinoystermushroom cultivationbecausethe mediahadcreatedusuallystill containsmanymicrobes,
especiallywildmushrooms. Manycrop failurescaused bymediasterilizationprocessis less than perfect.
Wildmushroomsthatstillexistinbaglogwill thriveandinhibitthe growth ofoyster mushroomif
thesterilizationprocessis notperfect. Therefore tohelp to fulfill the small industry requiremets for oyster
mushroom nursery, we are plannedatype offire tubeboilerthatcanhelpthe availability ofsteam ina
lowscalewithLPGfuelas a source ofheatenergy.
In general, thekettleisoftenusedtoassist foodproductionisfire tubeboilertype. Becauseof the
type offire tubeboilershaveseveraladvantages, ie. theconstruction is relativelymorerobust, lowmaintenance cost,
easyoperationandmaintenance, constructionboiler-making process can be madeat thesmall
workshopandthekettlehaveflexibilityinsettingandload changeduringoperation.
Boiler types comprises of fire tube, water tube, modular, coil tube and cast iron respectively. Steam
boilers could be used for various services, such as, steam process and heating, hot water heating, power
generation, petrochemical processes, chemical recovery, nuclear, just to mention a few[15]. Fire-tube boilers are
safer to use, require less expertise, and operate under lower pressures than water-tube boilers. Thus, they are
more suitable for small scale applications. Watertube boilers on the other hand, have a higher rate of steam
production and are easier to construct and transport [8].
They are designed to withstand the stress induced in the boilers [12]. In a boiler, water is heated, steam
is generated or superheated, or any combination thereof, under pressure or vacuum by the application of heat
Design with SolidWorks Software and Planning Calculation Analysis Of Fire Tube Boiler With Lpg-
www.ijres.org 45 | Page
resulting from the combustion of fuel (such as in a natural gas boiler), electrical resistance heating or the
recovery and conversion of normally unused energy [9].
Detailed theoretical analysis of the modified three pass dry back fire tube boiler was discussed and it
was found from the feasibility study that the proposed model could be expected to produced continuous and
constant steam input. It can be further expected to quicken the steam formation with higher efficiency and
minimum water loses. This proposed modified boiler could be used in food processing units, textile units etc.
with better productivity rates in future [2].
Based on the above issues and in terms of some of the results of research on fire-tube boiler, then in
this paper will be discuss how to perform heat transfer calculations and to determine a fire tube steam boilers
dimension planning with output capacity 70 kg / h, temperature 120 ℃ and pressure of 1.5 bar.
The purpose of this design is used to analyze the amount of heat transfer that occurs in the boiler and the
size dimensions are obtained to determine a draft boiler. The results obtained from the data steam output
capacity 70kg/h, temperature of 120 ℃ and pressure of 1.5 bar and to know the application of a fire tube boiler
in SMEs oyster mushroom.
II. METHODOLOGY
In this analysis and planning calculation, we will calculate the preliminary data previously retrieved and
complete with supporting data , which will be obtained a dimension of fire tube boiler .
Below are the steps - steps of data collection and planning dimensional shape of a fire tube boiler . To
clarify the flow of the final project and flow calculations and planning for fire tube boilers , can be seen in the
picture below .
Figure 1. Flowchart of Making Fire Tube Boilers
Design with SolidWorks Software and Planning Calculation Analysis Of Fire Tube Boiler With Lpg-
www.ijres.org 46 | Page
Figure 2. Flowchart of Calculation and Planning for Fire Tube Boilers
III. RESULTS AND DISCUSSION
Preliminary data are available :
ṁ_steam = ṁ_water = 70 kg / hour = 0.01944 kg / sec
T_steam = 120 ℃ = 393 ° K
T_water = 30 ℃ = 303 ° K
T_burning = 534 ℃ = 807 ° K
P_steam = 1.5 bar
III.1. Calculation of Heat Transfer
From Table A – 2 [5]:
The incoming water temperature the boiler is 30 º C thenthe price obtained for the enthalpy: h_inboiler
= 125.79 kJ / kg
From Table A – 4 [5,6]:
Temperature of 120 º C and a vapor pressure of 1.5 bar at exit of the boiler then the price obtained for
the enthalpy : h_outboiler = 2711.4 kJ / kg
Heat required by the Fire Tube Boilers
Q_boiler = m ( h_outboiler - h_inboiler )
Q_boiler = 50264.258 J / s
Analysis for ṁ_( flue gas ) and water average temperature absorbed ( T_cm ).All data obtained from Table
A - 4 [5] and Table A – 6 [5].
From Table A - 4 ( Air ) [5]:
𝑇𝑕𝑚 =
𝑇𝑠 + 𝑇∞
2
=
120 + 534
2
= 327℃
Design with SolidWorks Software and Planning Calculation Analysis Of Fire Tube Boiler With Lpg-
www.ijres.org 47 | Page
The data obtained:
𝐶𝑝 = 1051
𝐽
𝑘𝑔. °𝐾
𝜇 = 305,8 𝑥10−7
𝑁. 𝑠
𝑚2
𝑘 = 46,9 𝑥10−3
𝑊
𝑚. °𝐾
Pr = 0,685
From Table A –6 ( Water ) [5].
