Engineering Project involving design,manufacturing, testing of Fins( Heat exchanger for 2 wheeler). An analysis of heat transfer on fins with various geometrical perforations.
Steam ejector working principle
An ejector is a device used to suck the gas or vapour from the desired vessel or system. An ejector is similar to an of vacuum pump or compressor. The major difference between the ejector and the vacuum pump or compressor is it had no moving parts. Hence it is relatively low-cost and easy to operate and maintenance free equipment.
It is basic information about what is critical thickness and why we should we know this. Then there is critical thickness formula for cylindrical pipe and spherical shell.
The document discusses the history and principles of vapor absorption refrigeration systems. Some key points:
- Vapor absorption was first discovered in 1824 by Michael Faraday and the first machine was built in 1860. It uses a refrigerant (ammonia) that is absorbed into a solvent (water) for compression.
- Unlike vapor compression, it uses heat rather than mechanical energy to change the refrigerant's state. This allows it to be powered by waste heat or solar energy.
- The first domestic refrigerator using this technology was invented in 1925 and used ammonia, hydrogen, and water in a "three-fluid" system to eliminate the need for a pump.
This document defines key terms related to steam formation and describes processes involved. It discusses:
- Terms like saturated liquid, saturated vapor, superheated vapor etc.
- Temperature and pressure where a substance changes phase (saturation temperature and pressure)
- Graphs like P-V and h-s diagrams that represent steam formation processes
- Quantities of heat absorbed during heating, vaporization (latent heat) and superheating of steam
- Measurement of dryness fraction (quality) of wet steam using throttling or electric calorimeters.
This document discusses different types of steam turbines and their operating principles. It describes impulse turbines where steam expands within nozzles and does not change pressure as it passes over blades. Reaction turbines gradually decrease pressure as steam passes over fixed and moving blades. Compounding methods are also presented, including velocity compounding using multiple blade rings, pressure compounding with nozzle stages, and pressure-velocity compounding combining both methods. The document aims to explain steam turbine design and operation.
This document discusses boiling and condensation processes. It defines boiling as the transition of a liquid to vapor when heated to the saturation temperature. There are different types of boiling including pool boiling, where fluid motion is from natural convection, and flow boiling, where an external pump forces liquid motion.
The boiling curve is presented, outlining the different boiling regimes of natural convection, nucleate boiling, transition boiling, and film boiling that occur as heat flux increases. Correlations are provided for calculating heat transfer in the nucleate and film boiling regimes.
Condensation occurs when vapor temperature decreases below saturation. It can be dropwise or film condensation, with dropwise having higher heat transfer. The rate of heat transfer
The document discusses heat exchangers, which transfer heat from one medium to another. It classifies heat exchangers based on their processes, fluid motion direction, mechanical design, and physical state of fluids. It then describes several common types of heat exchangers - shell and tube, plate, adiabatic wheel, plate fin, and pillow plate. It notes that shell and tube exchangers use tubes to transfer heat between two fluids, while plate exchangers use thin stacked plates. Heat exchangers have applications in engines, industries like oil/gas and chemicals, power generation, and HVAC systems like air conditioners and furnaces.
The document reviews heat transfer enhancement techniques using twisted tape inserts. It discusses heat exchangers and classifications. Twisted tape is described as a passive enhancement method that induces swirl and turbulence to disrupt the thermal boundary layer. Attributes of twisted tape like pitch, twist ratio and shape are examined. Using twisted tape can increase heat transfer rate in a heat exchanger by up to 188% but also increases friction loss. Different tape configurations are evaluated and it is found that optimization of parameters like twist ratio can improve thermal performance.
The document summarizes key concepts about thermodynamics cycles. It describes the processes that make up the Otto cycle used in spark-ignition engines, including isentropic compression, constant volume heat addition, isentropic expansion, and constant volume heat rejection. The thermal efficiency of the Otto cycle is defined. An example calculation illustrates determining temperatures, pressures, thermal efficiency, back work ratio, and mean effective pressure for an Otto cycle. The Diesel cycle used in compression ignition engines is also introduced.
