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Heat Transfer in Flat-Plate Solar Air-Heating Collectors
Advanced Computational Methods in Heat Transfer VI, C.A. Brebbia & B. Sunden (Editors) © 2000 WIT Press, www.witpress.com, ISBN 1-85312-818-X Heat transfer in flat-plate solar air-heating collectors Y. Nassar & E. Sergievsky Abstract All energy systems involve processes of heat transfer. Solar energy is obviously a field where heat transfer plays crucial role. Solar collector represents a heat exchanger, in which receive solar radiation, transform it to heat and transfer this heat to the working fluid in the collector's channel The radiation and convection heat transfer processes inside the collectors depend on the temperatures of the collector components and on the hydrodynamic characteristics of the working fluid. Economically, solar energy systems are at best marginal in most cases. In order to realize the potential of solar energy, a combination of better design and performance and of environmental considerations would be necessary. This paper describes the thermal behavior of several types of flat-plate solar air-heating collectors. 1 Introduction Nowadays the problem of utilization of solar energy is very important. By economic estimations, for the regions of annual incident solar radiation not less than 4300 MJ/m^ pear a year (i.e. lower 60 latitude), it will be possible to cover - by using an effective flat-plate solar collector- up to 25% energy demand in hot water supply systems and up to 75% in space heating systems. Solar collector is the main element of any thermal solar system. Besides of large number of scientific publications, on the problem of solar energy utilization, for today there is no common satisfactory technique to evaluate the thermal behaviors of solar systems, especially the local characteristics of the solar collector. -
TIE-35: Transmittance of Optical Glass
DATE October 2005 . PAGE 1/12 TIE-35: Transmittance of optical glass 0. Introduction Optical glasses are optimized to provide excellent transmittance throughout the total visible range from 400 to 800 nm. Usually the transmittance range spreads also into the near UV and IR regions. As a general trend lowest refractive index glasses show high transmittance far down to short wavelengths in the UV. Going to higher index glasses the UV absorption edge moves closer to the visible range. For highest index glass and larger thickness the absorption edge already reaches into the visible range. This UV-edge shift with increasing refractive index is explained by the general theory of absorbing dielectric media. So it may not be overcome in general. However, due to improved melting technology high refractive index glasses are offered nowadays with better blue-violet transmittance than in the past. And for special applications where best transmittance is required SCHOTT offers improved quality grades like for SF57 the grade SF57 HHT. The aim of this technical information is to give the optical designer a deeper understanding on the transmittance properties of optical glass. 1. Theoretical background A light beam with the intensity I0 falls onto a glass plate having a thickness d (figure 1-1). At the entrance surface part of the beam is reflected. Therefore after that the intensity of the beam is Ii0=I0(1-r) with r being the reflectivity. Inside the glass the light beam is attenuated according to the exponential function. At the exit surface the beam intensity is I i = I i0 exp(-kd) [1.1] where k is the absorption constant. -
Reflectance and Transmittance Sphere
Reflectance and Transmittance Sphere Spectral Evolution four inch portable reflectance/ transmittance sphere is ideal for measuring vegetation physiological states SPECTRAL EVOLUTION offers a portable, compact four inch reflectance/transmittance (R/T) integrating sphere for measuring the reflectance and transmittance of vegetation. The 4 inch R/T sphere is lightweight and portable so you can take it into the field for in situ meas- urements, delivered with a stand as well as a ¼-20 mount for use with tripods. When used with a SPECTRAL EVOLUTION spectrometer or spectroradiometer such as the PSR+, RS-3500, RS- 5400, SR-6500 or RS-8800, it delivers detailed information for measurements of transmittance and reflectance modes. Two