Assumption average temperature (T_cm ) ≈ 80 ℃ = 353 º K then the data obtained from interpolation as
follows :
𝐶𝑝 = 4197,4
𝐽
𝑘𝑔. °𝐾
𝜇 = 351,8 𝑥10−6
𝑁. 𝑠
𝑚2
𝑘 = 669,8 𝑥10−3
𝑊
𝑚. °𝐾
Pr = 2,2
 Search ṁ_flue gas with the following equation :
𝑄 𝑏𝑜𝑖𝑙𝑒𝑟 = 𝑄 𝑓𝑙𝑢𝑒 𝑔𝑎𝑠
𝑄 𝑓𝑙𝑢𝑒 𝑔𝑎𝑠 = ṁ𝑓𝑙𝑢𝑒 𝑔𝑎𝑠 . 𝐶𝑝. ∆𝑇
ṁ𝑓𝑙𝑢𝑒 𝑔𝑎𝑠 = 0,1155
𝑘𝑔
𝑠
 Actual Proven average temperature absorbed by the water temperature is assumed :
Q = ṁ𝑓𝑙𝑢𝑒 𝑔𝑎𝑠 . 𝐶𝑝 𝑇𝑐𝑖 − 𝑇𝑐𝑜
𝑇𝑐𝑜 =
𝑄
ṁ𝑓𝑙𝑢𝑒 𝑔𝑎𝑠 . 𝐶𝑝
+ 𝑇𝑐𝑖
𝑇𝑐𝑜 = 406,68 °𝐾 = 133,68 ℃
𝑇𝑐𝑚 =
𝑇𝑐𝑜 +𝑇 𝑐𝑖
2
=
133,68 ℃+30 ℃
2
= 81,84℃
( AssumptionsT_cm = 80 ℃ is fulfilled )
The selection of pipes available in the market are taken with the following specifications :
 Material = Carbon Steel Pipe Tubing Boilers ASME SA - 178A GRADE A / SA - 214 ( Plain Carbon )
 Nominal Diameter = 3-1/2 " ( 11 GA )
 Outside Diameter = 3.500 in = 88.9 mm = 0.0889 m
 Pipe thickness = 0.120 in = 3.048 mm = 0.003048 m
 Inside Diameter = 3.380 in = 85.852 mm = 0.085852 m
1. Flue Gas Flowing In The Pipeline
𝑅𝑒 𝐷 =
4.ṁ 𝑓𝑙𝑢𝑒 𝑔𝑎𝑠
𝜋.𝐷 𝑖.𝜇
= 56014,982
Due to the turbulent flow correlation " Internal Convection Flow " using the equation :
𝑁𝑢 𝐷 = 0,023 𝑅𝑒 𝐷
4
5
𝑃𝑟 𝑛
𝑁𝑢 𝐷 = 0,023 𝑅𝑒 𝐷
4
5
𝑃𝑟0,4
n = 0,4 untuk heating
𝑁𝑢 𝐷 = 124,350
Then correlation " Internal Convection Flow " is :
𝑕𝑖 = 𝑁𝑢 𝐷.
𝑘
𝐷 𝑖
= 67,931 𝑊 𝑚2
. °𝐾
2. Water Flow at Outside Pipe
Design with SolidWorks Software and Planning Calculation Analysis Of Fire Tube Boiler With Lpg-
www.ijres.org 48 | Page
𝑅𝑒 𝐷 =
4.ṁ 𝑎𝑖𝑟
𝜋.𝐷 𝑜 .𝜇
= 791,423
Due to the laminar flow correlation " External Convection Flow " using the equation :
𝑁𝑢 𝐷 = 𝐶 𝑅𝑒 𝐷
𝑚
𝑃𝑟
1
3 (C and m Data obtained in the equation constants table )
Table 1. Constants Equation
𝑁𝑢 𝐷 = 0,683 .791,4230,466
2,21 3
𝑁𝑢 𝐷 = 19,917
𝑕 𝑜 = 𝑁𝑢 𝐷.
𝑘
𝐷 𝑜
= 150,061 𝑊 𝑚2
. °𝐾
3. Conduction Happens In Pipe
Data Analysis for Carbon Steel Tubing Boilers ASME SA - 178A GRADE A / SA - 214 ( Plain Carbon
) obtained from Table A - 1 in the book " Fundamentals of Heat and Mass Transfer " price obtained is k =
48.0 W / ( m. ° K )
 conduction pipe:
𝑟 𝑖
𝑘
ln
𝑟 𝑜
𝑟 𝑖
= 3,06879 x 10−5
𝑊 𝑚2
. °𝐾
 Heat Transfer Coefficient:
U=
1
1
𝑘𝑜𝑛𝑣𝑒𝑘𝑠𝑖 𝑖𝑛𝑡𝑒𝑟𝑛𝑎𝑙
+ 𝑘𝑜𝑛𝑑𝑢𝑘𝑠𝑖 𝑝𝑖𝑝𝑎 +
1
𝑘𝑜𝑛𝑣𝑒𝑘𝑠𝑖 𝑒𝑘𝑠𝑡𝑒𝑟𝑛𝑎𝑙
U = 47,125 𝑊 𝑚2
. °𝐾
 Dimensions Length Pipe:
Pipe is considered a new pipe , so no fouling factor ( crust ) , then the length of the pipe :
∆𝑇𝑙𝑚 =
𝑇 𝑕 𝑖−𝑇𝑐𝑜 −(𝑇 𝑕 𝑜−𝑇 𝑐𝑖 )
ln
𝑇 𝑕 𝑖−𝑇 𝑐𝑜
(𝑇 𝑕 𝑜−𝑇 𝑐𝑖 )
= 207,926 ℃
L =
𝑄
𝑈.𝜋.𝐷 𝑖.∆𝑇 𝑙𝑚
= 8,223 m
4.Fire Tube Boiler Efficiency
𝜂𝑡𝑕𝑒𝑟𝑚𝑎𝑙 =
ṁ 𝑠𝑡𝑒𝑎𝑚 (𝑕 𝑜𝑢𝑡 − 𝑕𝑖𝑛 )
ṁ 𝑓𝑙𝑢𝑒 𝑔𝑎𝑠 𝑥 𝐿𝐻𝑉
𝑥 100%
𝜂𝑡𝑕𝑒𝑟𝑚𝑎𝑙 = 0,934 %
III.2. Planning Design Fire Tube Boilers with Solid Work Software
Dimensions of the data that have been obtained from the calculation , then the design of fire tube boiler
can be designed into 3D and with the SolidWork software.
