The document describes several experiments analyzing heat transport through saturated sediments. A sandbox model was used to study heat flow, showing a cold front moving through the saturated zone over 3-5 hours. These results were modeled using TOUGH2 software. A flume experiment monitored temperature changes over 8 hours as the stream and groundwater reached equilibrium. Distributed temperature sensing (DTS) was then applied, measuring temperature variations in the flume induced by upstream heating. The high precision DTS data validated other measurements and provided spatial and temporal data on heat transport through the saturated sediments.
The students constructed a single pipe heat exchanger by burying a steel pipe in an active compost pile to study if compost heat could effectively heat water. Water was run through the pipe at two flow rates while temperature data was collected. The experiment resulted in water temperature increases of 1.4°C and 1.3°C for the different flow rates. Modeling in STELLA predicted the temperature increases could have been higher at around 9°C and 5°C if steady state conditions were reached. Faster flow rates led to higher heat transfer rates but slower rates allowed for greater temperature change according to the models.
The document presents a numerical investigation of natural convection heat transfer from a circular cylinder inside a square enclosure using different types of nanofluids. Governing equations for the laminar, steady-state flow and heat transfer are presented. The equations are solved using the vorticity-stream function formulation and finite difference method. Results are obtained for Rayleigh numbers between 104-106, enclosure width to cylinder diameter ratio of 2.5, and nanofluid volume fractions from 0-0.2. Types of nanofluids investigated include water with Cu, Al2O3, and TiO3 nanoparticles. Results show Nusselt number and heat transfer increase with nanofluid volume fraction. Heat transfer is more enhanced at lower Ray
NUMERICAL INVESTIGATION OF NATURAL CONVECTION HEAT TRANSFER FROM CIRCULAR CYL...IAEME Publication
In the present work, the enhancement of natural convection heat transfer utilizing nano fluids as working fluid from horizontal circular cylinder situated in a square enclosure is investigated numerically. Different types of nano particles were tested. The types of the nano fluids are Cu, Al2O3 and TiO3 with water as base fluid. A model is developed to analyze heat transfer performance of nano fluids inside an enclosure taking into account the solid particle dispersionrs on the flow and heat
transfer characteristics.
This document discusses empirical correlations for mixed convection heat transfer through a fin array based on various orientations. It summarizes previous research on the effects of fin orientation and channel inclination angle on heat transfer. The current study investigates the effect of lateral and longitudinal channel inclination on heat transfer in a rectangular channel with longitudinal fins. Experimental results show that heat transfer is highest for a laterally inclined channel at 0 degrees and increases with longitudinal inclination angle. Empirical equations are developed to correlate Nusselt number with orientation angles, Reynolds number, and Grashof number.
This document proposes a new method for determining the thermal conductivity of liquids using the transient hot disk method. The conventional method is found to be inaccurate due to its inability to account for the effects of natural convection and variations in volumetric heat capacity near the sensor. The new method utilizes the known volumetric heat capacity of the liquid and an equation to predict the onset of natural convection. Test results using six different liquids show the new method yields thermal conductivity measurements within 5.6% of literature values over a wide range of conditions, demonstrating it is highly accurate.
The document discusses various concepts related to thermal heat gain and loss in buildings, including:
- Thermal conductivity, resistivity, conductance, and resistance, which describe the ability of materials to allow heat to pass through them.
- Time lag and decrement factor, which characterize periodic heat flow patterns as outdoor temperatures fluctuate daily.
- Methods for calculating conduction, convection, radiation, and ventilation heat exchange in buildings.
- The concept of sol-air temperature, which combines radiant and convective heating effects on buildings.
- Factors like solar gain factor and surface conductance that influence a building's absorption of solar heat gain.
The document describes an experiment to determine the average surface heat transfer coefficient in natural convection. The apparatus consists of a vertically oriented brass tube heated by an electric element inside an enclosure. Thermocouples measure the tube temperature. Natural convection heat transfer from the tube to surrounding air is calculated using Newton's law of cooling. Correlations are used to compare the experimentally obtained heat transfer coefficient. The experiment aims to determine the heat transfer coefficient and compare it to values from correlations.
The students constructed a single pipe heat exchanger by burying a steel pipe in an active compost pile to study if compost heat could effectively heat water. Water was run through the pipe at two flow rates while temperature data was collected. The experiment resulted in water temperature increases of 1.4°C and 1.3°C for the different flow rates. Modeling in STELLA predicted the temperature increases could have been higher at around 9°C and 5°C if steady state conditions were reached. Faster flow rates led to higher heat transfer rates but slower rates allowed for greater temperature change according to the models.
The document presents a numerical investigation of natural convection heat transfer from a circular cylinder inside a square enclosure using different types of nanofluids. Governing equations for the laminar, steady-state flow and heat transfer are presented. The equations are solved using the vorticity-stream function formulation and finite difference method. Results are obtained for Rayleigh numbers between 104-106, enclosure width to cylinder diameter ratio of 2.5, and nanofluid volume fractions from 0-0.2. Types of nanofluids investigated include water with Cu, Al2O3, and TiO3 nanoparticles. Results show Nusselt number and heat transfer increase with nanofluid volume fraction. Heat transfer is more enhanced at lower Ray
NUMERICAL INVESTIGATION OF NATURAL CONVECTION HEAT TRANSFER FROM CIRCULAR CYL...IAEME Publication
In the present work, the enhancement of natural convection heat transfer utilizing nano fluids as working fluid from horizontal circular cylinder situated in a square enclosure is investigated numerically. Different types of nano particles were tested. The types of the nano fluids are Cu, Al2O3 and TiO3 with water as base fluid. A model is developed to analyze heat transfer performance of nano fluids inside an enclosure taking into account the solid particle dispersionrs on the flow and heat
transfer characteristics.
This document discusses empirical correlations for mixed convection heat transfer through a fin array based on various orientations. It summarizes previous research on the effects of fin orientation and channel inclination angle on heat transfer. The current study investigates the effect of lateral and longitudinal channel inclination on heat transfer in a rectangular channel with longitudinal fins. Experimental results show that heat transfer is highest for a laterally inclined channel at 0 degrees and increases with longitudinal inclination angle. Empirical equations are developed to correlate Nusselt number with orientation angles, Reynolds number, and Grashof number.