varying light intensity levels (High and Low) allow for a broader range of samples to be measured. Light reflected or transmitted from a sample in a sphere is integrated over a full hemisphere, with measurements insensitive to sample anisotropic directional reflectance (transmittance). This provides repeatable measurements of a variety of samples. The 4 inch portable R/T sphere can be used in vegetation studies such as, deriving absorbance characteristics, and estimating the leaf area index (LAI) from radiation reflected from a canopy surface. The sphere allows researchers to limit destructive sampling and provides timely data acquisition of key material samples. The R/T sphere allows you to collect all diffuse light reflected from a sample – measuring total hemispherical reflectance. You can measure reflectance and transmittance, and calculate absorption. You can select the bulb inten- sity level that suits your sample. A white reference is provided for both reflectance and transmittance measurements. -
Heat Transfer (Heat and Thermodynamics)
Heat Transfer (Heat and Thermodynamics) Wasif Zia, Sohaib Shamim and Muhammad Sabieh Anwar LUMS School of Science and Engineering August 7, 2011 If you put one end of a spoon on the stove and wait for a while, your nger tips start feeling the burn. So how do you explain this simple observation in terms of physics? Heat is generally considered to be thermal energy in transit, owing between two objects that are kept at di erent temperatures. Thermodynamics is mainly con- cerned with objects in a state of equilibrium, while the subject of heat transfer probes matter in a state of disequilibrium. Heat transfer is a beautiful and astound- ingly rich subject. For example, heat transfer is inextricably linked with atomic and molecular vibrations; marrying thermal physics with solid state physics|the study of the structure of matter. We all know that owing matter (such as air) in contact with a heated object can help `carry the heat away'. The motion of the uid, its turbulence, the ow pattern and the shape, size and surface of the object can have a pronounced e ect on how heat is transferred. These heat ow mechanisms are also an essential part of our ventilation and air conditioning mechanisms, adding comfort to our lives. Importantly, without heat exchange in power plants it is impossible to think of any power generation, without heat transfer the internal combustion engine could not drive our automobiles and without it, we would not be able to use our computer for long and do lengthy experiments (like this one!), without overheating and frying our electronics. -
(CFD) Modelling and Application for Sterilization of Foods: a Review
processes Review Computational Fluid Dynamics (CFD) Modelling and Application for Sterilization of Foods: A Review Hyeon Woo Park and Won Byong Yoon * ID Department of Food Science and Biotechnology, College of Agricultural and Life Science, Kangwon National University, Chuncheon 24341, Korea; [email protected] * Correspondence: [email protected]; Tel.: +82-33-250-6459 Received: 30 March 2018; Accepted: 23 May 2018; Published: 24 May 2018 Abstract: Computational fluid dynamics (CFD) is a powerful tool to model fluid flow motions for momentum, mass and energy transfer. CFD has been widely used to simulate the flow pattern and temperature distribution during the thermal processing of foods. This paper discusses the background of the thermal processing of food, and the fundamentals in developing CFD models. The constitution of simulation models is provided to enable the design of effective and efficient CFD modeling. An overview of the current CFD modeling studies of thermal processing in solid, liquid, and liquid-solid mixtures is also provided. Some limitations and unrealistic assumptions faced by CFD modelers are also discussed. Keywords: computational fluid dynamics; CFD; thermal processing; sterilization; computer simulation 1. Introduction In the food industry, thermal processing, including sterilization and pasteurization, is defined as the process by which there is the application of heat to a food product in a container, in an effort to guarantee food safety, and extend the shelf-life of processed foods [1]. Thermal processing is the most widely used preservation technology to safely produce long shelf-lives in many kinds of food, such as fruits, vegetables, milk, fish, meat and poultry, which would otherwise be quite perishable. -