As well as the body material is also determined boilers and pipes that are used to plan a fire tube boiler
. Here are the specifications of materials used for the body of the boiler and pipes in the boiler :
Design with SolidWorks Software and Planning Calculation Analysis Of Fire Tube Boiler With Lpg-
www.ijres.org 49 | Page
1. Boiler Materials:
a. Cold Rolled Carbon Structural Steel Sheet ASTM A611 GRADE E
b. Drum dimension :
 Plate thickness = 0.6 mm
 Drum length = 870 mm
 Drum Diameter = 500mm
2. Pipe material in Boiler
a. Carbon Steel Tubing Boilers ASME SA - 178A GRADE A / SA - 214 ( Plain Carbon )
b. The dimensions of the pipe diameter
 Nominal Diameter = 80 ( 10S )
 Outside Diameter = 88.9 mm = 0.0889 m
 Inside diameter = 85.852 mm = 0.085852 m
III.2.1.Dimensions of Fire Tube Boilers
Dimensions of Fire Tube Boilers can be planned from the total length of pipe that had been previously
calculated. For the dimensions of Fire Tube Boilers planning can begin searching for :
1. Number of pipes
Number of Fire Tube Boilers Pipe
=
Pipe length
body length boiler
= 12,273 ≈ 12 pipe
2. Plumbing Heating broad
The area of the heater on Fire Tube Boilers are :
The area of the heater = area x number of plumbing pipes
= ((𝜋 x r x 2) x (t x r)) x 12
= 99,811 𝑚2
3. Broad dimensions of the boiler body
Area of Fire Tube Boilers body dimensions are :
Broad dimensions of the boiler body = ((𝜋 x r x 2) x (t x r))
= 263,108 𝑚2
4. Volume weight effectively unused boiler
Fire Tube Boilers body volume that is effectively used :
Boiler body volume = volume of water height x volume of boiler body
=
3
4
𝜋 x 𝑟2
x t
= 98665644,28𝑚𝑚3
5. The volume of water required to fill the boiler body
The volume of water required to fill the body of Fire Tube Boilers are :
 Total volume of heating pipe
= 𝜋 x 𝑟2
x t x number of pipe = 49905619,62𝑚𝑚3
 The volume of water in the boiler body
= Volume of the boiler body - the total volume of heating pipe
= 48,760,024.66 mm3
6. Security analysis of drum boiler in terms of the comparison between the maximum capacity of internal
pressure asphalt drum boiler with a predetermined pressure .
Boiler body materials using bitumen drums with material Cold Rolled Carbon Structural Steel Sheet
ASTM A611 GRADE E.
 From the table Mechanical Properties of Steels Referred to in the 1996 AISI Specification will get
the price Yield Strength of the material .
Yield Strength ( Sy ) = 80 ksi = 552 MPa
 Factor of Safety ( SF ) is determined from the type of load , type of material , type of stress , and the
type of work that is being served . Because the boiler body material is made of stainless material
Design with SolidWorks Software and Planning Calculation Analysis Of Fire Tube Boiler With Lpg-
www.ijres.org 50 | Page
and the expenses incurred on the fire tube boilers including static load / Steady Load . SF prices are
obtained as follows :
Factor of Safety ( SF ) = 4
Normal Stress (𝜎) =
𝑆𝑦
𝑆𝐹
=
552 𝑀𝑃𝑎
4
= 138 MPa
7. Maximum internal pressure ofasphalt drum:
 Circumferential direction :
𝜎1 =
𝑃. 𝑟
𝑡
where:
r =radius of cylindrical body
t = thickness of the wall of the boiler body
P = internal pressure boiler
So,
P =
𝜎1. 𝑡
𝑟
=
138 𝑀𝑃𝑎 × 6𝑥10−4 𝑚
0,25 𝑚
= 0,3312MPa Figure 3. Circumferential direction of asphalt drum
= 3,312 Bar
 Longitudinal direction :
𝜎2 =
𝑃. 𝑟
2𝑡
P =
𝜎2. 2𝑡
𝑟
=
138 𝑀𝑃𝑎 × 2𝑥 6𝑥10−4 𝑚
0,25 𝑚
= 0,6624MPa
Figure 3. Circumferential direction of asphalt drum
= 6,624 Bar
From the calculation results can be proven that the boiler body made from asphalt drum is able to
withstand circumferential pressure of 3,312 bar and a longitudinal pressure of 6.624 bar, while the pressure in
the fire tube boiler that is planned at 1.5 Bar. It can be concluded that the asphalt drum made from Cold Rolled
Carbon Structural Steel Sheet ASTM A611 GRADE E is safe to use for fire tube boiler design.
III.2.2.1.Fire Tube Boiler Design in 3D
Design with SolidWorks Software and Planning Calculation Analysis Of Fire Tube Boiler With Lpg-
www.ijres.org 51 | Page
Figure 5. Plan Design for Fire Tube Boilers
III.2.2.2.Fire Tube Boiler Design in 2D ( Pieces )
Figure 6.Plan Design Dimensional for Fire Tube Boilers
III.3. Working Principle of Fire Tube Boilers
Fire tube boiler is a boiler where the flue gases of combustion are in the pipeline and water are in the
outer wall of the pipe , so that the steam produced is outside the pipe . Its working principle is:
1. Water treatment from water tank entering the bottom header boiler through feedwater pump in the first
passes through the water filter .
2. The water inbottom header and then enter the boiler and fill the space in between the outer wall of the pipe.
While the flue gas from the furnace / Firebox passed into the pipes contained within the boiler . Because of
the flue gas flowing inside the pipe and the outside wall of the pipe there is water , then the heat is located
in pipe, most of heat were given to the water in the boiler. Thus, the effect of the water heating process
turns into vapor.