The document discusses the iron-carbon phase diagram. It describes three important reactions:
1) The eutectic reaction occurs at 4.3% carbon and 1,147°C, where liquid transforms to austenite and cementite.
2) The eutectoid reaction occurs at 0.76% carbon and 727°C, where austenite transforms to ferrite and cementite to form pearlite.
3) The peritectic reaction occurs at 0.16% carbon and 1,493°C, where liquid and delta-ferrite transform to austenite.
The phase diagram is used to explain the microstructures that form in steels with different carbon
A U-tube heat exchanger consists of a shell containing a bundle of tubes that form a U-shape to transfer heat between two fluids, one flowing inside the tubes and the other outside the shell, with advantages of occupying less space than straight tube heat exchangers while providing maximum heat transfer through multiple tube passes, but disadvantages include higher costs from tube bending and difficulty cleaning inside tubes.
The document discusses different types of heat exchangers. It begins by defining a heat exchanger as a device that transfers heat between fluids, which may flow separately with a dividing wall or mix directly. Heat exchangers are widely used in applications like heating, cooling and industrial processes. The document then classifies heat exchangers based on the heat exchange process, relative fluid flow directions, mechanical design of the heat exchange surface, and physical states of the fluids. Specific heat exchanger types discussed include direct contact, regenerative, recuperative, parallel flow, counter flow, shell and tube, evaporator and condenser.
The document discusses high grade and low grade energy sources. High grade energy sources include mechanical, electrical, water, wind and tidal power which can be completely converted to work without loss. Low grade energy sources like heat can only partially be converted to work. Low grade energy consists of exergy (available energy) and anergy (unavailable energy). The maximum useful work obtainable from a heat source is called its availability or exergy. The minimum energy that must be rejected according to the second law of thermodynamics is called anergy. Availability reduces as the temperature difference between a system and its surroundings decreases.
Heat exchangers transfer heat from one medium to another. They are classified by flow configuration and construction. Key flow configurations are parallel, counter, and cross flow. Main construction types are shell and tube, and plate heat exchangers. Heat transfer is calculated using methods like log mean temperature difference (LMTD) and number of transfer units (NTU). Standards like TEMA provide guidelines for shell and tube heat exchanger design and components.
The document provides lecture notes on steam nozzles and power plants. It discusses:
1) The basic components and energy conversion process in thermal power plants, including the Rankine cycle in which water is heated to steam to power a turbine and generator.
2) The history and development of steam turbines, from early aeolipile devices to modern turbines invented by Charles Parsons in 1884.
3) How energy is converted in steam turbines via nozzles that accelerate steam to high velocity to impulse turbine blades and produce rotation.
4) Details on nozzle types, flow properties, relationships between area, velocity and pressure, and equations for calculating velocity from enthalpy change.
1. A steam generator or boiler is a closed vessel made of steel that transfers heat from fuel combustion to water to generate steam.
2. Boilers should be safe, accessible for maintenance, efficient in absorbing heat, simple in construction, and have low initial and maintenance costs.
3. There are many types of boilers classified by factors like the contents in tubes (fire tube or water tube), furnace position, and circulation method. Proper consideration of factors like steam needs, area, and costs is important for boiler selection.
1. Pool boiling occurs when a heated surface transfers heat to a liquid through natural convection and the formation of bubbles at the surface.
2. There are four regimes of pool boiling as excess temperature increases: natural convection, nucleate boiling, transition boiling, and film boiling. In nucleate boiling, bubbles form rapidly at nucleation sites on the surface.
3. The pool boiling curve graphs heat flux against the temperature excess of a surface above the liquid's boiling point. It shows regions of unstable and stable boiling across the different boiling regimes.