Recent Developments in Heat Transfer Fluids Used for Solar
enewa f R bl o e ls E a n t e n r e g Journal of y m a a n d d n u A Srivastva et al., J Fundam Renewable Energy Appl 2015, 5:6 F p f p Fundamentals of Renewable Energy o l i l ISSN: 2090-4541c a a n t r i DOI: 10.4172/2090-4541.1000189 o u n o s J and Applications Review Article Open Access Recent Developments in Heat Transfer Fluids Used for Solar Thermal Energy Applications Umish Srivastva1*, RK Malhotra2 and SC Kaushik3 1Indian Oil Corporation Limited, RandD Centre, Faridabad, Haryana, India 2MREI, Faridabad, Haryana, India 3Indian Institute of Technology Delhi, New Delhi, India Abstract Solar thermal collectors are emerging as a prime mode of harnessing the solar radiations for generation of alternate energy. Heat transfer fluids (HTFs) are employed for transferring and utilizing the solar heat collected via solar thermal energy collectors. Solar thermal collectors are commonly categorized into low temperature collectors, medium temperature collectors and high temperature collectors. Low temperature solar collectors use phase changing refrigerants and water as heat transfer fluids. Degrading water quality in certain geographic locations and high freezing point is hampering its suitability and hence use of water-glycol mixtures as well as water-based nano fluids are gaining momentum in low temperature solar collector applications. Hydrocarbons like propane, pentane and butane are also used as refrigerants in many cases. HTFs used in medium temperature solar collectors include water, water- glycol mixtures – the emerging “green glycol” i.e., trimethylene glycol and also a whole range of naturally occurring hydrocarbon oils in various compositions such as aromatic oils, naphthenic oils and paraffinic oils in their increasing order of operating temperatures. -
Beer-Lambert Law: Measuring Percent Transmittance of Solutions at Different Concentrations (Teacher’S Guide)
TM DataHub Beer-Lambert Law: Measuring Percent Transmittance of Solutions at Different Concentrations (Teacher’s Guide) © 2012 WARD’S Science. v.11/12 For technical assistance, All Rights Reserved call WARD’S at 1-800-962-2660 OVERVIEW Students will study the relationship between transmittance, absorbance, and concentration of one type of solution using the Beer-Lambert law. They will determine the concentration of an “unknown” sample using mathematical tools for graphical analysis. MATERIALS NEEDED Ward’s DataHub USB connector cable* Cuvette for the colorimeter Distilled water 6 - 250 mL beakers Instant coffee Paper towel Wash bottle Stir Rod Balance * – The USB connector cable is not needed if you are using a Bluetooth enabled device. NUMBER OF USES This demonstration can be performed repeatedly. © 2012 WARD’S Science. v.11/12 1 For technical assistance, All Rights Reserved Teacher’s Guide – Beer-Lambert Law call WARD’S at 1-800-962-2660 FRAMEWORK FOR K-12 SCIENCE EDUCATION © 2012 * The Dimension I practices listed below are called out as bold words throughout the activity. Asking questions (for science) and defining Use mathematics and computational thinking problems (for engineering) Constructing explanations (for science) and designing Developing and using models solutions (for engineering) Practices Planning and carrying out investigations Engaging in argument from evidence Dimension 1 Analyzing and interpreting data Obtaining, evaluating, and communicating information Science and Engineering Science and Engineering Patterns -
Convectional Heat Transfer from Heated Wires Sigurds Arajs Iowa State College