This document proposes a new method for determining the thermal conductivity of liquids using the transient hot disk method. The conventional method is found to be inaccurate due to its inability to account for the effects of natural convection and variations in volumetric heat capacity near the sensor. The new method utilizes the known volumetric heat capacity of the liquid and an equation to predict the onset of natural convection. Test results using six different liquids show the new method yields thermal conductivity measurements within 5.6% of literature values over a wide range of conditions, demonstrating it is highly accurate.
The document discusses various concepts related to thermal heat gain and loss in buildings, including:
- Thermal conductivity, resistivity, conductance, and resistance, which describe the ability of materials to allow heat to pass through them.
- Time lag and decrement factor, which characterize periodic heat flow patterns as outdoor temperatures fluctuate daily.
- Methods for calculating conduction, convection, radiation, and ventilation heat exchange in buildings.
- The concept of sol-air temperature, which combines radiant and convective heating effects on buildings.
- Factors like solar gain factor and surface conductance that influence a building's absorption of solar heat gain.
The document describes an experiment to determine the average surface heat transfer coefficient in natural convection. The apparatus consists of a vertically oriented brass tube heated by an electric element inside an enclosure. Thermocouples measure the tube temperature. Natural convection heat transfer from the tube to surrounding air is calculated using Newton's law of cooling. Correlations are used to compare the experimentally obtained heat transfer coefficient. The experiment aims to determine the heat transfer coefficient and compare it to values from correlations.
Dana May Ortmann Gilbert conducted a second year lab project to optimize an acoustic heat pump. The experiment involved creating a standing wave in a tube using a loudspeaker. Different stacks made of kapton tape and PVC tubes were placed in the tube to allow heat exchange. Temperature differences of over 3°C across the stacks were achieved at resonance frequencies. The project investigated how parameters like the stack material and size, frequency, and stack position affected the temperature difference.
This document appears to be the introduction or cover page of a lab manual for a Heat Transfer lab course. It provides information about the university and engineering college where the course is taught, and lists the name and identification information for the student. It also lists the experiments that will be conducted in the lab course, including determining thermal conductivity, studying heat exchangers, measuring emissivity, and analyzing heat transfer through fins, composite walls, and during convection. The document provides an overview of the lab course and experiments but no detailed information.
Experiments were conducted to calibrate Schmidt-Boelter heat flux gauges in stagnation and shear air flows. A thermal model was developed that predicts the gauge sensitivity will have a nonlinear dependence on the heat transfer coefficient. Experimental calibration systems were built to simultaneously measure gauge response and heat flux. For stagnation flow, measured sensitivities matched the model and were used to estimate the internal thermal resistance of each gauge. For shear flow, the effect of varying gauge surface temperature on the boundary layer was included. Results matched the model with a lower effective heat transfer coefficient. The internal thermal resistance impacted gauges differently in each flow condition.
Spe113595 - Detection of Scale Deposition Using Distributed Temperature Sensingfhmutairi
This paper investigates using distributed temperature sensing (DTS) data to detect scale deposition in well tubulars. The presence of scale, which has lower thermal conductivity than tubing, affects the temperature profile measured by DTS. Higher temperatures inside the tubing would be detected within scale zones due to reduced heat transfer. The magnitude of temperature increase depends on production conditions, completion design, scale location and length. DTS could provide a novel method for detecting scale and eliminating uncertainties in deriving properties like scale thickness from continuous temperature measurements.
This lab manual document provides instructions for experiments on heat transfer in a Mechanical Engineering department. The first experiment listed is on heat transfer from a pin-fin apparatus. The objective is to calculate the heat transfer coefficient for natural and forced convection from a fin. The experiment involves measuring temperatures along a brass fin heated at one end while air passes over it naturally or in a duct. The second experiment listed is on heat transfer through a composite wall, and involves determining the total thermal resistance and conductivity of a wall made of different slab materials sandwiching a heater.
This document contains information about experiments in heat transfer lab manual. It includes 13 experiments related to different modes of heat transfer like through composite walls, critical heat flux, measurement of surface emissivity, forced convection, lagged pipe, natural convection, heat exchangers, pin-fin, Stefan-Boltzmann apparatus, thermal conductivity of concentric sphere and metal rod, transient heat conduction, heat pipe demonstration. For each experiment, it provides introduction, description of apparatus, experimentation procedure, observations, calculations and precautions.
This document discusses psychrometry, which is the study of thermodynamic properties of moist air. It outlines several important psychrometric properties used to analyze air conditioning processes, including dry bulb temperature, wet bulb temperature, dew point temperature, humidity ratio, relative humidity, specific volume, and enthalpy. It then explains common psychrometric processes like sensible heating, sensible cooling, humidification, dehumidification, and their representations on a psychrometric chart. Basic concepts in air conditioning like adiabatic mixing, bypass factor, sensible heat factor, and room sensible heat factor are also introduced.
Psychrometry: Properties and processes discusses key concepts in psychrometry including:
- Psychrometry is the study of properties of air-water vapor mixtures, commonly known as moist air. Moist air consists of dry air, water vapor, and other inert gases.
- Key psychrometric properties include specific humidity, relative humidity, dry bulb temperature, wet bulb temperature, dew point temperature, and degree of saturation.
- The sling psychrometer is used to measure wet bulb temperature by whirling two thermometers, one dry and one wet, through the air. Wet bulb depression indicates the specific humidity of air.
- Dew point temperature is the temperature at which air becomes saturated when cooled at constant
This document contains instructions and procedures for experiments in a Heat Power Engineering Laboratory. It includes a bona fide certificate, instructions for students, a list of 11 experiments, and procedures and calculations for experiments on heat transfer through natural convection from a vertical cylinder, forced convection inside a horizontal tube, and determining temperature distribution and efficiency of a pin-fin apparatus using forced convection. Diagrams, observation tables, formulas, and sample calculations are provided for each experiment. The goal is to determine heat transfer coefficients and understand heat transfer processes like natural convection, forced convection, and heat transfer through fins.
This document discusses heat transfer, including:
1. The three modes of heat transfer - conduction, convection, and radiation. It provides equations to calculate heat transfer via these modes.
