The document discusses various notations, symbols, and nomenclature used in heat exchanger design and analysis including definitions of parameters like heat transfer coefficients, temperature differences, densities, and other thermal and fluid properties. It also provides references for standards and design methods from publications on topics like compact heat exchangers, heat exchanger design handbooks, and specifications for plate-fin heat exchangers. The notations are presented in SI and Imperial units.
This document provides an overview of Kern's method for designing shell-and-tube heat exchangers. It begins with objectives and an introduction to Kern's method. It then outlines the design procedure algorithm and provides an example application. The example involves designing an exchanger to sub-cool methanol condensate using brackish water as the coolant. The document walks through each step of the Kern's method design process for this example, including calculating properties, determining duties, selecting tube/shell parameters, and estimating heat transfer coefficients.
Heat exchangers transfer thermal energy between two or more fluids at different temperatures. They are classified based on their transfer process, geometry, heat transfer mechanism, and flow arrangement. Shell-and-tube heat exchangers consist of a set of tubes in a shell container and are the most important type, used across many industries. Their design involves calculating the heat transfer rate, selecting appropriate materials and geometry, and ensuring optimal fluid velocities and pressure drops within design limits.
Koldwave’s water-cooled portable air-conditioner solutions with heat pump offer maximum versatility with minimum effort. Our complete line offers cooling capacities from 6,300 to 34,700 BTU/HR, as well as heating capacities from 7,000 to 38,500 BTU/HR. Simple to install, these water-cooled systems are ideal for a variety of settings, including homes, apartments, laboratories, and hospitals.
Analysis comparing performance of a conventional shell and tube heat exchange...eSAT Publishing House
IJRET : International Journal of Research in Engineering and Technology is an international peer reviewed, online journal published by eSAT Publishing House for the enhancement of research in various disciplines of Engineering and Technology. The aim and scope of the journal is to provide an academic medium and an important reference for the advancement and dissemination of research results that support high-level learning, teaching and research in the fields of Engineering and Technology. We bring together Scientists, Academician, Field Engineers, Scholars and Students of related fields of Engineering and Technology
The document outlines a 14-step process for manually designing a shell and tube heat exchanger using the Kern method. Key steps include: 1) obtaining thermo-physical properties of fluids, 2) performing an energy balance to determine heat duty, 3) assuming an overall heat transfer coefficient, 4) deciding tube passes and calculating the log mean temperature difference, 5) calculating required heat transfer area, 6) selecting tube materials and dimensions, 7) deciding exchanger type and tube pitch, 8) assigning fluids and selecting baffles, 9) calculating heat transfer coefficients, 10) checking the calculated overall heat transfer coefficient, 11) recalculating as needed, 12) calculating overdesign, 13) calculating pressure drops, and 14)
This document discusses heat transmission and calculating refrigeration load. It defines key terms used in heat transfer calculations like thermal conductivity, resistance, conductance and overall heat transfer coefficient. It provides tables of conductivity values for common building materials and outdoor weather data for design temperatures. It also discusses allowances for solar heat gain, recommended insulation thicknesses, and quick methods to estimate heat transmission through insulated walls. Sections on air infiltration and product/supplementary load are summarized, but not in detail.
The document summarizes an experiment on a small shell and tube heat exchanger. Two technical objectives were tested: 1) varying the tube side flow rate while keeping the shell side constant, and 2) varying the shell side flow rate while keeping the tube side constant. Key results showed that increasing the flow rate on either side decreased temperatures and increased the heat transfer coefficient. The heat loss to the environment initially increased with flow before decreasing at the highest flow rate tested.
Finned-tube Heat Exchanger with Circular, Eliiptical and Rectangular Tubes wi...Hasibul Hasan Shovon
1) The study numerically investigates a finned-tube heat exchanger with circular, elliptical and rectangular tubes using water vapor as the working fluid.
