evaluation of granular fertilizer boom sprayer
TRANSCRIPT
i
EVALUATION OF GRANULAR FERTILIZER BOOM SPRAYER
PERFORMANCE VIA COMPUTATIONAL SIMULATION
AHMAD FARIQIN B. ABD MALEK
A thesis is submitted of the fulfillment of the requirements
For the award of the Degree of Master of Mechanical
Engineering
FACULTY OF MECHANICAL AND MANUFACTURING ENGINEERING
UNIVERSITY TUN HUSSIEN ONN MALAYSIA
JUNE 2015
v
ABSTRACT
Granular boom sprayer has been used by large scaled farmers for centuries. This
machine is used to repel or fertilize their crops. In MARDI, they used 3 types of
fertilizer that is Nitrogen, N, Phosphorus, P and Potassium, K. Those 3 types of particles
have been simulated by using Ansys software and the results show that potassium, K
fertilizer not scattered to the ground and the others 2 fertilizers are conversely. The
uniformity of the distribution of granular fertilizer was carried out with a reasonable
range of variables. Various methods have been used to study the efficiency of the spray
boom design on through simulation software and lab approach. In this work, the
simulation of the particles in the boom sprayer is performed from the boom sprayer
entering until the exit and distributed to the ground. The simulation is performed by
using ANSYS CFX based on the Taguchi method. Taguchi method have been used in
this study. For the orthogonal array, since this case study consists of 4 level and 5 factor,
L‟16 was used for the simulation process. This simulation utilize only one fertilizer that
contained all types of the basic NPK fertilizer. The parameters are involved the granular
diameter size, air velocity at the inlet, blow head distance, height of collecting plate and
width of collecting plate. Results shows that the air velocity must be kept higher when
the diameter of particle increases. Collecting plates with excessive height and width can
cause the velocity fertilizer to drop and the particles fail to distribute well. Furthermore,
furthers distance between the boom section can also cause the particles to scattered
unevenly onto the ground. The most desired simulation result was achieved with 1.5 mm
diameter particles, air velocity 8 m/s, distance between boom section is 200 mm and
height and width of collecting plate is 14 mm and 10 mm. Particle scattered well and the
average of the particle at the first exit until last exit of boom section were observed to be
evenly distributed.
vi
ABSTRAK
Penyembur bebutir bum telah digunakan oleh petani yang mempunyai ladang selama
berabad lamanya. Di MARDI, mereka menggunakan 3 jenis baja iaitu Nitrogen, N,
Fosforus, P dan Kalium, K. 3 jenis baja telah disimulasi dengan menggunakan perisian
ANSYS dan keputusan menunjukkan bahawa baja kalium, K tidak bertaburan ke tanah
dan baja yang lain adalah sebaliknya. Pelbagai kaedah telah digunakan untuk mengkaji
kecekapan ledakan semburan pada kaedah pembuatan, perisian simulasi dan pendekatan
makmal. Simulasi baja dalam penyembur bum dari bahagian masukan penyembur bum
sehingga bahagian keluaran dan disemburkan ke tanah. Kaedah Taguchi telah digunakan
dalam kajian ini. Untuk susunan ortogon, kajian ini terdiri daripada 4 tahap dan 5
faktor, L'16 telah digunakan untuk proses simulasi. Simulasi ini menggunakan hanya
satu baja yang mengandungi semua jenis baja asas NPK. Parameter yang terlibat ialah
diameter saiz berbutir, halaju udara di bahagian masukan, jarak bahagian bum keluaran,
ketinggian dan lebar plat pengumpul. Keputusan menunjukkan bahawa halaju udara
mesti lebih tinggi apabila diameter baja bertambah. Plat pengumpul dengan ketinggian
dan lebar yang berlebihan boleh menyebabkan halaju baja menurun dan baja gagal
berterabur dengan baik. Jarak antara bahagian keluaran bum juga boleh menyebabkan
baja bertabur tidak sekata ke atas tanah. Hasil simulasi yang paling diingini telah dicapai
dengan saiz diameter baja 1.5 mm, halaju udara 8 m/s, jarak antara bahagian keluaran
bum adalah 200 mm dan ketinggian dan lebar plat pengumpul adalah 14 mm dan 10
mm. Baja yang bertaburan dengan baik dan purata baja di bahagian keluaran yang
pertama sehingga keluaran terakhir diagihkan sama rata.