The document describes heat conduction through plane walls, cylinders, and spheres under steady-state conditions. It introduces the concepts of thermal resistance, resistance networks, and one-dimensional heat transfer. Equations are presented to calculate heat transfer rates and temperature distributions based on thermal properties and surface temperatures for multi-layered systems with conduction and convection. Special cases like contact resistance and critical insulation thickness are also covered.
APPLIED THERMODYNAMICS 18ME42 Module 03: Vapour Power CyclesTHANMAY JS
This document provides an overview of vapor power cycles, including the Carnot and Rankine cycles. It describes:
1) The Carnot vapor power cycle, including its four reversible processes of isothermal heat addition and rejection and adiabatic expansion and compression. However, it notes that the Carnot cycle is difficult to implement in practice.
2) The simple Rankine cycle, which uses the same four processes as the Carnot cycle but with complete condensation in the condenser. Equations for thermal efficiency are provided.
3) Key parameters used to analyze vapor power cycle performance such as heat added, heat rejected, turbine work, and pumping work.
The document describes a double pipe heat exchanger and provides classifications of heat exchangers. A double pipe heat exchanger consists of two concentric pipes and connecting tees to transfer thermal energy between two fluids. Heat exchangers can be classified based on their heat transfer mechanism, construction type, flow arrangement, number of passes, and operating temperatures and pressures. Common types include plate, tubular, extended surface, and phase change heat exchangers.
Experimentation to predict the thermal performance of conventional heat pipe ...eSAT Journals
Abstract
This work attempts to analyses the performance of conventional heat pipe with water and hydrocarbon as working fluid. The
hydrocarbon working fluid involve acetone and methanol. The experimental investigation involves the determination of thermal
resistance of conventional heat pipe at various heat input and to determine the best working fluid out of the water, acetone and
methanol. Conventional heat pipe is filled with water, acetone and methanol with the filling ratio of 60 % with this filling ratio the
thermal performance of the device is investigated.
Keywords: Working Fluid, Heat Transfer, Thermal Resistance, Thermal Performance.
Performance investigation of conventional heat pipe with hydrocarbon as worki...eSAT Journals
Abstract
This work attempts to analyses the performance of conventional heat pipe with hydrocarbon as working fluid. The performance
investigation involves the determination of thermal resistance of conventional heat pipe at various heat input. And to determine
the best hydrocarbon working fluid out of the acetone and methanol. Conventional heat pipe is filled with acetone and methanol
with the filling ratio of 60 % with this filling ratio the performance of the device is investigated.
Keywords: Working Fluid, Heat Transfer, Thermal Resistance.
ENGR202_69_group7_lab4partA_report.docxYIFANG WANG
This document summarizes an experiment conducted to measure temperature using a thermocouple. The experiment involved using a thermocouple and data logging software to record the cooling curve of a heated resistor over multiple trials. Time constants were calculated from the cooling curves and used to generate modified cooling curves that closely matched the experimental data. The goals of the experiment were to understand how to properly use a thermocouple to measure temperature changes and analyze the thermal properties of materials.
Lab Report Conduction With Free ConvectionHamzaArain8
This lab report details an experiment to measure the convection coefficient of a cylindrical aluminum fin. Temperature measurements were taken along the length of the fin using thermocouples when hot water was circulated through the fin's base. The temperature data was used to calculate the convection coefficient at different points along the fin based on a theoretical heat transfer model. The mean convection coefficient was determined to be 30.68 W/m2K. The experiment demonstrated a method for empirically determining a fin's convection coefficient to support heat transfer theory.