3. After the phase change from water to steam in the boiler , the saturated steam exit from boiler through the
distribution pipes. While the rest of flue gas that has passed through the pipes in the boiler are forwarded to
the upper header and then discharged through the chimney.
Design with SolidWorks Software and Planning Calculation Analysis Of Fire Tube Boiler With Lpg-
www.ijres.org 52 | Page
IV. CONCLUSIONS
From the analysis calculations that have been done then can be deduced:
1. The results of calculation of heat transfer of available data and the selection of pipes for fire tube boilers
obtained results are displayed in the form of heat required by the boiler at 50264.258 J / s .
2. From the results of the calculation, the total length of pipe is 8.223 m , the number of pipes used as many as
12 pieces of pipe, Fire Tube Boilers body volume are used effectively by 98,665,644.28 mm3
and the
volume of water required to fill the body of Fire Tube Boilers 48,760,024.66 mm3
.
3. Based on the calculation of the efficiency of the fire tube boiler with LPG fuel obtained thermal efficiency
of 0.934 %.
4. From the calculation of the maximum capacity of internal pressure on asphalt drum , with a circular
pressure of 3.312 bar and a longitudinal pressure of 6.624 bar . It can be concluded that the asphalt drum
safe for use as a fire tube boiler body with a capacity of 1.5 bar pressure .
5. Thefire tubeboilerunits, good enough tobe able toreplacesteaming equipmentona small industrialoyster
mushroomsin particularsterilizationprocess.
6. Construction of fire tube boiler is very simple, so it is easy for maintenance .
ACKNOWLEDGEMENTS
Science for Society Program (IbM), the DIPA funded through the Directorate of Research and
Community Services, the Directorate General of Higher Education, Ministry of Education and Culture No.
0541/023-04.1.01/00/2011 Date December 9, 2011. As per the Letter of Agreement (Contract), No.
538.09/IT2.7/PM/2012.
REFERENCES
Journal Paper:
[1.] Saidur, R., Ahamed, J. U. and Masjuki, H. H.,“Energy, Exergy and Economic Analysis of Industrial Boilers”, Energy Policy, Vol. 38,
pp2188–2197, 2010.
[2.] Priobrata Kar.,Gurmail Singh., “Feasibility Study of Modified Three Pass Dry Back Reversal Chamber Fire-Tube Boiler”,
International Journal of Applied Research in Mechanical Engineering, Vol-1, Issue-1, 2011.
Books:
[3.] Byrney, Richard C. Turbular Exchanger Manufacturers Association, Inc. 25 North Broadway Tarrytown, New York 10591.
[4.] Hibbeler , R.C. Mechanics of Materials 8th Edition,Jhonwiley& sons, Inc.
[5.] Incropera, Frank P. etall.,Fundamental Of Heat And Mass Transfer seventh edition . New York :Jhonwiley& sons, Inc.
[6.] Moran, Michael J. & Shapiro, Howard N. Fundamentals of Engineering Thermodynamics 5th_edition,Jhonwiley& sons, Inc.
[7.] PurnaIrawan, Agustinus. Diktat ElemenMesin,UniversitasTarumanagara. 2009
[8.] Rajput R.K., Thermal Engineering, Laxmi Publications (P) Ltd., New Delhi, 2006.
[9.] Rawson W.R., Boiler. The Encyclopedia of Earth, 2008
[10.] Sarsetyanto, Joko. Diktat PerpindahanPanas,Surabaya : D3 TeknikMesin ITS.
[11.] Wai-Fah, Chen.Structural Engineering Ηανδβοοκ , Cold-Formed Steel Structures,CRC Press LLC, 1999
[12.] Woodruff E.B., Lammers H.B. and Lammers T.F.,Steam Plant Operation, 8th Edition. The McGraw-Hill Companies, 2004
Final Project:
[13.] Ridwan, et all. “KarakteristikKetelPipaApiKapasitasUap 6000Kg /Jam BerbahanBakar Solar di PT.MustikaRatu,
Tbk.”UniversitasGunadarma.
[14.] Rusnoto, “Perencanaanketeluaptekanan 6 atmdenganbahanbakarkayuuntukindustrisederhana”.