2) Results show that heat exchanger designs with elliptical and rectangular tubes have higher heat transfer coefficients compared to the baseline circular tube design, with some designs also having lower pressure drops.
3) Temperature and pressure contours indicate better heat transfer and lower resistance for some modified designs compared to the baseline, especially at higher inlet velocities.
This document provides an overview of Kern's method for designing shell-and-tube heat exchangers. It begins with objectives and an introduction to Kern's method. It then outlines the design procedure algorithm and provides an example application. The example involves designing an exchanger to sub-cool methanol condensate using brackish water as the coolant. The document walks through each step of the Kern's method design process for this example, including calculating properties, determining duties, selecting tube/shell parameters, and estimating heat transfer coefficients.
Heat exchangers transfer thermal energy between two or more fluids at different temperatures. They are classified based on their transfer process, geometry, heat transfer mechanism, and flow arrangement. Shell-and-tube heat exchangers consist of a set of tubes in a shell container and are the most important type, used across many industries. Their design involves calculating the heat transfer rate, selecting appropriate materials and geometry, and ensuring optimal fluid velocities and pressure drops within design limits.
Koldwave’s water-cooled portable air-conditioner solutions with heat pump offer maximum versatility with minimum effort. Our complete line offers cooling capacities from 6,300 to 34,700 BTU/HR, as well as heating capacities from 7,000 to 38,500 BTU/HR. Simple to install, these water-cooled systems are ideal for a variety of settings, including homes, apartments, laboratories, and hospitals.
Analysis comparing performance of a conventional shell and tube heat exchange...eSAT Publishing House
IJRET : International Journal of Research in Engineering and Technology is an international peer reviewed, online journal published by eSAT Publishing House for the enhancement of research in various disciplines of Engineering and Technology. The aim and scope of the journal is to provide an academic medium and an important reference for the advancement and dissemination of research results that support high-level learning, teaching and research in the fields of Engineering and Technology. We bring together Scientists, Academician, Field Engineers, Scholars and Students of related fields of Engineering and Technology
The document outlines a 14-step process for manually designing a shell and tube heat exchanger using the Kern method. Key steps include: 1) obtaining thermo-physical properties of fluids, 2) performing an energy balance to determine heat duty, 3) assuming an overall heat transfer coefficient, 4) deciding tube passes and calculating the log mean temperature difference, 5) calculating required heat transfer area, 6) selecting tube materials and dimensions, 7) deciding exchanger type and tube pitch, 8) assigning fluids and selecting baffles, 9) calculating heat transfer coefficients, 10) checking the calculated overall heat transfer coefficient, 11) recalculating as needed, 12) calculating overdesign, 13) calculating pressure drops, and 14)
This document discusses heat transmission and calculating refrigeration load. It defines key terms used in heat transfer calculations like thermal conductivity, resistance, conductance and overall heat transfer coefficient. It provides tables of conductivity values for common building materials and outdoor weather data for design temperatures. It also discusses allowances for solar heat gain, recommended insulation thicknesses, and quick methods to estimate heat transmission through insulated walls. Sections on air infiltration and product/supplementary load are summarized, but not in detail.
The document summarizes an experiment on a small shell and tube heat exchanger. Two technical objectives were tested: 1) varying the tube side flow rate while keeping the shell side constant, and 2) varying the shell side flow rate while keeping the tube side constant. Key results showed that increasing the flow rate on either side decreased temperatures and increased the heat transfer coefficient. The heat loss to the environment initially increased with flow before decreasing at the highest flow rate tested.
Finned-tube Heat Exchanger with Circular, Eliiptical and Rectangular Tubes wi...Hasibul Hasan Shovon
1) The study numerically investigates a finned-tube heat exchanger with circular, elliptical and rectangular tubes using water vapor as the working fluid.
2) Results show that heat exchanger designs with elliptical and rectangular tubes have higher heat transfer coefficients compared to the baseline circular tube design, with some designs also having lower pressure drops.