2. Key heat transfer concepts like thermal conductivity, convection coefficients, emissivity, and overall heat transfer coefficients.
3. Examples of calculating heat transfer through composite walls and heat exchanger surfaces.
Hmt lab manual (heat and mass transfer lab manual)Awais Ali
This document describes procedures for 7 experiments on heat transfer:
1. Investigates Fourier's Law of heat conduction along a brass bar by measuring temperatures at points along the bar for different heat inputs.
2. Studies heat conduction along a composite bar and calculates the overall heat transfer coefficient.
3. Examines the effect of cross-sectional area changes on temperature profiles in a conductor.
4. Determines temperature profiles and heat transfer rates from radial conduction through a cylinder wall.
5. Measures thermal conductivity of non-metallic materials and compares to theory.
6. Determines thermal conductivity of liquids and gases.
7. Investigates the relationship between power input and surface temperature for free convection
The document discusses the psychrometric chart and various psychrometric processes involving moist air. It begins by identifying parts of the psychrometric chart and explaining how it can be used to determine moist air properties and analyze processes involving moist air. Several examples are then provided to illustrate key psychrometric processes including sensible heating/cooling, heating and humidifying, cooling and dehumidifying, adiabatic or evaporative cooling, and adiabatic mixing of moist air streams. Step-by-step workings are shown for each example to determine various moist air properties and mass transfer rates.
As companies examine their total cost of operations, energy usage and heat recovery deliver cost savings through increased energy utilization and efficiency. Heat exchangers offer companies the opportunity to reuse energy generated for a specific purpose instead of venting that energy to the atmosphere. Shell and tube heat exchangers are in wide use throughout the Food, Dairy, Beverage, Pharmaceutical, Chemicals, Petroleum Refining, and Utility industries. This paper briefly explores three modes of heat transfer and basic designs found in shell and tube heat exchangers. Also included are several case studies from different industries where
Enerquip’s heat exchangers have saved the operators energy and money.
International Journal of Engineering Research and DevelopmentIJERD Editor
Electrical, Electronics and Computer Engineering,
Information Engineering and Technology,
Mechanical, Industrial and Manufacturing Engineering,
Automation and Mechatronics Engineering,
Material and Chemical Engineering,
Civil and Architecture Engineering,
Biotechnology and Bio Engineering,
Environmental Engineering,
Petroleum and Mining Engineering,
Marine and Agriculture engineering,
Aerospace Engineering.
An Experimental Research on Heat Transfer Enhancement of a Circular Tube with...IRJESJOURNAL
ABSTRACT:- In the literature, internal tube baffles are widely studied. There is a lack of data for baffles mounted on outside of the tubes. This study aims to fill this gap. Therefore, the effect of baffle inclination angles on heat transfer improvement has been studied experimentally. The experiments were carried out for forced convection of air on a circular tube with inclined baffles. Air has been used as the cold fluid. Experimental results for eight different velocities of air flow (2 – 20 m/s) are presented. Pitch between baffles is 12 mm.The baffle inclination angles with respect to the tube axis were 45º, 60º and 80º. Water temperature is fixed as 65 °C. According to the experimental results, the baffles with an inclination angle of 45º enhance the heat transfer over 60º and 80º around 13.7 % and 10.5 %, respectively. However, pressure drop values for 45º and 60º are 18 % higher than pressure drop values for 80º. The empirical correlations of the Nusselt number have also been obtained for each angle.
The psychrometric chart theory and applicationUsama Khan
The document discusses the psychrometric chart and various psychrometric processes involving moist air. It begins by identifying parts of the psychrometric chart and explaining how it can be used to determine moist air properties and analyze processes involving moist air. Several examples are then provided to illustrate key psychrometric processes including sensible heating/cooling, heating and humidifying, cooling and dehumidifying, adiabatic or evaporative cooling, and adiabatic mixing of moist air streams.
EXPERIMENTAL ANALYSIS OF HEAT TRANSFER AND FLUID FLOW IN MICRO-CHANNEL HEAT SINKijmech
In this paper heat transfer in single phase through micro-channels was studied. The validation of classical correlations of conventional channels to micro-channels is explored. It is found that classical approach is in good agreement with the experimental results of heat transfer in micro-channels .The material used for micro-channel heat sink (MCHS) is copper, experiments were conducted using water as cooling agent in
this study. Micro-channels are made with the help of EDM machine on the upper surface of MCHS. Variation of heat transfer rates, effect of friction factor, effect of pressure drop and variation in temperature distribution is investigated in this study. It is observed in the study that with decrease in
velocity flow friction also decreases.
Research Inventy : International Journal of Engineering and Scienceinventy
Research Inventy : International Journal of Engineering and Science
Research Inventy : International Journal of Engineering and Science is published by the group of young academic and industrial researchers with 12 Issues per year. It is an online as well as print version open access journal that provides rapid publication (monthly) of articles in all areas of the subject such as: civil, mechanical, chemical, electronic and computer engineering as well as production and information technology. The Journal welcomes the submission of manuscripts that meet the general criteria of significance and scientific excellence. Papers will be published by rapid process within 20 days after acceptance and peer review process takes only 7 days. All articles published in Research Inventy will be peer-reviewed
1) The document presents an experimental study of heat transfer through a uniformly heated vertical tube air heater.
2) The study investigates the effect of tube length, diameter, and heat flux on heat transfer and buoyancy induced airflow.
3) It was found that the heat transfer coefficient increases with increasing heat flux but decreases with increasing tube diameter and length, while air outlet temperature increases with tube length and heat flux but decreases with diameter.
Dana May Ortmann Gilbert conducted a second year lab project to optimize an acoustic heat pump. The experiment involved creating a standing wave in a tube using a loudspeaker. Different stacks made of kapton tape and PVC tubes were placed in the tube to allow heat exchange. Temperature differences of over 3°C across the stacks were achieved at resonance frequencies. The project investigated how parameters like the stack material and size, frequency, and stack position affected the temperature difference.
This document appears to be the introduction or cover page of a lab manual for a Heat Transfer lab course. It provides information about the university and engineering college where the course is taught, and lists the name and identification information for the student. It also lists the experiments that will be conducted in the lab course, including determining thermal conductivity, studying heat exchangers, measuring emissivity, and analyzing heat transfer through fins, composite walls, and during convection. The document provides an overview of the lab course and experiments but no detailed information.