Symposium:
[15.] Mouchira Labidi, Julien Eynard, Olivier Faugeroux, Stéphane Grieu., “Optimal Design Of Thermal Storage Tanks For Multi-
Energy District Boilers”4th Inverse Problems, Design and Optimization Symposium (IPDO-2013), Albi, France, June 26-28,
2013

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Design With Solid works Software and Planning Calculation Analysis of Fire Tube Boiler With Lpg-Fuel For Oyster Mushroom Small Industries In Pacet, Mojokerto, East Java, Indonesia

  • 1. International Journal of Research in Engineering and Science (IJRES) ISSN (Online): 2320-9364, ISSN (Print): 2320-9356 www.ijres.org Volume 2 Issue 4 ǁ April. 2014 ǁ PP.44-52 www.ijres.org 44 | Page Design With Solid works Software and Planning Calculation Analysis of Fire Tube Boiler With Lpg-Fuel For Oyster Mushroom Small Industries In Pacet, Mojokerto, East Java, Indonesia Liza Rusdiyana1 , Sri Bangun S.2 , Denny M.E. Soedjono3 , Eddy Widiyono4 , Suhariyanto5 1 Department of 3 Diplome of Mechanical Engeneering, Industrial Engeneering Faculty, Institute of Technology Ten Nopember, Surabaya, 60111,Indonesia 2 Department of 3 Diplome of Mechanical Engeneering, Industrial Engeneering Faculty, Institute of Technology Ten Nopember, Surabaya, 60111,Indonesia 3 Department of 3 Diplome of Mechanical Engeneering, Industrial Engeneering Faculty, Institute of Technology Ten Nopember, Surabaya, 60111,Indonesia 4 Department of 3 Diplome of Mechanical Engeneering, Industrial Engeneering Faculty, Intitute of Technology Ten Nopember, Surabaya, 60111,Indonesia 5 Department of 3 Diplome of Mechanical Engeneering, Industrial Engeneering Faculty, Intitute of Technology Ten Nopember, Surabaya, 60111,Indonesia ABSTRACT: Steam boilers (boilers) is a closed vessel made of steel that is used to generate steam. In the modern era many industries such as household scale industries for the manufacture of oyster mushroom spawn to use aid as a supplier of steam boilers are used as a sterilization process baglog. Annually, the number of requests oyster mushroom spawn have been increases, so the boiler is very significant equipment to increase the number of baglog production as oyster mushroom growing media.To help to fulfill the small industryrequiremets for oyster mushroom nursery,plannedatype offire tubeboilerthatcanhelpthe availability ofsteam ina lowscalewithsteamoutputcapacity of70kg/ h, temperature120℃, pressure1.5barandusingmaterialsLPGfuelas a source ofheatenergy.From the results of this design, fire tube boiler have efficiency of 0.934 % . The kettle body is made from asphalt drums pertamina with the Cold Rolled Steel materials. Used asphalt drums because of its availability in the market more easier to obtained easily and the dimensions of asphalt drum capable of holding for temperature and pressure have been determined . As for the pipe material using Carbon Steel Tubing Boilers ASME SA - 178A GRADE A / SA - 214 (Plain Carbon). Keywords: Boiler, Fire-tube,Significant, Fuel,AsphaltDrum, Oyster Mushroom I. PREFACE Sterilizationof baglog as oyster mushroom mediais one of thevery important processinoystermushroom cultivationbecausethe mediahadcreatedusuallystill containsmanymicrobes, especiallywildmushrooms. Manycrop failurescaused bymediasterilizationprocessis less than perfect. Wildmushroomsthatstillexistinbaglogwill thriveandinhibitthe growth ofoyster mushroomif thesterilizationprocessis notperfect. Therefore tohelp to fulfill the small industry requiremets for oyster mushroom nursery, we are plannedatype offire tubeboilerthatcanhelpthe availability ofsteam ina lowscalewithLPGfuelas a source ofheatenergy. In general, thekettleisoftenusedtoassist foodproductionisfire tubeboilertype. Becauseof the type offire tubeboilershaveseveraladvantages, ie. theconstruction is relativelymorerobust, lowmaintenance cost, easyoperationandmaintenance, constructionboiler-making process can be madeat thesmall workshopandthekettlehaveflexibilityinsettingandload changeduringoperation. Boiler types comprises of fire tube, water tube, modular, coil tube and cast iron respectively. Steam boilers could be used for various services, such as, steam process and heating, hot water heating, power generation, petrochemical processes, chemical recovery, nuclear, just to mention a few[15]. Fire-tube boilers are safer to use, require less expertise, and operate under lower pressures than water-tube boilers. Thus, they are more suitable for small scale applications. Watertube boilers on the other hand, have a higher rate of steam production and are easier to construct and transport [8]. They are designed to withstand the stress induced in the boilers [12]. In a boiler, water is heated, steam is generated or superheated, or any combination thereof, under pressure or vacuum by the application of heat