vii
CONTENTS
TITLE i
DECLARATION ii
DEDICATION iii
ACKNOWLEDGEMENT iv
ABSTRACT v
ABSTRAK vi
CONTENTS vii
LIST OF TABLES xi
LIST OF FIGURES xii
LIST OF SYMBOLS xvii
LIST OF APPENDICES xviii
CHAPTER 1 INTRODUCTION
1.1 Introduction 1
1.2 Problem Statement 3
1.3 Significant of study 3
1.4 Objective and scope of study 5
CHAPTER 2 LITERITURE REVIEW
2.1 Granular Fertilizer Boom Sprayer 5
2.2 Nozzle and Blow head 6
viii
2.3 Pipe selection for granular material 8
2.4 Particle size and shape 9
2.5 Computing Fluid Dynamics Software 10
2.6 Benefits of CFD software 11
2.6.1 CFD Process 12
2.6.1.1 Preprocessing 12
2.6.1.2 Solver 12
2.6.1.3 Post processing 13
2.7 Flow in pipe 13
2.8 Design of experiment 14
2.8.1 Full factorial method 15
2.8.2 Advantages and Disadvantages
Full factorial method 17
2.9 Design of experiment via Taguchi method 17
2.9.1 General step for taguchi method 19
2.9.2 Types of Orthogonal Array 19
2.9.3 Advantages and disadvantages Taguchi method 20
2.10 Determining Parameter Design Orthogonal Array 20
2.11 NPK Fertilizer 22
CHAPTER 3 METHODOLOGY
3.1 Introduction 24
3.2 Methodology Flow Chart 26
3.3 Computational Modeling Using Solid Works 27
3.4 Computational modeling of the pipe and
blow head using Solid works 27
3.5 Parameter of pipe and blow head 28
3.6 Simulation using ANSYS Software 30
3.6.1 Meshing 30
3.6.2 Preprocessor 32
ix
3.7 Parameter selection 35
3.6.4 Post processer 35
3.6.3 Solver 35
3.8 Orthogonal Array 36
3.9 Grid Independency test 39
CHAPTER 4 RESULT AND DISCUSSION
4.1 Introduction 40
4.2 Grid Independence Test 41
4.3 Simulation the actual situation at MARDI 42
4.3.1 Analysis of NPK Distribution 48
4.4 Simulation of particle distribution using
Taguchi Method 48
4.4.1 Simulation No 1 48
4.4.2 Simulation No 2 51
4.4.3 Simulation No 3 55
4.4.4 Simulation No 4 59
4.4.5 Simulation No 5 62
4.4.6 Simulation No 6 65
4.4.7 Simulation No 7 71
4.4.8 Simulation No 8 75
4.4.9 Simulation No 9 79
4.4.10 Simulation No 10 82
4.4.11 Simulation No 11 87
4.4.12 Simulation No 12 91
4.4.13 Simulation No 13 95
4.4.14 Simulation No 14 98
4.4.15 Simulation No 15 102
4.4.16 Simulation No 16 107
4.5 Parameter Analysis 111
x
4.5.1 Size of Particles and Air velocity 111
4.5.2 Height and width of collecting plate 112
4.5.3 Blow head arrangement 115
CHAPTER 5 CONCLUSION AND RECOMENDATION
5.1 Conclusion 117
5.2 Simulation for NPK fertilizer 118
5.3 Simulation using Taguchi method 118
5.4 Recommendation 119
REFERENCES 120
APPENDICES 124
xi
LIST OF TABLE
Table 2.1 Parameter for example 16
Table 2.2 Test matrix 16
Table 2.3 Advantages and disadvantages of Full Factorial method 17
Table 2.4 Advantages and disadvantages of Taguchi method 20
Table 2.5 The Spindle Speed 21
Table 2.6 Selector Array 21
Table 2.7 L9 Array select 21
Table 2.8 L9 array table of experiment 22
Table 2.9 NPK specification 23
Table 3.1 Parameter for pipe and blow head 29
Table 3.2 Meshing parameter 30
Table 3.3 Setting the properties for the blow head and pipe. 34
Table 3.4 Parameter for Boom sprayer. 36
Table 3.5 Array selector 36
Table 3.6 Choose L27 from array selector 37
Table 3.7 Orthogonal array L‟16 37
Table 3.8 Number of experiment according Orthogonal Array 38
Table 4.1 Different grid size with number of elements and nodes. 41
xii
Table 4.2 Fertilizer properties 42
Table 4.3 Particle size and air velocity 111
xiii
LIST OF FIGURE
Figure 2.1 A prototype of granular boom sprayer. 6
Figure 2.2 Nozzle Manifold. 7
Figure 2.3 Blow Head with collecting plate 30º. 8
Figure 2.4 Circular PVC pipe. 9
Figure 2.5 Different size of particles. 9
Figure 2.6 Simulation of flow in pipe using CFD software. 11
Figure 2.7 Reynold Number. 13
Figure 2.8 Laminar and turbulent flow. 14
Figure 2.9 Example of Level and factor. 15
Figure 3.1 Flow chart of the process for this study. 26
Figure 3.1 Pipe and blow head design. 28
Figure 3.2 Dimension for pipe and blow head. 29
Figure 3.3 Before sizing the meshing. 31
Figure 3.4 After sizing the meshing. 32
Figure 3.5 Setting boundaries. 33
Figure 4.1 Drawing actual boom sprayer using Solid Work. 42
Figure 4.3 Nitrogen, N Particle Track Distribution. 43
Figure 4.2 Air Velocity. 44
xiv
Figure 4.3 Phosphorus, P Particle Track Distribution. 45
Figure 4.4 Potassium, K Particle Track Distribution. 46
Figure 4.5 NPK Particle Track Distribution. 47
Figure 4.6 Particle Distribution Track for Simulation 1. 49
Figure 4.7 Air velocity and Particle Distribution Track
For simualtion no 1. 50
Figure 4.8 Particle Distribution Track for Simulation 2. 52
Figure 4.9 Air velocity and Particle Distribution Track
For simulation no 2. 53
Figure 4.10 Particle Distribution at the end of Boom Sprayer. 54
Figure 4.11 Particle Distribution Track for Simulation 3. 55
Figure 4.12 Air velocity and Particle Distribution Track
For simulation no 3. 57
Figure 4.13 Particle Distribution at the end of Boom Sprayer. 58
Figure 4.14 Particle Distribution Track for Simulation 4. 59
Figure 4.15 Air velocity and Particle Distribution Track