Experiments were conducted to calibrate Schmidt-Boelter heat flux gauges in stagnation and shear air flows. A thermal model was developed that predicts the gauge sensitivity will have a nonlinear dependence on the heat transfer coefficient. Experimental calibration systems were built to simultaneously measure gauge response and heat flux. For stagnation flow, measured sensitivities matched the model and were used to estimate the internal thermal resistance of each gauge. For shear flow, the effect of varying gauge surface temperature on the boundary layer was included. Results matched the model with a lower effective heat transfer coefficient. The internal thermal resistance impacted gauges differently in each flow condition.
Spe113595 - Detection of Scale Deposition Using Distributed Temperature Sensingfhmutairi
This paper investigates using distributed temperature sensing (DTS) data to detect scale deposition in well tubulars. The presence of scale, which has lower thermal conductivity than tubing, affects the temperature profile measured by DTS. Higher temperatures inside the tubing would be detected within scale zones due to reduced heat transfer. The magnitude of temperature increase depends on production conditions, completion design, scale location and length. DTS could provide a novel method for detecting scale and eliminating uncertainties in deriving properties like scale thickness from continuous temperature measurements.
This lab manual document provides instructions for experiments on heat transfer in a Mechanical Engineering department. The first experiment listed is on heat transfer from a pin-fin apparatus. The objective is to calculate the heat transfer coefficient for natural and forced convection from a fin. The experiment involves measuring temperatures along a brass fin heated at one end while air passes over it naturally or in a duct. The second experiment listed is on heat transfer through a composite wall, and involves determining the total thermal resistance and conductivity of a wall made of different slab materials sandwiching a heater.
This document contains information about experiments in heat transfer lab manual. It includes 13 experiments related to different modes of heat transfer like through composite walls, critical heat flux, measurement of surface emissivity, forced convection, lagged pipe, natural convection, heat exchangers, pin-fin, Stefan-Boltzmann apparatus, thermal conductivity of concentric sphere and metal rod, transient heat conduction, heat pipe demonstration. For each experiment, it provides introduction, description of apparatus, experimentation procedure, observations, calculations and precautions.
This document discusses psychrometry, which is the study of thermodynamic properties of moist air. It outlines several important psychrometric properties used to analyze air conditioning processes, including dry bulb temperature, wet bulb temperature, dew point temperature, humidity ratio, relative humidity, specific volume, and enthalpy. It then explains common psychrometric processes like sensible heating, sensible cooling, humidification, dehumidification, and their representations on a psychrometric chart. Basic concepts in air conditioning like adiabatic mixing, bypass factor, sensible heat factor, and room sensible heat factor are also introduced.
Psychrometry: Properties and processes discusses key concepts in psychrometry including:
- Psychrometry is the study of properties of air-water vapor mixtures, commonly known as moist air. Moist air consists of dry air, water vapor, and other inert gases.
- Key psychrometric properties include specific humidity, relative humidity, dry bulb temperature, wet bulb temperature, dew point temperature, and degree of saturation.
- The sling psychrometer is used to measure wet bulb temperature by whirling two thermometers, one dry and one wet, through the air. Wet bulb depression indicates the specific humidity of air.
- Dew point temperature is the temperature at which air becomes saturated when cooled at constant
This document contains instructions and procedures for experiments in a Heat Power Engineering Laboratory. It includes a bona fide certificate, instructions for students, a list of 11 experiments, and procedures and calculations for experiments on heat transfer through natural convection from a vertical cylinder, forced convection inside a horizontal tube, and determining temperature distribution and efficiency of a pin-fin apparatus using forced convection. Diagrams, observation tables, formulas, and sample calculations are provided for each experiment. The goal is to determine heat transfer coefficients and understand heat transfer processes like natural convection, forced convection, and heat transfer through fins.
This document discusses heat transfer, including:
1. The three modes of heat transfer - conduction, convection, and radiation. It provides equations to calculate heat transfer via these modes.
2. Key heat transfer concepts like thermal conductivity, convection coefficients, emissivity, and overall heat transfer coefficients.
3. Examples of calculating heat transfer through composite walls and heat exchanger surfaces.
Hmt lab manual (heat and mass transfer lab manual)Awais Ali
This document describes procedures for 7 experiments on heat transfer:
1. Investigates Fourier's Law of heat conduction along a brass bar by measuring temperatures at points along the bar for different heat inputs.
2. Studies heat conduction along a composite bar and calculates the overall heat transfer coefficient.
3. Examines the effect of cross-sectional area changes on temperature profiles in a conductor.
4. Determines temperature profiles and heat transfer rates from radial conduction through a cylinder wall.
5. Measures thermal conductivity of non-metallic materials and compares to theory.
6. Determines thermal conductivity of liquids and gases.
7. Investigates the relationship between power input and surface temperature for free convection
The document discusses the psychrometric chart and various psychrometric processes involving moist air. It begins by identifying parts of the psychrometric chart and explaining how it can be used to determine moist air properties and analyze processes involving moist air. Several examples are then provided to illustrate key psychrometric processes including sensible heating/cooling, heating and humidifying, cooling and dehumidifying, adiabatic or evaporative cooling, and adiabatic mixing of moist air streams. Step-by-step workings are shown for each example to determine various moist air properties and mass transfer rates.
As companies examine their total cost of operations, energy usage and heat recovery deliver cost savings through increased energy utilization and efficiency. Heat exchangers offer companies the opportunity to reuse energy generated for a specific purpose instead of venting that energy to the atmosphere. Shell and tube heat exchangers are in wide use throughout the Food, Dairy, Beverage, Pharmaceutical, Chemicals, Petroleum Refining, and Utility industries. This paper briefly explores three modes of heat transfer and basic designs found in shell and tube heat exchangers. Also included are several case studies from different industries where
Enerquip’s heat exchangers have saved the operators energy and money.
International Journal of Engineering Research and DevelopmentIJERD Editor
Electrical, Electronics and Computer Engineering,
Information Engineering and Technology,
Mechanical, Industrial and Manufacturing Engineering,
Automation and Mechatronics Engineering,
Material and Chemical Engineering,
Civil and Architecture Engineering,
Biotechnology and Bio Engineering,
Environmental Engineering,
Petroleum and Mining Engineering,
Marine and Agriculture engineering,
Aerospace Engineering.