  • 2. Design with SolidWorks Software and Planning Calculation Analysis Of Fire Tube Boiler With Lpg- www.ijres.org 45 | Page resulting from the combustion of fuel (such as in a natural gas boiler), electrical resistance heating or the recovery and conversion of normally unused energy [9]. Detailed theoretical analysis of the modified three pass dry back fire tube boiler was discussed and it was found from the feasibility study that the proposed model could be expected to produced continuous and constant steam input. It can be further expected to quicken the steam formation with higher efficiency and minimum water loses. This proposed modified boiler could be used in food processing units, textile units etc. with better productivity rates in future [2]. Based on the above issues and in terms of some of the results of research on fire-tube boiler, then in this paper will be discuss how to perform heat transfer calculations and to determine a fire tube steam boilers dimension planning with output capacity 70 kg / h, temperature 120 ℃ and pressure of 1.5 bar. The purpose of this design is used to analyze the amount of heat transfer that occurs in the boiler and the size dimensions are obtained to determine a draft boiler. The results obtained from the data steam output capacity 70kg/h, temperature of 120 ℃ and pressure of 1.5 bar and to know the application of a fire tube boiler in SMEs oyster mushroom. II. METHODOLOGY In this analysis and planning calculation, we will calculate the preliminary data previously retrieved and complete with supporting data , which will be obtained a dimension of fire tube boiler . Below are the steps - steps of data collection and planning dimensional shape of a fire tube boiler . To clarify the flow of the final project and flow calculations and planning for fire tube boilers , can be seen in the picture below . Figure 1. Flowchart of Making Fire Tube Boilers
  • 3. Design with SolidWorks Software and Planning Calculation Analysis Of Fire Tube Boiler With Lpg- www.ijres.org 46 | Page Figure 2. Flowchart of Calculation and Planning for Fire Tube Boilers III. RESULTS AND DISCUSSION Preliminary data are available : ṁ_steam = ṁ_water = 70 kg / hour = 0.01944 kg / sec T_steam = 120 ℃ = 393 ° K T_water = 30 ℃ = 303 ° K T_burning = 534 ℃ = 807 ° K P_steam = 1.5 bar III.1. Calculation of Heat Transfer From Table A – 2 [5]: The incoming water temperature the boiler is 30 º C thenthe price obtained for the enthalpy: h_inboiler = 125.79 kJ / kg From Table A – 4 [5,6]: Temperature of 120 º C and a vapor pressure of 1.5 bar at exit of the boiler then the price obtained for the enthalpy : h_outboiler = 2711.4 kJ / kg Heat required by the Fire Tube Boilers Q_boiler = m ( h_outboiler - h_inboiler ) Q_boiler = 50264.258 J / s Analysis for ṁ_( flue gas ) and water average temperature absorbed ( T_cm ).All data obtained from Table A - 4 [5] and Table A – 6 [5]. From Table A - 4 ( Air ) [5]: 𝑇𝑕𝑚 = 𝑇𝑠 + 𝑇∞ 2 = 120 + 534 2 = 327℃
  • 4. Design with SolidWorks Software and Planning Calculation Analysis Of Fire Tube Boiler With Lpg- www.ijres.org 47 | Page The data obtained: 𝐶𝑝 = 1051 𝐽 𝑘𝑔. °𝐾 𝜇 = 305,8 𝑥10−7 𝑁. 𝑠 𝑚2 𝑘 = 46,9 𝑥10−3 𝑊 𝑚. °𝐾 Pr = 0,685 From Table A –6 ( Water ) [5]. Assumption average temperature (T_cm ) ≈ 80 ℃ = 353 º K then the data obtained from interpolation as follows : 𝐶𝑝 = 4197,4 𝐽 𝑘𝑔. °𝐾 𝜇 = 351,8 𝑥10−6 𝑁. 𝑠 𝑚2 𝑘 = 669,8 𝑥10−3 𝑊 𝑚. °𝐾 Pr = 2,2  Search ṁ_flue gas with the following equation : 𝑄 𝑏𝑜𝑖𝑙𝑒𝑟 = 𝑄 𝑓𝑙𝑢𝑒 𝑔𝑎𝑠 𝑄 𝑓𝑙𝑢𝑒 𝑔𝑎𝑠 = ṁ𝑓𝑙𝑢𝑒 𝑔𝑎𝑠 . 𝐶𝑝. ∆𝑇 ṁ𝑓𝑙𝑢𝑒 𝑔𝑎𝑠 = 0,1155 𝑘𝑔 𝑠  Actual Proven average temperature absorbed by the water temperature is assumed : Q = ṁ𝑓𝑙𝑢𝑒 𝑔𝑎𝑠 . 𝐶𝑝 𝑇𝑐𝑖 − 𝑇𝑐𝑜 𝑇𝑐𝑜 = 𝑄 ṁ𝑓𝑙𝑢𝑒 𝑔𝑎𝑠 . 𝐶𝑝 + 𝑇𝑐𝑖 𝑇𝑐𝑜 = 406,68 °𝐾 = 133,68 ℃ 𝑇𝑐𝑚 = 𝑇𝑐𝑜 +𝑇 𝑐𝑖 2 = 133,68 ℃+30 ℃ 2 = 81,84℃ ( AssumptionsT_cm = 80 ℃ is fulfilled ) The selection of pipes available in the market are taken with the following specifications :  Material = Carbon Steel Pipe Tubing Boilers ASME SA - 178A GRADE A / SA - 214 ( Plain Carbon )  Nominal Diameter = 3-1/2 " ( 11 GA )  Outside Diameter = 3.500 in = 88.9 mm = 0.0889 m  Pipe thickness = 0.120 in = 3.048 mm = 0.003048 m  Inside Diameter = 3.380 in = 85.852 mm = 0.085852 m 1. Flue Gas Flowing In The Pipeline 𝑅𝑒 𝐷 = 4.ṁ 𝑓𝑙𝑢𝑒 𝑔𝑎𝑠 𝜋.𝐷 𝑖.𝜇 = 56014,982 Due to the turbulent flow correlation " Internal Convection Flow " using the equation : 𝑁𝑢 𝐷 = 0,023 𝑅𝑒 𝐷 4 5 𝑃𝑟 𝑛 𝑁𝑢 𝐷 = 0,023 𝑅𝑒 𝐷 4 5 𝑃𝑟0,4 n = 0,4 untuk heating 𝑁𝑢 𝐷 = 124,350 Then correlation " Internal Convection Flow " is : 𝑕𝑖 = 𝑁𝑢 𝐷. 𝑘 𝐷 𝑖 = 67,931 𝑊 𝑚2 . °𝐾 2. Water Flow at Outside Pipe
  • 5. Design with SolidWorks Software and Planning Calculation Analysis Of Fire Tube Boiler With Lpg- www.ijres.org 48 | Page 𝑅𝑒 𝐷 = 4.ṁ 𝑎𝑖𝑟 𝜋.𝐷 𝑜 .𝜇 = 791,423 Due to the laminar flow correlation " External Convection Flow " using the equation : 𝑁𝑢 𝐷 = 𝐶 𝑅𝑒 𝐷 𝑚 𝑃𝑟 1 3 (C and m Data obtained in the equation constants table ) Table 1. Constants Equation 𝑁𝑢 𝐷 = 0,683 .791,4230,466 2,21 3 𝑁𝑢 𝐷 = 19,917 𝑕 𝑜 = 𝑁𝑢 𝐷. 𝑘 𝐷 𝑜 = 150,061 𝑊 𝑚2 . °𝐾 3. Conduction Happens In Pipe Data Analysis for Carbon Steel Tubing Boilers ASME SA - 178A GRADE A / SA - 214 ( Plain Carbon ) obtained from Table A - 1 in the book " Fundamentals of Heat and Mass Transfer " price obtained is k = 48.0 W / ( m. ° K )  conduction pipe: 𝑟 𝑖 𝑘 ln 𝑟 𝑜 𝑟 𝑖 = 3,06879 x 10−5 𝑊 𝑚2 . °𝐾  Heat Transfer Coefficient: U= 1 1 𝑘𝑜𝑛𝑣𝑒𝑘𝑠𝑖 𝑖𝑛𝑡𝑒𝑟𝑛𝑎𝑙 + 𝑘𝑜𝑛𝑑𝑢𝑘𝑠𝑖 𝑝𝑖𝑝𝑎 + 1 𝑘𝑜𝑛𝑣𝑒𝑘𝑠𝑖 𝑒𝑘𝑠𝑡𝑒𝑟𝑛𝑎𝑙 U = 47,125 𝑊 𝑚2 . °𝐾  Dimensions Length Pipe: Pipe is considered a new pipe , so no fouling factor ( crust ) , then the length of the pipe : ∆𝑇𝑙𝑚 = 𝑇 𝑕 𝑖−𝑇𝑐𝑜 −(𝑇 𝑕 𝑜−𝑇 𝑐𝑖 ) ln 𝑇 𝑕 𝑖−𝑇 𝑐𝑜 (𝑇 𝑕 𝑜−𝑇 𝑐𝑖 ) = 207,926 ℃ L = 𝑄 𝑈.𝜋.𝐷 𝑖.∆𝑇 𝑙𝑚 = 8,223 m 4.Fire Tube Boiler Efficiency 𝜂𝑡𝑕𝑒𝑟𝑚𝑎𝑙 = ṁ 𝑠𝑡𝑒𝑎𝑚 (𝑕 𝑜𝑢𝑡 − 𝑕𝑖𝑛 ) ṁ 𝑓𝑙𝑢𝑒 𝑔𝑎𝑠 𝑥 𝐿𝐻𝑉 𝑥 100% 𝜂𝑡𝑕𝑒𝑟𝑚𝑎𝑙 = 0,934 % III.2. Planning Design Fire Tube Boilers with Solid Work Software Dimensions of the data that have been obtained from the calculation , then the design of fire tube boiler can be designed into 3D and with the SolidWork software. As well as the body material is also determined boilers and pipes that are used to plan a fire tube boiler . Here are the specifications of materials used for the body of the boiler and pipes in the boiler :