For simulation no 4. 61
Figure 4.16 Particle Distribution at the end of Boom Sprayer. 62
Figure 4.17 Particle Distribution Track for Simulation 5. 63
Figure 4.18 Air velocity and Particle Distribution Track
For simulation no 5. 65
Figure 4.19 Particle Distribution Track for Simulation 6. 67
Figure 4.20 Air velocity and Particle Distribution Track
For simulation no 6. 69
xv
Figure 4.21 Particle Distribution at the end of Boom Sprayer. 70
Figure 4.22 Particle Distribution Track for Simulation 7. 71
Figure 4.23 Air velocity and Particle Distribution Track
For simulation no 7. 73
Figure 4.24 Particle Distribution at the end of Boom Sprayer. 74
Figure 4.25 Particle Distribution Track for Simulation 8. 75
Figure 4.26 Air velocity and Particle Distribution Track
For simulation no 8. 77
Figure 4.27 Particle Distribution at the end of Boom Sprayer. 78
Figure 4.28 Particle Distribution Track for Simulation 9. 79
Figure 4.29 Air velocity and Particle Distribution Track
For simulation no 9. 81
Figure 4.30 Particle Distribution Track for Simulation 10. 83
Figure 4.31 Air velocity and Particle Distribution Track
For simulation no 10. 85
Figure 4.32 Particle Distribution at the end of Boom Sprayer. 86
Figure 4.33 Particle Distribution Track for Simulation 11. 87
Figure 4.34 Air velocity and Particle Distribution Track
For simulation no 11. 89
Figure 4.35 Particle Distribution at the end of Boom Sprayer. 90
Figure 4.36 Particle Distribution Track for Simulation 12. 91
Figure 4.37 Air velocity and Particle Distribution Track
For simulation no 12. 93
Figure 4.38 Particle Distribution at the end of Boom Sprayer. 94
xvi
Figure 4.39 Particle Distribution Track for Simulation 13. 95
Figure 4.40 Air velocity and Particle Distribution Track
For simulation no 13. 97
Figure 4.41 Particle Distribution Track for Simulation 14. 99
Figure 4.42 Air velocity and Particle Distribution Track
For simulation no 14. 101
Figure 4.43 Particle Distribution at the end of Boom Sprayer. 102
Figure 4.44 Particle Distribution Track for Simulation 15. 103
Figure 4.45 Air velocity and Particle Distribution Track
For simulation no 15. 105
Figure 4.46 Particle Distribution at the end of Boom Sprayer. 106
Figure 4.47 Particle Distribution Track for Simulation 16. 107
Figure 4.48 Air velocity and Particle Distribution Track
For simulation no 16. 109
Figure 4.49 Particle Distribution at the end of Boom Sprayer. 110
Figure 4.50 Particle size versus Air velocity graph. 112
Figure 4.51 Height and width comparison 1. 113
Figure 4.52 Height and width comparison 2. 114
Figure 4.53 Comparison between distances of boom section. 115
xviii
LIST OF SYMBOL
CFD - Computational Fluid Dynamics
Re - Reynold Number
ρ - Ketumpatan, kg/m³
μ - Kelikatan dinamik, kg/(m*s)
ν - Kelikatan kinematik, m²/s
V - Halaju purata, m/s
D - Diameter, m
3D - 3 Dimensi
Mm - Milimeter
xviii
LIST OF APPENDICES
BOOM SPRAYER 1 125
BOOM SPRAYER 2 126
GANTT CHART PS 1 127
GANTT CHART PS 2 128
1
CHAPTER 1
INTRODUCTION
1.1 Introduction
In agriculture, the process of fertilizing and fumigating insects is one of the most
important processes. This can help farmers to harvest more quality crop. In the early
1800s, most of the pesticides and fertilizer applications are carried out manually [1].
This method requires number of workers if the agricultural area was spacious. As a
result, it would involve high costs.
2
In the mid-1800s, the group of researchers has succeeded in producing a
knapsack sprayer. Knapsack sprayer can help farmers with this tool just need to bear
filled with poison or steel. Farmers only need to pump and nozzle tip pointing in the
desired direction. Even so, the development of more advanced agricultural technologies.
In the late 1800s, the first spray machines have been introduced [1]. This
machine does not require human power, it depends on the machine but must be
controlled by farmers.Advances in agricultural technology is growing and today has
many machines and methods have been introduced by researchers to facilitate
agricultural work. Sprayers usually consist of basic parts such as tanks, delivery pipe,
pump, boom and nozzles [1].
Granular boom sprayer has been used by farmers who have a farm or a wide
area. This machine is used to repel or fertilize their crops. This machine has been studied
by researchers for several decades. They study in terms of the efficiency of the system to
reduce the error to be a problem to them. Many changes have been made, especially in
the design of the sprayer boom although the results show that the role of variable rate
plays an important role in influencing the rate of distribution of granular uniformity [2].
As a result, the uniformity of the distribution of granular fertilizer was carried
out with a reasonable range of variables. Various methods have been used to study the
efficiency of the spray boom design on manufacturing methods, simulation software and
lab approach.