An Experimental Research on Heat Transfer Enhancement of a Circular Tube with...IRJESJOURNAL
ABSTRACT:- In the literature, internal tube baffles are widely studied. There is a lack of data for baffles mounted on outside of the tubes. This study aims to fill this gap. Therefore, the effect of baffle inclination angles on heat transfer improvement has been studied experimentally. The experiments were carried out for forced convection of air on a circular tube with inclined baffles. Air has been used as the cold fluid. Experimental results for eight different velocities of air flow (2 – 20 m/s) are presented. Pitch between baffles is 12 mm.The baffle inclination angles with respect to the tube axis were 45º, 60º and 80º. Water temperature is fixed as 65 °C. According to the experimental results, the baffles with an inclination angle of 45º enhance the heat transfer over 60º and 80º around 13.7 % and 10.5 %, respectively. However, pressure drop values for 45º and 60º are 18 % higher than pressure drop values for 80º. The empirical correlations of the Nusselt number have also been obtained for each angle.
The psychrometric chart theory and applicationUsama Khan
The document discusses the psychrometric chart and various psychrometric processes involving moist air. It begins by identifying parts of the psychrometric chart and explaining how it can be used to determine moist air properties and analyze processes involving moist air. Several examples are then provided to illustrate key psychrometric processes including sensible heating/cooling, heating and humidifying, cooling and dehumidifying, adiabatic or evaporative cooling, and adiabatic mixing of moist air streams.
EXPERIMENTAL ANALYSIS OF HEAT TRANSFER AND FLUID FLOW IN MICRO-CHANNEL HEAT SINKijmech
In this paper heat transfer in single phase through micro-channels was studied. The validation of classical correlations of conventional channels to micro-channels is explored. It is found that classical approach is in good agreement with the experimental results of heat transfer in micro-channels .The material used for micro-channel heat sink (MCHS) is copper, experiments were conducted using water as cooling agent in
this study. Micro-channels are made with the help of EDM machine on the upper surface of MCHS. Variation of heat transfer rates, effect of friction factor, effect of pressure drop and variation in temperature distribution is investigated in this study. It is observed in the study that with decrease in
velocity flow friction also decreases.
Research Inventy : International Journal of Engineering and Scienceinventy
Research Inventy : International Journal of Engineering and Science
Research Inventy : International Journal of Engineering and Science is published by the group of young academic and industrial researchers with 12 Issues per year. It is an online as well as print version open access journal that provides rapid publication (monthly) of articles in all areas of the subject such as: civil, mechanical, chemical, electronic and computer engineering as well as production and information technology. The Journal welcomes the submission of manuscripts that meet the general criteria of significance and scientific excellence. Papers will be published by rapid process within 20 days after acceptance and peer review process takes only 7 days. All articles published in Research Inventy will be peer-reviewed
1) The document presents an experimental study of heat transfer through a uniformly heated vertical tube air heater.
2) The study investigates the effect of tube length, diameter, and heat flux on heat transfer and buoyancy induced airflow.
3) It was found that the heat transfer coefficient increases with increasing heat flux but decreases with increasing tube diameter and length, while air outlet temperature increases with tube length and heat flux but decreases with diameter.
HEAT TRANSFER AND FLOW FRICTION CHARACTERISTICS OF SOLAR WATER HEATER WITH IN...IAEME Publication
Experimental investigation of friction factor and heat transfer characteristics of thermosyphone solar water heater with flat plate solar collector fitted with full length baffle of 10cm
pitch have been presented. The flow regime is laminar for this study with the Reynolds number range 124 to 258. The experimental data obtained were compared with those obtained from plain tube data. The effects of full length baffle inside the tube on heat transfer and friction factor were presented.
This document summarizes an experimental study on heat transfer and flow friction characteristics of a solar water heater with inserted baffles inside tubes. The study found that inserting full-length baffles inside tubes enhanced heat transfer and improved solar water heater performance compared to plain tubes. Maximum collector efficiency and outlet fluid temperature occurred at 12:45 hours for both baffled and plain tubes, but values were higher for baffled tubes. Friction factor was also lower for the baffled tube design at the point of maximum outlet temperature. The baffled tube design improved heat transfer and solar water heater performance relative to the plain tube design.
The document summarizes research on the suitability of heat exchangers for use as solar receivers in solar thermal power applications. It discusses two main solar collector technologies - point focusing and line focusing collectors - and the receiver design requirements for each. It then outlines the methodology used, which includes designing and fabricating a shell and helical tube heat exchanger, modeling a porous disc line receiver with CFD, simulating different configurations and working fluids, and determining parameters for maximum efficiency. Literature on existing receiver models is reviewed and key findings are summarized. Experimental work involving a shell and helical tube receiver with nanofluid is described and optimization of parameters is discussed. Results from CFD analysis of the porous disc receiver showing heat transfer and fluid
SUMMARYThis report represents the outcome of heat exchang.docxpicklesvalery
SUMMARY:
This report represents the outcome of heat exchange via 4 tubes that are fitted within the shell with four thermocouples to determine the temperature for every pass, two passes for the hot water (in/out) and two for the cold water (in/out). The experiment was commencing according to the amount of hot and cold water that was supplied to the inputs of the heat exchange. The supply was managed by the use of taps that would restrain or allow the gush of water. The temperature for the inputs was constant in the most of the 5 runs while the outputs had been changed due to heat exchange occurring within the shell. Hot water had lost temperature while cold water had gained temperature.
An experiment was set up to resolve the energy losses that affect the hot and cold water, by using thermodynamic laws. During the experiment the water gush rates were measured carefully and the data had been collected and entered to allow the calculations of the energy losses that came out. Finally, it was discovered the heat had been exchanged from the hot into the cold to maintain the temperature inside the shell.