Experimental and Exergy Analysis of A Double Pipe Heat Exchanger for Parallel...IJERA Editor
This paper presents For Experimental and Exergy Analysis of a Double Pipe Heat Exchanger for Parallel- flow Arrangement. The Double pipe heat exchanger is one of the Different types of heat exchangers. double-pipe exchanger because one fluid flows inside a pipe and the other fluid flows between that pipe and another pipe that surrounds the first.In a parallel flow, both the hot and cold fluids enter the Heatexchanger at same end andmove in same direction. The present work is taken up to carry experimental work and the exergy analysis based on second law analysis of a Double-Pipe Heat Exchanger. In experimental set up hot water and cold water will be used working fluids. The inlet Hot water will be varied from 40 0C and 50 0C and cold water temperature will be varied from between 15 and 20. It has been planned to find effects of the inlet condition of both working fluid flowing through the heat exchanger on the heat transfer characteristics, entropy generation, and Exergy loss. The Mathematical modelling of heat exchanger will based on the conservation equation of mass, energy and based on second law of thermodynamics to find entropy generation and exergy losses.
1) The document describes an experiment to measure the thermal conductivity of a solid cylindrical iron specimen through heat conduction. Thermocouples were used to measure the temperature at three points along the specimen as heat was transferred to water flowing through a reservoir.
2) Calculations were shown to determine the thermal conductivity (K) at each measurement point and the average conductivity based on temperature differences and heat transfer equations.
3) The thermal conductivities calculated at the three points along the specimen were 66.0646 W/mK, 80.44709 W/mK, and 73.2589 W/mK, with an average of 73.256 W/mK.
Thermal Expansion Apparatus 012-04394C
2
Accepted Values for Coefficient of
Thermal Expansion
Material a ( x10-6/∞C )
Copper 17.6
Steel 11.3 to 13.5
Aluminum 23.4
Changing Tubes
➤ Caution:
When changing tubes be careful
not to pull the wires off the
thermistor. The thumb-
screw must be com-
pletely removed
before the thermistor
can be lifted off the
threaded rod.
Replacement Parts
The following parts can be ordered from
PASCO scientific.
Item PASCO Part #
mod. Thermistor (100 kΩ) 150-03140
Al Tube Assy 003-04413
Cu Tube Assy 003-04412
Steel Tube Assy 003-04414
Foam Insulator 648-03100
Dial Gauge 620-050
Thermistor
Tube
Thumbscrew
012-04394C Thermal Expansion Apparatus
3
Introduction
Most materials expand somewhat when heated through a temperature range that does not
produce a change in phase. The added heat increases the average amplitude of vibration of
the atoms in the material which increases the average separation between the atoms.
Suppose an object of length L undergoes a temperature change of magnitude ∆T. If ∆T is
reasonably small, the change in length, ∆L, is generally proportional to L and ∆T. Stated
mathematically:
∆L = αL ∆T;
where α is called the coefficient of linear expansion for the material.
For materials that are not isotropic, such as an asymmetric crystal for example, a can have a
different value depending on the axis along which the expansion is measured.
a can also vary somewhat with temperature so that the degree of expansion depends not
only on the magnitude of the temperature change, but on the absolute temperature as well.
In this experiment, you will measure α for copper, aluminum, and steel. These metals are
isotropic so that a need only be measured along one dimension. Also, within the limits of
this experiment, a does not vary with temperature.
Procedure
➀ Measure L, the length of the copper tube at room temperature. Measure from the inner edge
of the stainless steel pin on one end, to the inner edge of the angle bracket at the other end
(see Figure 1). Record your results in Table 1.
➁ Mount the copper tube in the expansion base as shown in Figure 2. The stainless steel pin
on the tube fits into the slot on the slotted mounting block and the bracket on the tube
presses against the spring arm of the dial
gauge.
➤ NOTE: Slide or push the tube to one side of
the slide support. Drive the thumbscrew
against the pin until the tube can no longer be
moved. Use this as your reference point.
➂ Use one of the provided
thumbscrews to attach
the thermistor lug to the
threaded hole in the
middle of the copper
tube. The lug should be
aligned with the axis of
the tube, as shown in
Figure 2, so there is
maximum contact
L
Bracket on tube
Dial Gauge Spring Arm
Stainless steel pin
Figure 2 Equipment Setup (Top View)
Slotted bracket Thumbscrew
Figure 1 Measuring Tube Length
Experiment: Measuring the Coefficient of Linear
Expansion for Copper, Steel, and Aluminum
brucejohnson
H.