In the modern world of technology, have a lot of software that can examine and
give an overview on the parts that have been studied. In addition, the results from these
experiments can be compared against variable rate difference. Some examples of
software that can be used as CFD software, AMIRA, mathlab, Lisa software, Tecplot,
and more. Calculations and experiments carried out using a computer to simulate
3
reaction or the reaction between granular particles and the air based on the specified
settings of boundary conditions.
Fluid dynamics is a field of science that studies the physical laws governing the
flow of fluid under various conditions. In this study, Computational Fluid Dynamics
software, better known as CFD has been used to study the air and particle flow in a pipe
and then at the exit blow head.
CFD is a software that makes the prediction of fluid flow by means of
mathematical modeling (partial differential equations), numerical methods
(discretization and solution technique) and software tools, namely (preprocessing, solver
and post processing). Additionally, CFD can also help scientists and engineer for carry
out experiments in a „virtual flow laboratory‟.
Continuous research will improve the efficiency of the design in terms of the
geometry boom sprayer and air flow. Besides, using High Speed computer will affect the
the answers more precise.
1.2 Problem statement
Boom sprayer is used to distribute crop. In this study the focused, fertilizer used is
granular and pushed by high pressure air to scattered the fertilizer falls into place to be
fertilized. But the spray fertilizer uniformity is a problem to researchers because
fertilizer falls on the ground are not uniform. It causes the plant to grow irregular. This
study to examine the uniformity the spray granular fertilizer using a variety of high-
pressure air. In addition, in this study to modify the design boom sprayer to uniformity
spray fertilizer on the areas that have been sprayed. This studies have to go through three
stages which is pre-processing, solver and post-processing to achieve the result.
4
1.3 Significant of study
This study can be obtained as a result of various designs boom sprayer with an effective
and more efficient as well as cost effective research. The success of this study will be
beneficial to the agricultural sector to achieve uniformity in the distribution of granular
boom sprayer. In addition, it can help other researchers who study the granular flow in
the pipe. Besides, using software that has been developed, it can help or advice for the
best solution to achieved the goal of the experiment.
By using software, can simulated the result and also can cut the cost before go to
the actual part and its call Virtual Engineering. It can help to perform the experiment
without carry out the cost of the experiment and just using software can find the result.
Besides, it can help to reduce the time of the making the product. Futhermore, various
design of boom sprayer can be made and help the researcher to find the best and most
effective design.
1.4 Objective and scope of study
The objective of this study is to:
1. To evaluate the existing boom sprayer design for effectiveness of the granular
flow through and out the boom sprayer.
2. To design a new boom sprayer mechanism for optimum granular fertilizer
distribution.
3. To suggest and improve the boom sprayer design to achieve a better efficiency
levels for MARDI.
5
To avoid diverted research objectives, some scope of study was created to be guidelines
to achieve the above objectives:
1. Using ANSYS CFD CFX software
2. Analyzing the fertilizer particle movement from the inlet to the outlet of boom
sprayer section.
3. Blow head diameter is 32 mm.
4. Air velocity at 1 m/s, 3 m/s, 5 m/s and 8 m/s.
5. Diameter particle 1 mm, 1.5 mm, 2 mm and 2.5 mm.
6. Collecting plate angle 60º.
7. Height of collecting plate 10 mm, 14 mm, 18 mm and 22 mm.
8. Width of collecting plate 10 mm, 15 mm, 20 mm and 25 mm
9. Use cylinder boom shape.
6
CHAPTER 2
LITERATURE REVIEW
2.1 Granular Fertilizer Boom Sprayer
In agriculture, engineering may not be suitable to associate with. However engineering
in agriculture nowadays is very important. The results of combining engineering and
agriculture can increase productivity and can help and facilitate the farmers perform
their daily work. Bum granular fertilizer sprayer is one of the engineering innovations in
agriculture. Granular fertilizer boom sprayer works as a machine that helps farmers
apply fertilizers or to combat the pests.
The method used is to spray fertilizer or pesticides to the crops by using
machines. Prototype ofthe granular boom sprayer show as Figure 2.1.
7
Figure 2.1: A prototype of granular boom sprayer. [3]
The boom sprayer machinery usually contains the granular fertilizer in a storage
container called a hopper. Apart from storing granular fertilizer, shaft design also serves
to reduce energy consumption. Granular fertilizer will apply pressure so that it moves
through the pipe before it is released through the blow head and scattered on the ground.
2.2 Nozzle and Blow head
Nozzle and blow head are the most important part of the spray process regardless of the
situation of substances is in the form of a liquid or granular form. It depends on the
results requested by the user. Nozzle is a device designed to control or direction of fluid
flow characteristics particularly to increase the velocity when leaving or entering a
confined space or pipes. The nozzles are typically used on pipes or tubes of varying
cross-sectional area and it can be used to redirect or change the flow of liquid or gas.
The nozzles are often used to control the flow rate, speed, direction, shape, mass and
pressure flow out of it [4]. Example of the nozzle is shown in igure 2.2.
8
Figure 2.2: Nozzle Manifold [5].
Unlike the blow head, blow head used for granular materials. Blow head is to
standardize the use of spray which isspattered all over the place. In Figure 2.2, blow
head is attached to the pipe. Previous studies have been carried out by connecting the
delivery pipe and angled the blow head at 120º and 185 mm long. The size of the boom
at the input section is 35 mm X 35 mm.
To produce a uniform spray, researchers have been collecting plate placed on the
inlet and collecting plate height can be changed. Collecting angled plate 30º [3]. Figure
2.3 shows the blow head.