Contents:
SUMMARY:i
1.0INTRODUCTION:1
2.0AIM:1
3.0EXPERIMENTAL METHOD:1
4.0EXPERIMENTAL DATA:2
5.0DATA ANALYSIS:2
6.0DISCUSSION:4
7.0CONCLUSION4
ii
INTRODUCTION:
The exchanger consists of a number of tubes that sit inside a shell that allows cold water to flow through them. Hot water flow through the bordering shell and the two fluids exchange heat. Heat exchanger can come in various forms and as such can have many different motives. A radiator in a car and a boiler in a steam engine are both heat exchanger with the radiator cooling the engine, and the boiler exchanging raw materials into steam that can be used for power generation. The heat exchanger that has been used in this experiment was a basic shell and tube style as shown in figure 1. A Jenco digital thermometer and Jenco thermocouple switches are used in the heat exchanger set up to allow to calculate the measurements for the experiment. Flow meters fitted on the inlet of hot and cold water taps are used to change volume flow rates.
AIM:
The aim of the report is to evaluate the heat losses that came out for the hot water. The experiment will carry of recording temperatures and flow rates and then calculating other possible factors that may cause heat loss.EXPERIMENTAL METHOD:
1) Be familiar with the different part of the experimental.
2) Turn on the cold and hot water taps.
3) Turn valves for the cold water at an initial flow rate (approximate 15 L/min for cold water) Make sure that all the water passes through the flow meters (turn off one of the valves in each water supply line)
4) Water for couple of minutes before reading the data.
5) Take the temperature reading for the thermocouples 1 to 5 by press the Jenco thermocouple buttons.
6) Repeat steps from 3) to 5) for 5 different flow rate combinations.EXPERIMENTAL DATA:
Room temperature: 15°C
Run/Quantities
(L/min)
(L/min)
in ...
The document summarizes an experiment to determine heat transfer coefficients in a cross-flow plate heat exchanger under both continuous and batch operations. For continuous operation, the heat transfer rate and coefficient increased with increasing cold water flow rate. The heat transfer coefficient was highest at around 5 gallons per minute. For batch operation, the heat transfer coefficient was determined to be 7490 ± 300 W/m2K using linear regression modeling, which was higher than continuous operation. Heat losses to the environment likely contributed to the lower coefficient in continuous operation compared to batch.
This document describes an experimental study of heat transfer in a rectangular duct with and without internal V-shaped ribs. Experiments were conducted with air flow in turbulent regime (Reynolds numbers 3000-18000) in smooth duct and ducts with continuous or discrete internal V-shaped ribs. Temperature and pressure measurements were taken to determine heat transfer coefficients and friction factors for different configurations. Results showed that continuous ribs enhanced heat transfer more than discrete ribs, but also increased pressure drop more substantially. Heat transfer enhancement was dependent on rib geometry and position.
Analysis of effect gapsize to counter current flow limitation knep bali 2014moh rohmatulloh
Three methods were used to analyze the existence of counter current flow limitation (CCFL) in vertical rectangular narrow channels with varying gap sizes:
1. Comparing the time it took for cooling water to flow through the channel without heating versus with initial heating of the plates to 500°C. Smaller gap sizes resulted in longer times, indicating stronger CCFL effects.
2. Analyzing the vapor and water superficial velocities - CCFL occurs when the vapor velocity is higher than the water velocity. For all gap sizes, the vapor velocity was higher, showing CCFL was present.
3. Examining the rewetting time and critical heat flux (CHF) values. Under the same initial temperature,
The document describes heat exchangers and experiments conducted using a shell and tube heat exchanger and a plate heat exchanger. It discusses three types of fluid flow - parallel, counter, and cross-flow. Experiments were conducted with both exchangers under parallel and counter-flow configurations. Temperature and flow rate data was collected and used to calculate effectiveness, heat transfer coefficients, and log mean temperature difference. The results showed that the counter-flow configuration had higher effectiveness compared to parallel flow in both exchangers.
This document analyzes critical heat flux (CHF) in vertical rectangular narrow channels. It summarizes several previous studies that experimentally analyzed CHF in narrow channels using different fluids, channel dimensions, and heating conditions. The document then describes the author's own experiment on CHF using a vertical stainless steel plate with a 1 mm gap. Results showed the highest CHF occurred at the middle of the plate and CHF decreased towards the upper and lower parts. CHF values were compared to several existing correlations, with some correlations showing better agreement with results from different plate positions. The study contributes to understanding CHF in narrow channels.
Experimental study of the structure of a thermal plume inside a rectangular t...IOSR Journals
The objective of this work is to experimentally simulate a plume developing inside a horizontal
tunnel. The experimental device used in this simulation is essentially constituted of a hot disk, a rectangular
tunnel and a ventilation system. The hot disk is heated by Joule effect to a constant and uniform temperature,
and placed inside the tunnel. The hot source generates a thermal plume. We first studied the evolution of the
thermal plume without ventilation system. The study of the average and fluctuating thermal and dynamic fields
shows three zones during the vertical evolution of the free plume. A first zone close to the source, serving to the
plume supply in fresh air, is characterized by the apparition of three escapes of the thermal plume. Followed by
a second zone where the main escape undergoes a contraction. Finally, a third zone where the thermal plume
accumulates and undergoes a flow upstream named backlayering and a flow downstream that borders the
ceiling to leave by the free part of the tunnel.
Experimental Study of Heat Transfer Analysis in Vertical Rod Bundle of Sub Ch...IJMER
The ability of the fluid in taking the heat generated by the nuclear reactor fuel is one
important aspect of reactor safety. These capabilities must be kept high enough to maintain integrity of
the fuel cladding as inside retaining radioactive substances. Study characteristics of forced convection in
the fluid water using seven vertical cylinders heated uniformly in the composition ratio of hexagons with
Pitch/Diameter (P/D) at 1.58 in the hexagon-shaped shell model of the reactor core test equipment in
order to obtain the correlation equation displacement convection force. In this study, the heat flux and
velocity of fluid flow greatly affect the temperature of the fluid. The greater the heat flux given the fluid
temperature is getting higher because of the greater heat flux on the cylinder heating the heat absorbed
by the fluid is also getting bigger. Similarly, the velocity of fluid flow, increasing the velocity of the fluid
flow, the smaller the fluid temperature because by increasing the velocity of fluid flow in the sub channel
the heat received by the fluid on the wane led to the smaller fluid temperature. Heat transfer coefficient
results obtained at a velocity flow of 0.1 m s-1
is 500 Wm-2K
-1
to 23 500 Wm-2K
-1
, at a velocity flow of 0.3
m s
-1
is 3 100 Wm-2K
-1
up to 2 800 Wm-2K
-1
and in velocity flow of 0.5 m s-1
is 3 500 Wm-2K
-1
to 32 500
Wm-2K
-1
. In this experimental study use forced convection flow has a Reynolds number range from 3 991
to 29 537 and Graetz numbers from 1 371 to 41 244. The correlation of forced convection heat transfer as
follows: Nu forced = 1.641 Gz 0.4267
IOSR Journal of Mechanical and Civil Engineering (IOSR-JMCE) is an open access international journal that provides rapid publication (within a month) of articles in all areas of mechanical and civil engineering and its applications. The journal welcomes publications of high quality papers on theoretical developments and practical applications in mechanical and civil engineering. Original research papers, state-of-the-art reviews, and high quality technical notes are invited for publications.