  • 6. Design with SolidWorks Software and Planning Calculation Analysis Of Fire Tube Boiler With Lpg- www.ijres.org 49 | Page 1. Boiler Materials: a. Cold Rolled Carbon Structural Steel Sheet ASTM A611 GRADE E b. Drum dimension :  Plate thickness = 0.6 mm  Drum length = 870 mm  Drum Diameter = 500mm 2. Pipe material in Boiler a. Carbon Steel Tubing Boilers ASME SA - 178A GRADE A / SA - 214 ( Plain Carbon ) b. The dimensions of the pipe diameter  Nominal Diameter = 80 ( 10S )  Outside Diameter = 88.9 mm = 0.0889 m  Inside diameter = 85.852 mm = 0.085852 m III.2.1.Dimensions of Fire Tube Boilers Dimensions of Fire Tube Boilers can be planned from the total length of pipe that had been previously calculated. For the dimensions of Fire Tube Boilers planning can begin searching for : 1. Number of pipes Number of Fire Tube Boilers Pipe = Pipe length body length boiler = 12,273 ≈ 12 pipe 2. Plumbing Heating broad The area of the heater on Fire Tube Boilers are : The area of the heater = area x number of plumbing pipes = ((𝜋 x r x 2) x (t x r)) x 12 = 99,811 𝑚2 3. Broad dimensions of the boiler body Area of Fire Tube Boilers body dimensions are : Broad dimensions of the boiler body = ((𝜋 x r x 2) x (t x r)) = 263,108 𝑚2 4. Volume weight effectively unused boiler Fire Tube Boilers body volume that is effectively used : Boiler body volume = volume of water height x volume of boiler body = 3 4 𝜋 x 𝑟2 x t = 98665644,28𝑚𝑚3 5. The volume of water required to fill the boiler body The volume of water required to fill the body of Fire Tube Boilers are :  Total volume of heating pipe = 𝜋 x 𝑟2 x t x number of pipe = 49905619,62𝑚𝑚3  The volume of water in the boiler body = Volume of the boiler body - the total volume of heating pipe = 48,760,024.66 mm3 6. Security analysis of drum boiler in terms of the comparison between the maximum capacity of internal pressure asphalt drum boiler with a predetermined pressure . Boiler body materials using bitumen drums with material Cold Rolled Carbon Structural Steel Sheet ASTM A611 GRADE E.  From the table Mechanical Properties of Steels Referred to in the 1996 AISI Specification will get the price Yield Strength of the material . Yield Strength ( Sy ) = 80 ksi = 552 MPa  Factor of Safety ( SF ) is determined from the type of load , type of material , type of stress , and the type of work that is being served . Because the boiler body material is made of stainless material
  • 7. Design with SolidWorks Software and Planning Calculation Analysis Of Fire Tube Boiler With Lpg- www.ijres.org 50 | Page and the expenses incurred on the fire tube boilers including static load / Steady Load . SF prices are obtained as follows : Factor of Safety ( SF ) = 4 Normal Stress (𝜎) = 𝑆𝑦 𝑆𝐹 = 552 𝑀𝑃𝑎 4 = 138 MPa 7. Maximum internal pressure ofasphalt drum:  Circumferential direction : 𝜎1 = 𝑃. 𝑟 𝑡 where: r =radius of cylindrical body t = thickness of the wall of the boiler body P = internal pressure boiler So, P = 𝜎1. 𝑡 𝑟 = 138 𝑀𝑃𝑎 × 6𝑥10−4 𝑚 0,25 𝑚 = 0,3312MPa Figure 3. Circumferential direction of asphalt drum = 3,312 Bar  Longitudinal direction : 𝜎2 = 𝑃. 𝑟 2𝑡 P = 𝜎2. 2𝑡 𝑟 = 138 𝑀𝑃𝑎 × 2𝑥 6𝑥10−4 𝑚 0,25 𝑚 = 0,6624MPa Figure 3. Circumferential direction of asphalt drum = 6,624 Bar From the calculation results can be proven that the boiler body made from asphalt drum is able to withstand circumferential pressure of 3,312 bar and a longitudinal pressure of 6.624 bar, while the pressure in the fire tube boiler that is planned at 1.5 Bar. It can be concluded that the asphalt drum made from Cold Rolled Carbon Structural Steel Sheet ASTM A611 GRADE E is safe to use for fire tube boiler design. III.2.2.1.Fire Tube Boiler Design in 3D
  • 8. Design with SolidWorks Software and Planning Calculation Analysis Of Fire Tube Boiler With Lpg- www.ijres.org 51 | Page Figure 5. Plan Design for Fire Tube Boilers III.2.2.2.Fire Tube Boiler Design in 2D ( Pieces ) Figure 6.Plan Design Dimensional for Fire Tube Boilers III.3. Working Principle of Fire Tube Boilers Fire tube boiler is a boiler where the flue gases of combustion are in the pipeline and water are in the outer wall of the pipe , so that the steam produced is outside the pipe . Its working principle is: 1. Water treatment from water tank entering the bottom header boiler through feedwater pump in the first passes through the water filter . 2. The water inbottom header and then enter the boiler and fill the space in between the outer wall of the pipe. While the flue gas from the furnace / Firebox passed into the pipes contained within the boiler . Because of the flue gas flowing inside the pipe and the outside wall of the pipe there is water , then the heat is located in pipe, most of heat were given to the water in the boiler. Thus, the effect of the water heating process turns into vapor. 3. After the phase change from water to steam in the boiler , the saturated steam exit from boiler through the distribution pipes. While the rest of flue gas that has passed through the pipes in the boiler are forwarded to the upper header and then discharged through the chimney.