9
Figure 2.3: Blow Head with collecting plate 30º[3].
2.3 Pipe selection for granular material
The pipe is used to channel the fluid from one place to another place. Pipe design is very
important because it will affect the flow therein. There are several types of pipes which
are circular pipe and non-circular pipe. A cicular pipe is used to transport fluid because
circular pipe can withstand the pressure difference between the inside and the outside of
the pipe without significantly disturbing the flow [6]. Non circular pipes are used for
applications in the cooling or heating system for the building. This type of non-circular
pipe commonly used for low-pressure fluid. In addition, the inside of the pipe also play
an important role. It will help to smooth the movement of fluid in a pipe even it can
improve efficiency at the output. Moreover, the choice of the pipe depends on the type
of materials used for distribution through pipelines. Figure 2.4 show the example of
circular pipe.
10
Figure 2.4 : Circular PVC pipe [7].
2.4 Particle size and shape
Fertilizer distribution pattern consistency and effectiveness is a key requirement in this
study. Therefore, particle size plays an important role in order to spread the fertilizer
evenly. Particle size is used to facilitate the work of farmers when spreading the
fertilizerat a distance. However, it requires a lot of energy to push granular fertilizer to
distant places. In addition, the large particle size cannot drain properly and causes
stunted spreading fertilizer. Normally the particle size measuring 2-4 mm can help
spread the fertilizer uniformly. [8]. Figure 2.5 shows the different size of particles.
Figure 2.5 : Different size of particles [9].
11
Shape also plays an important role in spreading fertilizer. Normally, fertilizer is a
spherical shape and can flow in pipe when high-pressured air is applied and helps to
spread the fertilizer evenly and uniformly.
2.5 Computational Fluid Dynamics Software
Computational Fluid Dynamics (CFD) is computer-based software to simulate the
behavior of a system such as fluid flow, heat transfer and other related physical
processes. It works by solving the equations of fluid flow (in a special form) to the
desired areaand prescribed conditions (known) at the boundary of the area are required.
Computers have been used to solve problems of fluid over the years in which
CFD solvers have been developed since the mid-1970s. The latest developments in the
field of computing power, together with the manipulation of 3-D graphics and
interactive effectively means the process of making a CFD model and analyse the results
is much less labour intensive, saving time and costs. Advanced CFD solver contains
algorithms that enable robust solutions in the field of flow in a fast time. As a result of
these factors, CFD is now a robust industrial design software, helps to reduce design
timescales and improve processes worldwide engineering.
CFD provides a cost-effective alternative and appropriate for the testing of scale
models, with changes in the simulations carried out quickly, which offers significant
advantages. By using CFD software, virtual prototyping system or device can be
designed to be analysed, then the real-world physics and chemistry is for use on the
model and the software will generate the images and data to predict the performance of
the design [10]. Figure 2.6 shows the results of using Ansys software-CFD.
12
Figure 2.6: Simulation of flow in pipe using CFD software [11].
2.6 Benefits of CFD software
There are three compelling reasons to use CFD software which are visionary, far-sighted
and have high efficiency. If any device or system that is difficult to build prototype or
tested experimentally, CFD analysis is able sneak into the design and show how it is
implemented. There are many phenomena that can be seen through the CFD, which
cannot be seen by any other means. CFD provides a deeper insight for each design. CFD
is a tool to predict what will happen under certain circumstances.
If there is one set of boundaries, the software will deliver results. Moreover, in a
short time, the software can predict how a particular design will be implemented and can
tested with variety for optimal results. All this can be done prior to physical prototyping
and testing. The results obtained from CFD helps improve the design, save money, meet
environmental regulations and ensure industry requirements. CFD analysis leads to
shorter design cycle and help to market more quickly. CFD software is also able to
shorten the development cycle and enables the design to make a quick prototype [12].
13
2.6.1 CFD Process
In the CFD process, there are basically three levels for each CFD simulation process
prior to pre-processing, solving and post-processing process.
2.6.1.1 Pre processing
This is the first step in constructing and analysing flow model. It includes building a
model in Solid work, create and use appropriate calculation network, and enter the
boundary flow conditions and fluid properties. Solid work simple geometry are imported
and adapted for CFD solutions in GAMBIT.
3D model selection in GAMBIT allows construction, simple geometry and
geometry translation of high quality. GAMBIT is a unique curvature and distance based
„functional size‟ to produce the right type of CFD and fine mesh around the model.
Along with the boundary layer technology, some schemes produce a volume mesh
correction for the application. Parameter differences also exist in the process [12].
2.6.1.2 Solver
CFD flow solver calculations and produce results. FLUENT CFD code has an extensive
interactive, so it can make changes to the analysis at any point during the process. This
saves time and allows you to refine a more efficient design. Graphical user interface
(GUI) is intuitive, which helps to shorten the learning time, and made the process faster
model. It is also easy to adjust physical condition and function interfaces to specific
needs. In addition, adaptive and dynamic network capability is unique among the
FLUENT CFD provider and works with various physical models. This capability makes
it possible and easy to create complex model moving objects in relation to the flow [12].
14
2.6.1.3 Post processing
This is the final step in CFD analysis, and it involves the organization and interpretation
of the data flow and earnings forecasts CFD images and animations. In addition,
FLUENT CFD solution easily added to the code structure as ABAQUS, ANSYS and
MSC, as well as simulation software engineering process to another.