3) Temperature and pressure contours indicate better heat transfer and lower resistance for some modified designs compared to the baseline, especially at higher inlet velocities.
The document summarizes the design and analysis of an air-cooled heat exchanger for a 3-phase induction motor. It outlines specifications for the heat exchanger including air flow rates, temperatures, and heat exchange capacity. It then describes an 8-step process for the design including selecting materials, configuring piping, calculating heat transfer coefficients, and evaluating effectiveness. The scope of the project is defined as developing a prototype while considering losses, fan calculations, cost analysis, and testing iterations through graphical plotting.
This document discusses heat transfer fins or extended surfaces. It begins by introducing fins and their importance in industry for controlling heat transfer. It then covers fin types, materials, applications, effectiveness vs efficiency, and formulas for calculating heat transfer via fins. Key points include that fins increase heat transfer area and are often made of aluminum or copper. Common applications include heat exchangers, condensers, and electronic devices. Formulas are provided for calculating heat transfer and temperature distribution for different fin boundary conditions.
This document provides specifications for an electric heat exchanger including its type, model, power rating, voltage, temperature range, pressure ratings, dimensions, and manufacturer information. Key details are its classification as a SM2-4KW electric heat exchanger with 380V power, a design pressure of 250 bar, an operating temperature range of -40/+120 to -10/+100 Celsius, and manufactured by Pegoraro Gas Technologies in Vicenza, Italy.
This document provides information about shell and tube heat exchangers, including basic calculations. It defines key concepts such as specific heat, temperature scales, pressure units and energy conversions. It also outlines the overall design process for a shell and tube heat exchanger, describing how to calculate the required heat transfer rate and surface area based on parameters like the overall heat transfer coefficient and log mean temperature difference.
An innovative technology to increase the heater capacity without increasing the coil side pressure drop in fired heaters.
Furnace Improvements has implemented this technology in many fired heaters around the world. This technology is useful specially for Reformer heaters as coil pressure drop is limited for those heaters, typically 2-5 psi.
Analysis of Thermal Profiles of Various Power Extraction Limits in a PWR Hea...IRJET Journal
This document analyzes the thermal profiles of various power extraction limits in a pressurized water reactor (PWR) heated channel. It examines three cases: 1) keeping the coolant exit temperature sub-cooled, 2) keeping the maximum cladding temperature below saturation, and 3) keeping the fuel maximum temperature below the melting point. The second case had the lowest power extraction due to the low cladding surface temperature limiting outlet temperature. While the first and third cases extracted almost the same power, the document concludes the first case should be used as the standard, as it keeps outlet temperature away from saturation while also avoiding high temperature differences that can damage fuel. Numerical computations of the thermal profiles are performed for each case.
Un virus informático es un programa que se autopropaga insertando copias de sí mismo en otros programas y archivos, infectando ordenadores a medida que viaja de uno a otro. Las bombas lógicas son códigos que se activan en un momento predeterminado, como una fecha específica, para activarse en varios equipos a la vez. Los gusanos se replican automáticamente de un equipo a otro para propagarse rápidamente.
Integrated Marketing Communication (IMC) needs to be updated to account for changes in the digital era. The consumer journey is now more complex, with many new touchpoints influencing consumers. Consistency across touchpoints is still important, but campaigns need to leverage each touchpoint's unique strengths rather than using the same execution everywhere. Successful campaigns now synchronize different creative executions across touchpoints, with media and creative planned together. They also allow two-way engagement with consumers to co-create the brand narrative. The new approach of "orchestrated marketing" coordinates all elements like an orchestra for maximum impact.