Iowa State University Capstones, Theses and Retrospective Theses and Dissertations Dissertations 1957 Convectional heat transfer from heated wires Sigurds Arajs Iowa State College Follow this and additional works at: https://lib.dr.iastate.edu/rtd Part of the Physics Commons Recommended Citation Arajs, Sigurds, "Convectional heat transfer from heated wires " (1957). Retrospective Theses and Dissertations. 1934. https://lib.dr.iastate.edu/rtd/1934 This Dissertation is brought to you for free and open access by the Iowa State University Capstones, Theses and Dissertations at Iowa State University Digital Repository. It has been accepted for inclusion in Retrospective Theses and Dissertations by an authorized administrator of Iowa State University Digital Repository. For more information, please contact [email protected]. CONVECTIONAL BEAT TRANSFER FROM HEATED WIRES by Sigurds Arajs A Dissertation Submitted to the Graduate Faculty in Partial Fulfillment of The Requirements for the Degree of DOCTOR 01'' PHILOSOPHY Major Subject: Physics Signature was redacted for privacy. In Chapge of K or Work Signature was redacted for privacy. Head of Major Department Signature was redacted for privacy. Dean of Graduate College Iowa State College 1957 ii TABLE OF CONTENTS Page I. INTRODUCTION 1 II. THEORETICAL CONSIDERATIONS 3 A. Basic Principles of Heat Transfer in Fluids 3 B. Heat Transfer by Convection from Horizontal Cylinders 10 C. Influence of Electric Field on Heat Transfer from Horizontal Cylinders 17 D. Senftleben's Method for Determination of X , cp and ^ 22 III. APPARATUS 28 IV. PROCEDURE 36 V. RESULTS 4.0 A. Heat Transfer by Free Convection I4.0 B. Heat Transfer by Electrostrictive Convection 50 C. -
THERMODYNAMICS, HEAT TRANSFER, and FLUID FLOW, Module 3 Fluid Flow Blank Fluid Flow TABLE of CONTENTS
Department of Energy Fundamentals Handbook THERMODYNAMICS, HEAT TRANSFER, AND FLUID FLOW, Module 3 Fluid Flow blank Fluid Flow TABLE OF CONTENTS TABLE OF CONTENTS LIST OF FIGURES .................................................. iv LIST OF TABLES ................................................... v REFERENCES ..................................................... vi OBJECTIVES ..................................................... vii CONTINUITY EQUATION ............................................ 1 Introduction .................................................. 1 Properties of Fluids ............................................. 2 Buoyancy .................................................... 2 Compressibility ................................................ 3 Relationship Between Depth and Pressure ............................. 3 Pascal’s Law .................................................. 7 Control Volume ............................................... 8 Volumetric Flow Rate ........................................... 9 Mass Flow Rate ............................................... 9 Conservation of Mass ........................................... 10 Steady-State Flow ............................................. 10 Continuity Equation ............................................ 11 Summary ................................................... 16 LAMINAR AND TURBULENT FLOW ................................... 17 Flow Regimes ................................................ 17 Laminar Flow ............................................... -
Forced Convection Heat Transfer Convection Is the Mechanism of Heat Transfer Through a Fluid in the Presence of Bulk Fluid Motion
Forced Convection Heat Transfer Convection is the mechanism of heat transfer through a fluid in the presence of bulk fluid motion. Convection is classified as natural (or free) and forced convection depending on how the fluid motion is initiated. In natural convection, any fluid motion is caused by natural means such as the buoyancy effect, i.e. the rise of warmer fluid and fall the cooler fluid. Whereas in forced convection, the fluid is forced to flow over a surface or in a tube by external means such as a pump or fan. Mechanism of Forced Convection Convection heat transfer is complicated since it involves fluid motion as well as heat conduction. The fluid motion enhances heat transfer (the higher the velocity the higher the heat transfer rate). The rate of convection heat transfer is expressed by Newton’s law of cooling: q hT T W / m 2 conv s Qconv hATs T W The convective heat transfer coefficient h strongly depends on the fluid properties and roughness of the solid surface, and the type of the fluid flow (laminar or turbulent). V∞ V∞ T∞ Zero velocity Qconv at the surface. Qcond Solid hot surface, Ts Fig. 1: Forced convection. It is assumed that the velocity of the fluid is zero at the wall, this assumption is called no‐ slip condition. As a result, the heat transfer from the solid surface to the fluid layer adjacent to the surface is by pure conduction, since the fluid is motionless. Thus, M. Bahrami ENSC 388 (F09) Forced Convection Heat Transfer 1 T T k fluid y qconv qcond k fluid y0 2 y h W / m .K y0 T T s qconv hTs T The convection heat transfer coefficient, in general, varies along the flow direction. -