2.7 Flow in pipe
Air flow has two types of movement which are laminar flow and turbulent flow Laminar
flow occurs when the fluid layer adjacent to move at the same speed and liquid particles
do not cross paths with each other. Laminar flow occurs at low velocity and high
viscosity. Is laminar flow in a pipe when Re = 2300. Turbulent flow occurs when the
current cross each other and mixing liquid flow occurs. This flow occurs at high speed
and low viscosity. A turbulent flow in pipes when Re = 4000. In fluid mechanics, the
Reynolds number (Re) is a dimensionless number which gives a measure of the ratio of
inertial forces to viscous forces and thus the quantity of the relative importance of the
two types of forces for given flow conditions [12]. Reynolds number can be calculated
using the following formula.
.................... (1)
Figure 2.7 : Reynold Number [6].
Where; ρ = Density, kg / m
μ = dynamic viscosity, kg / (m^ s)
ν = Kinematic viscosity, m / s
V = average velocity, m / s
D = Diameter, m
At Re ≤ 2300, flow is laminar,
At Re ≥ 4000, flow is turbulent,
Between 2000 < Re < 4000, flow is in the transition between laminar and turbulent
15
Air flow has 3 types of flow which are laminar flow, turbulent flow and
midstream. The diagram below shows the velocity profile of the three types of flow [6].
Figure 2.8 : Laminar and turbulent flow [13].
2.8 Design of experiment
In industry, designed experiments can be used to systematically investigate the process
or product variables that influence product quality. After you identify the process
conditions and product components that influence product quality, you can direct
improvement efforts to enhance a product's manufacturability, reliability, quality, and
field performance
For example, we may want to investigate the influence of coating type and
furnace temperature on the corrosion resistance of steel bars. We could design an
experiment that allows you to collect data at combinations of coatings/temperature,
measure corrosion resistance, and then use the findings to adjust manufacturing
conditions. Because resources are limited, it is very important to get the most
information from each experiment performed. Well‐designed experiments can produce
significantly more information and often require fewer runs than haphazard or
unplanned experiments [14].
16
In addition, a well‐designed experiment will ensure that we can evaluate the
effects that we have identified as important. For example, if we believe that there is an
interaction between two input variables, be sure to include both variables in your design
rather than doing a "one factor at a time" experiment. An interaction occurs when the
effect of one input variable is influenced by the level of another input variable. Designed
experiments are often carried out in four phases which are planning, screening also
called process characterization, optimization, and verification [15]. There are many
types of design of experiment such as one factorial designs, 2 factorial design consist
Taguchi method, response surface method design and reliability design of experiment
[16].
2.8.1 Full factorial method
This method was a traditional method which means all researchers used this method to
solve their problem. This method has level and factor which means level powered by
factor. The example of level and factor is shown below.
Figure 2.9 : Example of Level and factor[17].
Full factorial designs are the most conservative of all design types. There is little
scope for ambiguity when you are willing to try all combinations of the factor settings.
Unfortunately, the sample size grows exponentially in the number of factors, so full
factorial designs are too expensive to run for most practical purposes
For example, the experiment has 2 levels and 2 factors so it can write as 2². The
level is a velocity, temperature and pressure in the intake manifold. For the factor there
are „low‟ and „high‟ value for every levels. Velocity is 5m/s and 10m/s and pressure is
10kPa and 50kpa. This levels and factors can write in table such as table 2.1.
17
Table 2.1 : Example of parameters.
Level Low ( - ) High ( + )
Velocity, m/s 5 10
Pressure, kPa 10 50
Calculation for the experiment test is 2 X 2 is equal to 4 run for this experiment.
So, it can be write in the table such below.
Table 2.2 : Matrix Test [17].
Run number Factor Level
Low ( - ) High ( + ) Velocity, m/s Pressure, kPa
1 - - 5 10
2 + - 10 50
3 - + 5 10
4 + + 10 50
After matrix test iscompleted, the experiment can be performed according to the
table. The result can conclude which combination is the best and the worse.
18
2.8.2 Advantages and Disadvantages Full factorial method
This method have several advantages and limitation that researcher must know
before used this method. Table shown below are the advantages and disadvantages of
the full factorial method.
Table 2.3 : The Advantages and disadvantages of Full Factorial method [17].
No Advantages Disadvantages
1 This method is more precision on each
factor than with single factor
experiment.
When number of factor and level increase,
number of experiment will increase.
2 Broadening the scope of the
experiment.
Need more time for experiment when number
of factor and level more than 2.
3 Possible to estimate the interaction
effect.
Can be more complicated when the number of
interaction increase.
4 This method can lead to more
powerful test by reducing the error
variance.
Very high cost to do all experimental work.
5 Good for exploratory work that we
wish to find the most important factor.
Need more time to compare the result if those
experiment have many level and factor.
2.9 Design of experiment via Taguchi method
Dr. Genichi Taguchi is regarded as the foremost proponent of robust parameter design,
which isan engineering method for product or process design that focuses on minimizing
variation or sensitivity to noise. When used properly, Taguchi designs provide a
powerful and efficient method for designing products that operate consistently and
optimally over a variety of conditions.