Thermal diffusivity is a physical property that measures how quickly a material responds to changes in thermal energy. It is the ratio of a material's ability to conduct heat to its ability to store heat. Materials with higher thermal diffusivity respond faster to temperature changes. Thermal diffusivity can be measured directly using methods like the flash method or indirectly using temperature history charts. Newton's Law of Cooling states that the rate of heat loss from a body is proportional to the difference between the body's temperature and the temperature of its surroundings. This law can be used to model and predict how quickly hot water in pipes will cool over time.
International Journal of Computational Engineering Research(IJCER) is an intentional online Journal in English monthly publishing journal. This Journal publish original research work that contributes significantly to further the scientific knowledge in engineering and Technology.
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.
International Journal of Computational Engineering Research(IJCER)ijceronline
International Journal of Computational Engineering Research(IJCER) is an intentional online Journal in English monthly publishing journal. This Journal publish original research work that contributes significantly to further the scientific knowledge in engineering and Technology.
1) The document analyzes heat transfer in a double pipe heat exchanger with helical tape inserts in the annulus of the inner pipe using computational fluid dynamics (CFD).
2) A 3D model is developed and simulations are run using the SST k-ω turbulent model to analyze how helical tape inserts influence heat transfer and pressure drop at different pitch lengths and Reynolds numbers.
3) The results show that helical tape inserts increase the heat transfer rate but also increase pressure drop due to flow disruption. Nusselt number and friction factor are found to correlate well with Reynolds number for enhancing heat transfer.
Experimental Investigation on the Heat Transfer Coefficient of the Thermosyph...IJERA Editor
This document presents an experimental investigation of the heat transfer coefficient of a two-phase closed thermosyphon with different cross-section shapes (circular, square, and rectangular). Methanol was used as the working fluid. Thermocouples were used to measure the temperature distribution across the thermosyphon surface under varying input powers (200-500W). The results showed that the heat transfer coefficient increases with increasing input power. The maximum heat transfer coefficient of 1815 W/m2C was obtained for the square cross-section at an input power of 500W. Thermal resistance decreases with increasing input power. Equations for calculating hydraulic diameter, input/output heat rates, average heat transfer rate, thermal resistance,
Experimental Investigation on the Heat Transfer Coefficient of the Thermosyph...
FINAL_POSTER
1. Spatial and Temporal Analysis of Heat Transport through Saturated Sediments
in Sandbox and Flume Models
Mitchell Schutte, John Teppler, and Cassandra Wolf
Department of Geosciences, University of Wisconsin-Milwaukee, Milwaukee, Wisconsin
Geosciences Undergraduate
Research
Abstract
Spatial and temporal behavior of heat transport through fully saturated sediment was studied using a
variety of experimental models. Knowledge of heat transport was obtained by implementation of a
sandbox model. Point-based transducers were used to collect temperature and pressure readings
from input and output tanks. Once the model was fully saturated with warm water and steady state
flow was obtained, warm water was removed from the input tank and replaced to a constant cold ice
water flow. The transducer data allowed for interpretation of the dynamics of cold fronts through the
saturated zone and help generate a computer model showing heat changes through the sediment,
through time. Increasing the scale, transducers allowed study of flow through the saturated sand of
the flume. The transducers, through time, were able to read a gradual decrease in temperature in the
flow of the saturated sediment and an increase in stream temperature. After calibration times were
monitored, constants of fluid properties between the saturated zone and the stream flow of the flume
were established. With this background, distributed temperature sensing (DTS) through fiber optic
cables buried in the flume sediment were implemented with the capabilities to measure temperature
changes of 0.01 °C. Heat was induced upstream from the DTS to measure temperature variations
along the stream bed surface. The DTS refined prior conclusions of the relationships of saturated
flow rate to heat transport. This research advanced understanding of the use, application, and
capabilities of the DTS technology. Moving forward continued DTS research will be used to monitor
seasonal and diurnal changes in the hyporheic zone of streambeds of the Fox River.
Objectives
Evaluate small scale heat flow through saturated sediment in sandbox model
Understand fluid dynamics of flume environment
Apply Distributed Temperature Sensing calibration and implementation in large scale laboratory
setting
Understand how to properly implement long term DTS field study
Ÿ
Ÿ
Ÿ
Ÿ
Conclusion
In Figure 9, the vertical black line indicates 240 minutes representing the time the heat was
introduced. The double black horizontal line represents the temperature the stream and ground
water reached. The goal was to obtain equal temperature through the stream and ground. The
equilibrium was not perfectly met, but the data shows an approximate 0.5 °C difference. After the 4
hours, all transducers both in sediment and stream, located 0.13 and 1.74 meters from heat source,
showed immediate increase in temperature response. The DTS wrapped cylinder laid within the
transducers boundary, coincided with immediate temperature response. Figure 10 combines 480
individual files creating a plot of time vs. length as a function of temperature. The top half of the
graph validates sediment transducer data of the initial 4 hour decrease of temperature. After the heat
was introduced at the black line, the slow warming color gradient shows the most dramatic increase
of temperature at the first 20 meters of wrapped cable. After the 4 hours of heat, the entire length of
wrapped cable shows a detectable raise in temperature. Figure 8 is a complete temperature vs.
length plot showing the full potential of how much cable can be deployed. The red circle highlights
the last 180 meters of cable applied in this experiment. It is important to note there is a considerable
amount of unused cable. Field settings would provide better use of the full cable length and deliver
more meaningful data. Future work for this project involves the installation of the full 1000 meter
cable in the Fox River.