Low Outgassing of Silicon-Based Coatings on Stainless Steel Surfaces for Vacuum Applications
Low Outgassing of Silicon-Based Coatings on Stainless Steel Surfaces for Vacuum Applications David A. Smith, Martin E. Higgins Restek Corporation, 110 Benner Circle Bellefonte, PA 16823, www.restekcoatings.com Bruce R.F. Kendall Elvac Laboratories 100 Rolling Ridge Drive, Bellefonte, PA 16823 Performance Coatings This presentation was developed through the collaborative efforts of Restek Performance Coatings and Bruce Kendall of Elvac Labs. Restek applied the coatings to vacuum components and Dr. Kendall developed, performed and interpreted the experiments to evaluate the coating performance. lit. cat.# RPC-uhv3 1 Objective Evaluate comparative outgassing properties of vacuum components with and without amorphous silicon coatings Performance Coatings lit. cat.# RPC-uhv3 2 Theoretical Basis – Heat Induced Outgassing • Outgassing rate (F) in monolayers per sec: F = [exp (-E/RT)] / t’ t’ = period of oscillation of molecule perp. to surface, ca. 10-13 sec E = energy of desorption (Kcal/g mol) R = gas constant source: Roth, A. Vacuum Technology, Elsevier Science Publishers, Amsterdam, 2nd ed., p. 177. • Slight elevation of sample temperature accelerates outgassing rate exponentially Performance Coatings The design of the first set of experiments allowed the isolation and direct comparison of outgassing rates with increasing temperature. By applying heat, the outgassing rates are exponentially increased for the purpose of timely data collection. These comparisons with experimental controls will directly illustrate the differences incurred by the applied coatings. lit. cat.# RPC-uhv3 3 Experimental Design – Heated Samples • Turbo pump for base pressures to 10-8 Torr – pumping rate between gauge and pump: 12.5 l/sec (pump alone: 360 l/sec) – system vent with dry N2 between thermal cycles • Comparative evaluation parts – a-silicon coated via CVD (Silcosteel®-UHV); 3D deposition – equally treated controls without deposition Performance Coatings The blue sample (left) was a standard coating commercially available through Restek. -
Irradiance and Beam Transmittance Measurements Off the West Coast of the Americas
VOL. 84, NO. C1 JOURNAL OF GEOPHYSICAL RESEARCH JANUARY 20, 1979 Irradiance and Beam Transmittance Measurements off the West Coast of the Americas RICHARD W. SPINRAD,J. RONALD V. ZANEVELD, AND HASONG PAK Schoolof Oceanography,Oregon State University, Corvallis, Oregon 97331 Measurementsof total irradiance versusdepth and beam transmissionversus depth were made at stationsnear shore along the west coast of the North and South American continents.The water typesat each station were optically classifiedaccording to the systemof Jerlov (1976), thus providingadditional information for the descriptionof the distribution of the world's ocean water types. In addition, the parameterk/c, wherek is the irradianceattenuation coefficient and c is the beamattenuation coefficient, has been shown to be a useful parameterfor determiningthe relative particle concentrationsof ocean water. INTRODUCTION mately 75 m. At two stations(8 and 9), equipmentmalfunc- Optical classificationof oceanwater is an important means tions preventedmeasurements from being taken. of distinguishing water types. Jerlov [1951] presented a The irradiance meter usedhad a flat opal glassdiffuser as a method of classificationaccording to spectraltransmittance of cosinecollector and containeda signallog amplifierto provide downward irradiance at high solar altitude. Downward irra- an outputsignal between +4 V dc. The spectralresponse of the diance is defined as the radiant flux on an infinitesimal element irradiance meter is shown in Figure 3. The transmissivity of the upper face (0 ø-180ø) of a horizontal surfacecontaining meter consistedessentially of a light-emitting diode (wave- the point being considered,divided by the area of that element length = 650 nm), collimatinglenses, and a photodiode.The [Jerlov, 1976]. Jerlov's [1951] classificationdefined three dif- optical path length of the meter was 0.25 m.