19
In robust parameter design, the primary goal is to find factor settings that
minimize response variation, while adjusting the process on target. After we determine
which factors affect variation, we can try to find settings for controllable factors that will
either reduce the variation, make the product insensitive to changes in uncontrollable
noise factors, or both. A process designed with this goal will produce more consistent
output. A product designed with this goal will deliver more consistent performance
regardless of the environment in which it is used [18].
Engineering knowledge should guide the selection of factors and responses.
Robust parameter design is particularly suited for energy transfer processes, for
example, a car's steering wheel is designed to transfer energy from the steering wheel to
the wheels of the car. We should also scale control factors and responses so that
interactions are unlikely. When interactions among control factors are likely or not well
understood, we should choose a design that is capable of estimating those interactions.
Noise factors for the outer array should also be carefully selected and may
require preliminary experimentation. The noise levels selected should reflect the range
of conditions under which the response variable should remain robust. Robust parameter
design uses Taguchi designs (orthogonal arrays), which allow to analyse many factors
with few runs. Taguchi designs are balanced, that is, no factor is weighted more or less
in an experiment, thus allowing factors to be analysed independently of each other.
20
2.9.1 General step for Taguchi method
Taguchi method has the steps or procedures that have been designed by Dr.Genichi
Taguchi let users know how to use this method [19]. The steps are as following:
1 Identify objectives or more specific, target value for a performance
measure of the process.
2 Identify design parameters that will affect the experiment
3 Orthogonal array for the design parameters have been selected. It shows
the number and variations of each trial.
4 Run experiments according orthogonal array that have been made.
5 Analyse the data from the experiments that have been conducted
2.9.2 Types of Orthogonal Array
Taguchi has introduced several kinds of orthogonal arrays that can be used in
accordance with the parameters and the level required by the Researcher. Among the
types of orthogonal array is shown below:
L4 L8
L9 L12
L16 L‟16
L18 L25
L27 L32
L‟32 L36
L50
While many introduced by Taguchi orthogonal array, this study uses orthogonal
array L27. Parameters and levels is an important role in determining the appropriate
orthogonal array for the experiment to be carried out.
21
2.9.3 Advantages and disadvantages Taguchi method
There have several benefits and limitation of Taguchi method that user must know
before using this method for experimental work. Table below shows the benefits and
limitations of Taguchi method.
Table 2.4 : Advantages and disadvantages of Taguchi method[17]
No Advantages Disadvantages
1 Suitable for many levels and
factors
Do not test all variable combination
2 Time saving Difficulty accounting interactions between
parameter
3 Cost saving Do not exactly indicate what parameter has
the highest effect on the performance
characteristic value
4 Easy to complement Results obtained the relative
2.10 Determining Parameter Design Orthogonal Array
Taguchi has introduced a method that can help researchers utilize orthogonal array. The
parameter is a variable that will change and affect the experiment when diversified.
When the parameters affecting the experiment, the level where these parameters need to
be changed must be determined. To determine the level of variables requires a deep
understanding of the process, including minimum, maximum and current parameter
value. For example, there are six speed gear spindle, three in front and three on the rear
gear like the table below.
22
Table 2.5: The Spindle speed[20].
From the table above, there are 3 levels and 3 parameters. Parameter is the
spindle speed, feed rate and depth of cut. While the level is the number of parameters is
three. Referring to the selector array that has been introduced by Taguchi, Table selector
array is shown below.
Table 2.6 : Selector Array [19].
Table 2.7 : L9 Array select [19].
23
L9 array is an array of numbers that help researchers to facilitate the course of
the experiment. In addition, it can provide a guide to researchers in conducting
experiments. Table L9 is shown below.
Table 2.8 : L9 array table of experiment [19].
2.11 NPK Fertilizer
In agriculture fertilizer or seed is most important part or others name likes “vitamin” to
the plants. Like human, plants also need Carbohydrates, Protein and fat but for plant also
have three main "food groups", or rather "macro nutrients", the three main elements that
make up the bulk of a fertilizer is NPK[21].
NPK is short name of Nitrogen (N), Phosphorus (P) and Potassium (K) or in
other name „Kalium‟ hence the chemical symbol K. All elements have their own
characteristic of shape, density and molar mass. Nitrogen, N helps the plant to grow
strong and if too high nitrogen fertilizers will make for quick growth but weaker plants
that are more susceptible to attacks by diseases and pests. This chemical fertilizer is a
component of chlorophyll and aid to photosynthesis. Phosphorus, P is important in the
photosynthesis process.
24
This chemical fertilizer supports the component such as oils, sugar and starches
to the plant. In addition, phosphorus helps the growth of root and flower development.
The last content is Potassium, K, besides help the photosynthesis process, this „vitamin‟
help to support protein to the plant. Most importantly, this chemical fertilizer controls
the fruit‟s quality and to make the plant healthy [21]. These 3 elements have their own
specification as shown table 2.5 below.
Table 2.9 : The NPK specifications [22].
Fertilizer
element
Density, g/cm³ Molar mass,
g/mol Particle Shape Size, mm
Nitrogen, N 1.026 14.0067 Granular/ Fluid 1 - 5
Phosphorus, P 1.823 30.9737620 Granular/Fluid 2 - 6
Potassium, K 0.862 39.0983 Granular/Fluid/Powder 0.1 - 1
There have ratio between NPK elements for example 10-10-10 that means
Nitrogen 10%, Phosphorus 10% and Potassium 10%. This ratio has their purpose for the
growth of the plant. For example 10-10-10 fertilizer has a 1-1-1 ratio, 10-20-10 fertilizer
has a 1-2-1 ratio and 30-15-15 fertilizer has a 2-1-1 ratio. Basically, gardener use 1-2-1
ratio for the rooting, 1-1-2 or 1-2-2 or 2-1-2 ratio for the flowering and fruiting, for leafy
growth the ratio is 2-1-1 or 3-1-1 and for all purpose the ratio is 1-1-1 [22].