Este documento discute la pregunta "¿Qué es la Psicología?". Presenta dos perspectivas: 1) La Psicología como una ciencia natural que estudia el alma como una forma natural dentro del cuerpo, remontándose a ideas aristotélicas. 2) Duda que definir la Psicología como una "teoría general de la conducta" capture adecuadamente la diversidad de enfoques, como la Psicología clínica se centra más en el ser humano que en el método. Plantea que la unidad de la Psicología podría estar mejor
Safety guidelines by ec 17 references r 1Mumbai Hiker
This document lists 24 references related to safety guidelines for various outdoor activities. The references include definitions, standards, ethics declarations, and guidelines from organizations such as the UIAA and IMF related to climbing, mountaineering, expeditions, trekking, and risk management for outdoor adventure programs.
This certificate of membership certifies that Ms. M. Blakley is member number 10439 of The British Medical Ultrasound Society for the period of January 1, 2015 to December 31, 2015. The certificate is signed by Prof. Paul Sidhu as the president of the society and provides the registered office address and registration numbers for the nonprofit organization.
Cinco personas son mencionadas en el documento: Álvaro Fernando Sosa González, Astrid Biviana Giraldo Ochoa, María Isabel Osorio Lopéz, Sara María Arroyave Cardona y Yenny Alexandra Castaño Blandón.
Hybrid Approach for generating Binary Secured Face templates with BDASelf
This document proposes a hybrid approach for generating binary secured face templates that combines biometric cryptosystems and cancellable biometrics. It uses binary discriminant analysis (BDA) to transform a real-valued face template into a binary template. BDA finds optimal linear discriminant functions using perceptron learning to minimize within-class variance and BCH codes to maximize between-class variance. In the proposed method, feature extraction is done using DCT and passwords are secured using SHA-256 hashing during enrollment and authentication. Experimental analysis shows the method achieves strong security, performance and revocability for moderate-level applications.
משוב הוא מידע המגיע ממקור חיצוני באופן מוזמן או אקראי, ותכליתו לאפשר למקבל המשוב לכוון את עצמו ואת מעשיו ביתר דיוק ומיקוד להשגת מטרותיו. משוב איכותי מאפשר הפקת תועלת במיידי, בטווח הקצר.
Dokumen tersebut berisi soal-soal integral dan luas daerah yang dibatasi kurva. Terdapat 4 bagian (A, B, C, D) yang masing-masing berisi 7 soal integral, luas daerah, dan volume putaran.
El documento habla sobre el aprendizaje de la percepción y cómo afecta la forma en que procesamos la información sensorial. Menciona experimentos donde personas usaron lentes que invirtieron su visión, causando inicialmente mareos pero luego se adaptaron a ver el mundo de cabeza. También cubre ilusiones ópticas y cómo factores como el contexto y hábitos perceptuales influyen en cómo percibimos los estímulos.
Pembahasan soal kalkulus pada buku karangan edwin j. purcell dan dale varberg...Faris Audah
Dokumen tersebut berisi penjelasan tentang latihan soal sederhana kalkulus yang meliputi operasi aljabar seperti penjumlahan, pengurangan, perkalian, dan pembagian bilangan pecahan serta penyederhanaan ekspresi aljabar. Terdapat 32 soal latihan yang berisi operasi-operasi tersebut beserta penjelasan singkat konsep-konsep dasar kalkulus.
The document summarizes the design and analysis of an air-cooled heat exchanger for a 3-phase induction motor. It outlines specifications for the heat exchanger including air flow rates, temperatures, and heat exchange capacity. It then describes an 8-step process for the design including selecting materials, configuring piping, calculating heat transfer coefficients, and evaluating effectiveness. The scope of the project is defined as developing a prototype while considering losses, fan calculations, cost analysis, and testing iterations through graphical plotting.
This document discusses heat transfer fins or extended surfaces. It begins by introducing fins and their importance in industry for controlling heat transfer. It then covers fin types, materials, applications, effectiveness vs efficiency, and formulas for calculating heat transfer via fins. Key points include that fins increase heat transfer area and are often made of aluminum or copper. Common applications include heat exchangers, condensers, and electronic devices. Formulas are provided for calculating heat transfer and temperature distribution for different fin boundary conditions.