  • 9. Design with SolidWorks Software and Planning Calculation Analysis Of Fire Tube Boiler With Lpg- www.ijres.org 52 | Page IV. CONCLUSIONS From the analysis calculations that have been done then can be deduced: 1. The results of calculation of heat transfer of available data and the selection of pipes for fire tube boilers obtained results are displayed in the form of heat required by the boiler at 50264.258 J / s . 2. From the results of the calculation, the total length of pipe is 8.223 m , the number of pipes used as many as 12 pieces of pipe, Fire Tube Boilers body volume are used effectively by 98,665,644.28 mm3 and the volume of water required to fill the body of Fire Tube Boilers 48,760,024.66 mm3 . 3. Based on the calculation of the efficiency of the fire tube boiler with LPG fuel obtained thermal efficiency of 0.934 %. 4. From the calculation of the maximum capacity of internal pressure on asphalt drum , with a circular pressure of 3.312 bar and a longitudinal pressure of 6.624 bar . It can be concluded that the asphalt drum safe for use as a fire tube boiler body with a capacity of 1.5 bar pressure . 5. Thefire tubeboilerunits, good enough tobe able toreplacesteaming equipmentona small industrialoyster mushroomsin particularsterilizationprocess. 6. Construction of fire tube boiler is very simple, so it is easy for maintenance . ACKNOWLEDGEMENTS Science for Society Program (IbM), the DIPA funded through the Directorate of Research and Community Services, the Directorate General of Higher Education, Ministry of Education and Culture No. 0541/023-04.1.01/00/2011 Date December 9, 2011. As per the Letter of Agreement (Contract), No. 538.09/IT2.7/PM/2012. REFERENCES Journal Paper: [1.] Saidur, R., Ahamed, J. U. and Masjuki, H. H.,“Energy, Exergy and Economic Analysis of Industrial Boilers”, Energy Policy, Vol. 38, pp2188–2197, 2010. [2.] Priobrata Kar.,Gurmail Singh., “Feasibility Study of Modified Three Pass Dry Back Reversal Chamber Fire-Tube Boiler”, International Journal of Applied Research in Mechanical Engineering, Vol-1, Issue-1, 2011. Books: [3.] Byrney, Richard C. Turbular Exchanger Manufacturers Association, Inc. 25 North Broadway Tarrytown, New York 10591. [4.] Hibbeler , R.C. Mechanics of Materials 8th Edition,Jhonwiley& sons, Inc. [5.] Incropera, Frank P. etall.,Fundamental Of Heat And Mass Transfer seventh edition . New York :Jhonwiley& sons, Inc. [6.] Moran, Michael J. & Shapiro, Howard N. Fundamentals of Engineering Thermodynamics 5th_edition,Jhonwiley& sons, Inc. [7.] PurnaIrawan, Agustinus. Diktat ElemenMesin,UniversitasTarumanagara. 2009 [8.] Rajput R.K., Thermal Engineering, Laxmi Publications (P) Ltd., New Delhi, 2006. [9.] Rawson W.R., Boiler. The Encyclopedia of Earth, 2008 [10.] Sarsetyanto, Joko. Diktat PerpindahanPanas,Surabaya : D3 TeknikMesin ITS. [11.] Wai-Fah, Chen.Structural Engineering Ηανδβοοκ , Cold-Formed Steel Structures,CRC Press LLC, 1999 [12.] Woodruff E.B., Lammers H.B. and Lammers T.F.,Steam Plant Operation, 8th Edition. The McGraw-Hill Companies, 2004 Final Project: [13.] Ridwan, et all. “KarakteristikKetelPipaApiKapasitasUap 6000Kg /Jam BerbahanBakar Solar di PT.MustikaRatu, Tbk.”UniversitasGunadarma. [14.] Rusnoto, “Perencanaanketeluaptekanan 6 atmdenganbahanbakarkayuuntukindustrisederhana”. Symposium: [15.] Mouchira Labidi, Julien Eynard, Olivier Faugeroux, Stéphane Grieu., “Optimal Design Of Thermal Storage Tanks For Multi- Energy District Boilers”4th Inverse Problems, Design and Optimization Symposium (IPDO-2013), Albi, France, June 26-28, 2013