121
REFERENCES
1. Archie Augustus Stone, Harold E. Gulvin 1977-Machines for power
farmingTechnology& Engineering - University of Wisconsin – Madison
2. Angel P. Garcia, Nelson L. Capella & Claudio K (2012). Umeza. Auger – Type
granular fertilizer distribution: Mathematical Model and Dynamic Simulation.
Engineering Agriculture.
3. Y.J Kim, H.J. Kim, K.H. Ryu& J.Y. Rhee (2008). Fertilizer application
performance of a variable rate pneumatic granular applicator for rice
production. Biosystem Engineering. 498-510.
4. SaburoTsutsumi, Yokohama, Japan (1981). Internal Combustion Engine Intake
system having Jet-Producing Nozzle in Intake Port. Patern No 4,286,561.
5. Paxton product, retrived at 28/11/2014, from
http://www.paxtonproducts.com/products/airdeliverydevices/nozzlemanifolds
6. Yunus A. Çengel, John M. Cimbala (2006). Fluid mechanics: fundamentals and
applications. McGraw-HillHigher Education.
7. Kevin Meinert, subatomicglue, retrived at 28/11/2014, from
http://www.subatomicglue.com/didjl0g/
8. Ian Yule (2011).The Effect of Fertilizer particle size on spread distribution, NZ
Centre for Precision Agriculture, Massey University, Palmerston North, New
Zealand.
9. D.Forristal Jan 2014, IFJ Article: FertiliserPrills or Granules: which spread
best?.Teagasc Oak Park.
10. A.E.P.Veldman (2012). Computational Fluid Dynamics. University of
Groningen. Faculty of Mathemathics and Natural Sciences
122
11. PrzemekSokołowski, retrived at 28/11/2014, fromhttp://autodesk-inventor-
pl.typepad.com/my-blog/2013/06/autodesk-simulation-cfd-symulacja-
kranu.html
12. Fluent 6.2 Inc (2005), Fluent Europe User‟s Guide. Fluent Inc. Lebanon, NH
03766.
13. OMEGA Engineering inc 2003-2014, retrived at 28/11/2014, from
http://www.omega.com/techref/flowcontrol.html
14. Juran, J. M.., Editor, &Gryna, F. M., Associate Editor. (1998). Juran‟s Quality
Control Handbook, 4th edition, McGraw‐Hill Book Company, New York.
15. Montgomery. D.C, and George C. Runger, (2003), Applied Statistics and
Probability for engineers, (John Wiley and sons).
16. ReliaSoft Corporation, retrived at 29/11/2014, from
http://www.weibull.com/hotwire/issue85/relbasics85.htm
17. Introduction to Statistical Quality Control, 6th Edition by Douglas C.
Montgomery.Copyright (c) 2009 John Wiley & Sons, Inc.
18. Taguchi G, Konishi S ,Taguchi Methods, orthogonal arrays and linear graphs,
tools for quality American supplier institute, American Supplier Institute; 1987.
19. RavellaSreenivas Rao, C. Ganesh Kumar, R. Shetty Prakasham, Phil J. Hobbs
(2008) The Taguchi methodology as a statistical tool for biotechnological
applications: A critical appraisal Biotechnology Journal 3:510–523.
20. Krishankant, JatinTaneja, MohitBector, Rajesh Kumar (2012), Application of
Taguchi Method for Optimizing Turning Process by the effects of Machining
Parameters . International Journal of Engineering and Advanced Technology
(IJEAT)
21. FEECO international inc, copyright 2015, retriveat 26 may 2015,1010am from
http://feeco.com/npk-fertilizer-what-is-it-and-how-does-it-work/
22. Ville de Montreal 2015, ,retrived 26 may 2015,1010am from
http://espacepourlavie.ca/en/ratio-fertilizer-n-p-k
23. Mohamad Zaki M.S. (2013). A Numerical Study On Air-Fuel Mixture
Transportation To The Combustion Chamber Using Different Intake Manifold
Angle PFI System. UniversitiTunHussien Onn Malaysia: Degree thesis.
123
24. Iseki & Co., LTD. Boom spreader operation manual. Overseas Business
Department, Tokyo, Japan.
25. MetinOzen, OZEN ENGINEERING, INC, Meshing Workshop Ansys training,
retrieved at 23 May 2015 at 2.30 PM from www.ozeninc.com
26. Tingwen Li, Aytekin Gel, SreekanthPannala, MehrdadShahnam,
MadhavaSyamlal2014 .CFD simulations of circulating fluidized bed risers, part
I: Grid study. National Energy Technology Laboratory, Morgantown, WV, USA
27. Khalid. Ali. M. Gelim 2011. Mechanical and physical properties of fly ash
foamed concrete,UniversitiTunHussien Onn Malaysia: Master thesis.
28. HORIBA, Ltd 1996 – 2015, Guidebook for particle size analysis, retrieved at 20
April 2015, 3.40 AM from http://www.horiba.com/sg/process-environmental/