This document provides specifications for an electric heat exchanger including its type, model, power rating, voltage, temperature range, pressure ratings, dimensions, and manufacturer information. Key details are its classification as a SM2-4KW electric heat exchanger with 380V power, a design pressure of 250 bar, an operating temperature range of -40/+120 to -10/+100 Celsius, and manufactured by Pegoraro Gas Technologies in Vicenza, Italy.
This document provides information about shell and tube heat exchangers, including basic calculations. It defines key concepts such as specific heat, temperature scales, pressure units and energy conversions. It also outlines the overall design process for a shell and tube heat exchanger, describing how to calculate the required heat transfer rate and surface area based on parameters like the overall heat transfer coefficient and log mean temperature difference.
An innovative technology to increase the heater capacity without increasing the coil side pressure drop in fired heaters.
Furnace Improvements has implemented this technology in many fired heaters around the world. This technology is useful specially for Reformer heaters as coil pressure drop is limited for those heaters, typically 2-5 psi.
Analysis of Thermal Profiles of Various Power Extraction Limits in a PWR Hea...IRJET Journal
This document analyzes the thermal profiles of various power extraction limits in a pressurized water reactor (PWR) heated channel. It examines three cases: 1) keeping the coolant exit temperature sub-cooled, 2) keeping the maximum cladding temperature below saturation, and 3) keeping the fuel maximum temperature below the melting point. The second case had the lowest power extraction due to the low cladding surface temperature limiting outlet temperature. While the first and third cases extracted almost the same power, the document concludes the first case should be used as the standard, as it keeps outlet temperature away from saturation while also avoiding high temperature differences that can damage fuel. Numerical computations of the thermal profiles are performed for each case.
Un virus informático es un programa que se autopropaga insertando copias de sí mismo en otros programas y archivos, infectando ordenadores a medida que viaja de uno a otro. Las bombas lógicas son códigos que se activan en un momento predeterminado, como una fecha específica, para activarse en varios equipos a la vez. Los gusanos se replican automáticamente de un equipo a otro para propagarse rápidamente.
Integrated Marketing Communication (IMC) needs to be updated to account for changes in the digital era. The consumer journey is now more complex, with many new touchpoints influencing consumers. Consistency across touchpoints is still important, but campaigns need to leverage each touchpoint's unique strengths rather than using the same execution everywhere. Successful campaigns now synchronize different creative executions across touchpoints, with media and creative planned together. They also allow two-way engagement with consumers to co-create the brand narrative. The new approach of "orchestrated marketing" coordinates all elements like an orchestra for maximum impact.
Este documento discute la pregunta "¿Qué es la Psicología?". Presenta dos perspectivas: 1) La Psicología como una ciencia natural que estudia el alma como una forma natural dentro del cuerpo, remontándose a ideas aristotélicas. 2) Duda que definir la Psicología como una "teoría general de la conducta" capture adecuadamente la diversidad de enfoques, como la Psicología clínica se centra más en el ser humano que en el método. Plantea que la unidad de la Psicología podría estar mejor
Safety guidelines by ec 17 references r 1Mumbai Hiker
This document lists 24 references related to safety guidelines for various outdoor activities. The references include definitions, standards, ethics declarations, and guidelines from organizations such as the UIAA and IMF related to climbing, mountaineering, expeditions, trekking, and risk management for outdoor adventure programs.
This certificate of membership certifies that Ms. M. Blakley is member number 10439 of The British Medical Ultrasound Society for the period of January 1, 2015 to December 31, 2015. The certificate is signed by Prof. Paul Sidhu as the president of the society and provides the registered office address and registration numbers for the nonprofit organization.
Cinco personas son mencionadas en el documento: Álvaro Fernando Sosa González, Astrid Biviana Giraldo Ochoa, María Isabel Osorio Lopéz, Sara María Arroyave Cardona y Yenny Alexandra Castaño Blandón.