Experimentation to predict the thermal performance of closed loop pulsating h...eSAT Journals
Abstract
The closed-loop pulsating heat pipe is a type of small heat transfer device with a very high thermal conductivity. It was invented to meet the requirement for smaller heat transfer devices. It can transfer sufficient heat for heat dissipation applications in modern electronic devices. The objective of this work is to study thermal performance of closed loop pulsating heat pipe with acetone and methanol as working fluid.. Copper has been selected as material for heat pipe due to compatibility of copper with acetone and methanol as working fluid. Filling ratio of the working fluid significantly influence on the performance closed loop pulsating heat pipe. From the past studies it was observed that filling ratio of 30-75 % provides the best result hence 60 % filling ratio has been selected for this filing ratio the thermal performance of closed loop pulsating heat pipe with acetone and methanol as working fluid is investigate.
Keywords: closed loop pulsating heat pipe, condenser, evaporator, working fluid, filling ratio.
1. The document describes an experiment on radial heat conduction conducted by students. The experiment aims to determine the thermal conductivity of unknown materials.
2. Key steps of the experiment include setting up the equipment, taking temperature readings at different points in the material as heat is applied, and calculating the thermal conductivity using the temperature data and heat transfer equations.
3. Results showed a linear relationship between temperature difference and distance from the heat source, and that thermal conductivity values decreased with increasing heat input, as expected based on theory.
To investigate the effect of a change in the cross section area on the temper...Salman Jailani
Experiment #2 investigated the effect of changing the cross-sectional area of a thermal conductor on its temperature profile. Sensors were placed along a brass conductor to measure the temperature at various points as heat was applied. The temperature and heat input power were recorded at steady state intervals. Varying the input power affected the overall heat transfer coefficient, with higher input power resulting in a lower coefficient. The calculated and theoretical heat transfer coefficients differed due to differences in experimental variables.
This document summarizes a laboratory experiment on linear heat conduction. The objectives were to measure thermal conductivity along the z-direction and verify Fourier's Law. The procedure involved installing a heating element in a brass barrel, adjusting the cooling water and heater power, and measuring temperatures at points along the barrel until steady state was reached. Thermal conductivity values were calculated at different temperature drops and distances. The results showed that conductivity decreased with increasing temperature difference and distance, in agreement with theory. Sources of error and ways to improve the experiment were also discussed.
The document discusses deposition rates, electrode efficiency, and electrode weld metal recovery, which are different metrics for measuring welding consumables. Deposition rate is the rate at which weld metal is deposited, while electrode efficiency is the percentage of filler metal that is deposited. Electrode weld metal recovery allows calculating the percentage of welding consumable that will end up in the finished weld. Tables provide the weight of weld metal deposited per meter for common weld geometries like triangles and rectangles at different thicknesses.
Experimental Investigation of Heat Transfer by Electrically Heated Rectangula...IRJET Journal
This document presents an experimental investigation of heat transfer from an electrically heated rectangular surface by natural convection. The experiment measured the temperature distribution of air around a flat aluminum plate heated to temperatures between 347-365K at various angles from vertical. As the plate angle increased, the slope of the dimensionless temperature curve decreased, showing angle affects heat transfer. The Nusselt number also varied with angle. The experimental data agreed with previous work for vertical plates and showed temperature was independent of distance horizontally. The results provide insight into heat transfer behavior from inclined surfaces.
International Journal of Engineering Research and Applications (IJERA) is an open access online peer reviewed international journal that publishes research and review articles in the fields of Computer Science, Neural Networks, Electrical Engineering, Software Engineering, Information Technology, Mechanical Engineering, Chemical Engineering, Plastic Engineering, Food Technology, Textile Engineering, Nano Technology & science, Power Electronics, Electronics & Communication Engineering, Computational mathematics, Image processing, Civil Engineering, Structural Engineering, Environmental Engineering, VLSI Testing & Low Power VLSI Design etc.