Sandbox
The sandbox model was performed to demonstrate heat flow through saturated, well-sorted sand.
The dimensions of the sandbox are 1.175 meters by 0.500 meters. Head decreases to the right, from
the input tank, to the output tank. One transducer was placed in the input tank and two were
staggered top to bottom in the output tank. To start the experiment, hot water (42 °C) was injected
into the model for 2 hours until the output transducers showed an adequate temperature elevation
(23-30 °C). The hot water was drained from the input tank, filled with ice, and constant cold water (4
°C) filled the input tank and proceeded to progress through the model. Figure 2 shows the output
transducers interact with the cold front 3 hours into the experiment. From 3 to 5 hours the cold front
continued to decline the output transducers temperature until the input and output become equal.
Modeling Temperature Flow with TOUGH2
The TOUGH2 petrasim model is a 2-D representation of the sandbox system, with the same
dimensions, to simulate a similar system. A pressure gradient was assigned based on the head
gradient. Instead of an injection well on the right, a one grid block wide column was defined as an
extremely high density rock with a temperature of 4 °C to stimulate heat flow. This computer model
starts at hour 2 of the experiment, so the rest of the rock was given and initial temperature of 27 °C,
an average of the top and bottom output transducers. There was also no output tank in the model,
only a no flow boundary.
Distributed Temperature Sensing
Distributed Temperature Sensing (DTS) is a new technology that recently has been fine tuned for
geologic use. The applications range from surface and near surface hydrologic processes, ground to
surface water interaction, bore-hole circulation, and sensing temperatures of water, air, and various
other media. The DTS machine has optical connectors for multiple lengths and varieties of fiber optic
cables. Light is sent from a laser starting at DTS machine output, through the entire length of cable
and back. The temperature is measured from the ratio of backscattered photons: Stokes (lower
frequency) and Anti-Stokes (higher frequency). As temperature increases, the light photons vibrate at
a higher frequency, changing the ratio, resulting in the systems calculation of temperature along the
cable.
After flume dynamics were observed (Figure 5), appropriate background knowledge allows
implementation of DTS unit. After test ran for 4 hours, the stream to groundwater temperature has
converged steadily, the DTS then starts to capture induced heat flux through space and time, while
the stream and sediment transducers validate recorded DTS data. This 8 hour experiment consisted
of calibrating the temperature offset of the fiber optic cable and setting measurement time intervals.
This system allows for temperature measurement every 1 meter with 0.01 °C precision.
Acknowledgments: Dr. Weon Shik Han, Jack P. Graham
Flume
The Flume is a laboratory controlled model of stream sediment and flow. It is an elongated artificial
stream bed that recirculates water at variable flow velocities. The flume dimensions are 10.36m x
1.23m x 1.23m. This controlled environment provides a replicable setting for each consecutive
experiment. These experiments progress knowledge of the natural stream and sediment
interactions, and how the relationship of the two react to induced temperature.
The first experiment, seen in Figure 5, shows the interaction of stream and ground water
temperature over time with constant flow. This step is necessary to understand the natural system
properties over extended time periods. One can view this as a form of calibration. The stream flow
was initiated at a constant rate of 0.28 m/s for 5.5 hours.
Utilizing 5 buried point-based transducers, in 2 meter interval spacing (1m, 3m, 5m, 7m, and 9m),
the groundwater temperature was recorded throughout the length of the sediment. The stream
temperature was captured separately by 2 floating transducers placed near the upstream, input of
flow, and downstream, recirculating output tank.
Initially, groundwater data showed warmer temperatures ranging from 14.5-16.2 °C whereas stream
temperatures varied from 6.5-7.5 °C. Over the 5.5 hours, the temperature differences between the
two decreased, heading towards a steady state equilibrium temperature. Final experimental data
shows groundwater temperatures at 11.5-12.8 °C and stream temperatures reaching 9.8-10.5 °C.*
Figure 5 allows for interpolation of the ground and stream water reaching calibrated equilibrium in 8
hours at 11.8 °C.
Figure 4
Figure 1
Figure 3a
3d
Using Sensornet ORYX DTS unit accompanied by 1000 meter Brugg fiber optic cable, the calibration
was set to store data points formatted as separate distributed temperature files every 1 minute, while
the transducers collect data through one measurement per minute forming one continuous file.
Separate drainage from input and output tanks create an uneven desaturation of sediment, causing
sediment at 5 meters (center) to retain the most water. The cable was tightly wrapped around a
hollow cylindrical tube of 1.034 meters in length with a circumference of 0.7037 meters. The cable
circled the tube approximately 270 times validating the last 180 meters of measurements. The
wrapped cable was then buried in the sediment aligning the center of the tubing to the 5 meter
center of the flume. 1000 Watt titanium submersible heating device was placed 0.4 meters upstream
from DTS burial site. Two sediment and stream transducers were placed upstream and downstream,
4.35 and 5.96 meters respectfully, from the input tank.
Compared to the experiment, the simulated model shows the first cold front reaching the other side
of the tank at 1 hour, seen in Figure 3b. The same time the output transducers start to show a
decrease in temperature. The cold front continues to decrease the temperature as it travels to the
right and runs for 9 hours; since there is no output tank in the simulation, an accumulation of slightly
warmer temperatures linger on the right side.
Though the sandbox data ends at 3 hours after the cold water introduction, the simulated data
continues to show heat flow for 9 hours. This discrepancy could be due, in part, to the transducer
data recording only two output points whereas the simulation gathered data at every grid block, at
every time step. The discrepancy in the experimental data comes from the output tank allowing
warm water to leave the system whereas the simulation necessitates an equilibrium to be reached
with no removal of water.
Figure 6a 6b 6c
Figure 7 Figure 8
Figure 9a 9b
Figure 10
3b
3c
Output TankInput Tank
1.175 Meters
1 Hour
9 Hours4 Hours
Head Gradient
10 m 5 m 1 m
Figure 5
1.034
Meters
Figure 2