Hybrid Approach for generating Binary Secured Face templates with BDASelf
This document proposes a hybrid approach for generating binary secured face templates that combines biometric cryptosystems and cancellable biometrics. It uses binary discriminant analysis (BDA) to transform a real-valued face template into a binary template. BDA finds optimal linear discriminant functions using perceptron learning to minimize within-class variance and BCH codes to maximize between-class variance. In the proposed method, feature extraction is done using DCT and passwords are secured using SHA-256 hashing during enrollment and authentication. Experimental analysis shows the method achieves strong security, performance and revocability for moderate-level applications.
משוב הוא מידע המגיע ממקור חיצוני באופן מוזמן או אקראי, ותכליתו לאפשר למקבל המשוב לכוון את עצמו ואת מעשיו ביתר דיוק ומיקוד להשגת מטרותיו. משוב איכותי מאפשר הפקת תועלת במיידי, בטווח הקצר.
Dokumen tersebut berisi soal-soal integral dan luas daerah yang dibatasi kurva. Terdapat 4 bagian (A, B, C, D) yang masing-masing berisi 7 soal integral, luas daerah, dan volume putaran.
El documento habla sobre el aprendizaje de la percepción y cómo afecta la forma en que procesamos la información sensorial. Menciona experimentos donde personas usaron lentes que invirtieron su visión, causando inicialmente mareos pero luego se adaptaron a ver el mundo de cabeza. También cubre ilusiones ópticas y cómo factores como el contexto y hábitos perceptuales influyen en cómo percibimos los estímulos.
Pembahasan soal kalkulus pada buku karangan edwin j. purcell dan dale varberg...Faris Audah
Dokumen tersebut berisi penjelasan tentang latihan soal sederhana kalkulus yang meliputi operasi aljabar seperti penjumlahan, pengurangan, perkalian, dan pembagian bilangan pecahan serta penyederhanaan ekspresi aljabar. Terdapat 32 soal latihan yang berisi operasi-operasi tersebut beserta penjelasan singkat konsep-konsep dasar kalkulus.
O documento contém 22 problemas de adição com números de 2 a 3 dígitos. Cada problema apresenta a operação matemática com os números a serem somados e o resultado. Os problemas são agrupados em blocos de 10 questões e marcados com o nome "SCHOOLHOUSE TECHNOLOGIES EVALUATION".
The document provides details on the design and construction of shell and tube heat exchangers. It describes the key components of a shell and tube heat exchanger including the shell, tubes, tube sheets, bonnet, channel, pass partition plates, nozzles, baffles, tie rods, and flanges. It also explains the functions of each component and provides examples of different types of components like baffles, joints between tubes and tube sheets, and impingement plates.
This document discusses the thermal and hydraulic design of brazed aluminum plate-fin heat exchangers. It covers topics such as single and multiple banking configurations, multi-stream designs, thermal design procedures and relationships, hydraulic design considerations, and the selection of fin geometry. Key points include defining the components of heat transfer surface area and pressure drop, methods for calculating overall heat transfer coefficients and temperature differences, and considerations for single-phase versus two-phase stream calculations.
A Review on Heat Transfer Improvent of Plate Heat ExchangerIJERA Editor
Plate heat exchanger has found a wide range of application in various industries like food industries, chemical industries, power plants etc. It reduces the wastage of energy and improves the overall efficiency of the system. Hence, it must be designed to obtain the maximum heat transfer possible. This paper is presented in order to study the various theories and results given over the improvement of heat transfer performance in a plate heat exchanger. However, there is still a lack in data and generalized equations for the calculation of different parameters in the heat exchanger. It requires more attention to find out various possible correlations and generalized solutions for the performance improvement of plate heat exchanger.