Experimental Investigation of Natural Convection Heat Transfer Enhancement fr...IRJET Journal
This document describes an experimental investigation of natural convection heat transfer from rectangular fin arrays with combinations of V-notches and perforations. Four fin array configurations were tested: one without notches or perforations (un-notched), and three with different combinations of V-notches and perforations removing different percentages of the fin area. The fin arrays were heated to different temperatures and the resulting heat transfer coefficients were measured and compared. The results showed that the combination of V-notches and perforations both increased the surface area and the turbulence near the fins, allowing more air contact and higher heat transfer coefficients compared to the un-notched fins. Among the configurations tested, the fin array with 20% of its area removed
The lab report summarizes an experiment conducted to determine the reaction order and rate constant (K) of a reaction at 40°C. Readings of conductivity were recorded over time and used to calculate concentration. The results were plotted as ln(CA/CAo) vs. time and 1/CA vs. time. The ln(CA/CAo) plot was nonlinear, indicating a second-order reaction. The rate constant K was calculated to be 8.268 × 10-3 at 40°C. The 1/CA plot was linear, also suggesting a first-order reaction, and the rate constant was calculated from the slope to be 0.177166013.
This lab report summarizes 6 experiments conducted to measure various mechanical properties:
1. Measuring temperature using different devices and noting the differences.
2. Explaining the working of a 4-stroke internal combustion engine through diagrams and concluding that isothermal and adiabatic processes allow it to generate power.
3. Demonstrating the working principle of a concentric heat exchanger under counterflow conditions and calculating efficiency.
4. Demonstrating the working principle of a concentric heat exchanger under parallel flow conditions and concluding more heat is transferred under counterflow.
5. Determining the temperature distribution during steady-state heat conduction through a cylinder wall and demonstrating the effect of
Prediction of friction factor and non dimensions numbers in force convectionIAEME Publication
This document summarizes an experimental study on heat transfer in an insulated cylindrical pipe. The study measured parameters like Nusselt number, Reynolds number, and frictional factor under different flow conditions. Experiments were conducted with air flow through a 40mm diameter pipe with 5mm insulation. Measurements were taken for 1/3, 2/3, and full opening of a control valve, and results were validated against analytical calculations using common heat transfer equations. Experimental values matched well with theoretical predictions.
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1. EXPERIMENTATION AND ANALYSIS OF HEAT TRANSFER
THROUGH PERFORATED FINS OF DIFFERENT
GEOMETRY.
Visvesvaraya Technological University, Belgaum
ABHIJATH H B 4VV11ME002
AKSHAY MOHAN RAJ 4VV11ME012
DASHARATHA H S 4VV11ME024
M S SHARATH KUMAR 4VV11ME039
Under the Guidance of
Mr B B GANESH
B.E, M.Tech,
Assistant Professor
Department of Mechanical Engineering
Vidyavardhaka College of Engineering
Gokulam 3rd Stage, Mysore 570002,Karnataka, India
2014-2015
2. INTRODUCTION
• The removal of excessive heat from system components
is essential to avoid damaging effects of burning or
overheating. Therefore, the enhancement of heat
transfer is an important subject of thermal engineering.
• Extended surfaces (fins) are frequently used in heat
exchanging devices for the purpose of increasing the
heat transfer between a primary surface and the
surrounding fluid.
3. OBJECTIVE
• To increase the heat transfer between system and the
surroundings at faster rate.
• To achieve required output by reducing the weight of
the system.
• Simple in construction.
• Cheaper in cost.
• Effective cooling capability.
4. SCOPE
Further more geometrical variations of complex shapes and
tapered can be incorporated into fins .
This may increase the rate of heat transfer due to turbulence .
Incorporating fins made of aluminum into automobile engines
and electronic gadgets help in proper dissipation of heat to the
surrounding.
6. MERITS
• Considerably reduces the weight of the system.
• Aluminum fins are lighter due to lower density and
are effective fin materials.
• Due to turbulence over all heat transfer is
considerably high compared to heat transfer in solid
fins.
• Perforations induce turbulence and creates critical
points of heat transfer.
7. DEMERITS
• Stability of perforation plays an important role.
• Sharp edges results in wearing of fin over the time.
8. LITERATURE SURVEY
• Perforations in the fins will increase the heat
convection from the body of the system to
surroundings.
• By varying the geometrical shapes we can achieve
higher efficiency compared to solid fin
• This not only increases the convection but also helps
in reducing the weight of the body
9. EXPERIMENTAL SETUP
The air duct is the housing where the fin and the heating coil assembly
are placed. It is a rectangular passage made of ply wood . It’s dimension
being 150×100×600mm.Its one end is exposed to blower and other is
open to the atmosphere.
AIR DUCT
10. Dimmer stator is used to regulate the input voltage. As the
voltage increases, the heat generated in the heating coil also
increases.
DIMMER STATOR
The display unit consists of three displays. One display measures the
different temperatures in the system. The other two are used to
measure the voltage and current in the circuit.
DISPLAY UNIT
11. Artificially, air is circulated over the fins with the help of an Air
blower . Valve varies the velocity of air in the duct .The velocity of
forced air is calculated using an Anemometer.
AIR BLOWER
12. •A heating element converts electricity into heat through the process of
resistive or Joule heating. Electric current passing through the element
encounters resistance, resulting in heating of the element.
•The heater is made of mica and heats upto 100
o
c
ELECTRIC HEATER
13. Thermally conductive tape is one of the most cost-effective heat sink
attachment materials. It is suitable for low-mass heat sinks and
relatively lower temperature. It consists of a thermally conductive
carrier material with a pressure-sensitive adhesive on each side.It
sticks the fin surface to the thermocouple.
THERMAL TAPE
14. The experiments have been conducted in a controlled
environment inside the laboratory. The experiment is carried out for
two different fin materials. Thermocouples are fixed to the heating
coil to measure the base temperature, freely left inside the air duct
to measure ambient temperature and to the fin to measure the fin
temperatures.
EXPERIMENTAL PROCEDURE
15. •The experiment is conducted by keeping the voltage constant and
varying velocity of air i.e. 4, 5, 6, 7, 8, 9, 10,11,12,13 and 14 m/s.
•Once the steady state is reached, voltmeter reading, ammeter reading
and temperature readings T1 to T5 for fins are noted down.
•The experiment is repeated for voltage value 50, 60, 70, 80, and 90
respectively
16. DESIGN OF FINS
Fins have a rectangular cross section of 100 x 55 and width 50 mm
It is an array containing 4 rectangular surfaces .
Every surface acts as a medium for convection heat transfer.
17. FINS WITH CIRCULAR PERFORATIONS
Circular through perforations are
made on the rectangular surface
of the fin.
The size of the hole being 1mm
radius
Tolerance is given at both sides to
ensure mechanical stability of the
fin.
A matrix of 3 X 4 perforations are
created on all the rectangular
surface of the fin.
18. FINS WITH RECTANGULAR PERFORATIONS
Rectangular fins of 5x2 cross
section are made on the
rectangular surface .
The perforation is given
chamfering at the edges to
reduce wearing and increase the
stability.
Matrix of 4x4 are made on the
fins .
A total of 64 rectangular
perforation is made . This greatly
reduces the weight of the fin.
20. SELECTING THE FACES FOR SECOND CONVECTION
TEMPERATURE DISTRIBUTION
HEAT FLUX DISTRIBUTION
21. THERMAL ANALYSIS
Thermal analysis shows
significant reduction in the
temperature in the case of fins
with rectangular and circular
compared to solid fins .