This document summarizes a study on assessing the thermal performance of semicircular fins under forced air convection and its application to air preheaters. The study finds that semicircular fins have greater thermal efficiency compared to circular fins of the same volume due to their larger surface area. Mathematical models are developed to analyze heat transfer in the fins and an air preheater. Various parameters like number of fins, pipe size, air velocity and temperature are examined. The results show that larger preheat can be achieved using semicircular fins, providing potential for higher energy efficiency.
This document summarizes a study on assessing the thermal performance of semicircular fins under forced air convection and its application to air preheaters. The study finds that semicircular fins have greater thermal efficiency compared to circular fins of the same volume due to their larger surface area. Mathematical models are developed to analyze heat transfer in the fins and an air preheater. Various parameters like number of fins, pipe size, air velocity and temperature are examined. The results show that larger preheat can be achieved using semicircular fins, providing potential for higher energy efficiency.
1) The document discusses improvements in fired heater design and specifications over the last 30 years due to changes in fuel properties and new materials.
2) Vertical cylindrical heaters have become popular due to their compact design and lower cost compared to horizontal box heaters, but box heaters can accommodate more burners and have better two-phase flow.
3) Lower radiant heat flux leads to lower tube metal temperatures and higher run lengths before cleaning is needed, but requires more radiant tube area. Optimization of design parameters like flux, tube size and passes is important.
FEEMSSD presentation on shell and tube heat exchanger75 .pptxAdarshPandey510683
The document describes the design of a shell and tube heat exchanger. It discusses the components of a shell and tube heat exchanger including the shell, tubes, tube bundle, tubesheet, expansion joint, flanges, gaskets, nozzles, and baffles. It also outlines the objectives of designing a shell and tube heat exchanger for an industry application. The thermal design process involves selecting fluids for the tube and shell sides based on properties, calculating the heat transfer area, tube dimensions, and other parameters. The results of the design case study showed that using recommended design ranges from literature led to an optimal design that met design specifications.
The International Journal of Engineering & Science is aimed at providing a platform for researchers, engineers, scientists, or educators to publish their original research results, to exchange new ideas, to disseminate information in innovative designs, engineering experiences and technological skills. It is also the Journal's objective to promote engineering and technology education. All papers submitted to the Journal will be blind peer-reviewed. Only original articles will be published.
The papers for publication in The International Journal of Engineering& Science are selected through rigorous peer reviews to ensure originality, timeliness, relevance, and readability.
This document discusses the advantages of considering compact heat exchangers like plate-and-frame exchangers early in the process design stage. Plate-and-frame exchangers can be significantly smaller than traditional shell-and-tube exchangers while meeting the same heat transfer needs. Specifying design requirements without considering the characteristics of different exchanger types can lead to oversized and more expensive designs. Charts are provided to help estimate the required area of plate-and-frame exchangers for preliminary sizing.
This document discusses the advantages of considering compact heat exchangers like plate-and-frame exchangers early in the process design stage. Plate-and-frame exchangers can be significantly smaller than traditional shell-and-tube exchangers while meeting the same heat transfer needs. Specifying design requirements without considering the characteristics of different exchanger types can lead to oversized and more expensive designs. Charts are provided to help estimate the required area of plate-and-frame exchangers for preliminary sizing.
This document discusses the advantages of considering compact heat exchangers like plate-and-frame exchangers early in the process design stage. Plate-and-frame exchangers can be significantly smaller than traditional shell-and-tube exchangers while meeting the same heat transfer needs. Specifying design requirements without considering the unique capabilities of different exchanger types can lead to oversized and more expensive designs. Charts are provided to help estimate the required area of plate-and-frame exchangers for preliminary sizing.
EXPERIMENTAL STUDY OF MIXED CONVECTION HEAT TRANSFER USING CIRCULAR, SQUARE, ...ijiert bestjournal
Pulling Fins are extended surfaces employed to enha nce the convective heat transfer from a surface for increasing heat dissipation. Fins with various geometries have been designed and used in various cooling application the selection o f particular fins configuration in any heat transfer application is an important state in desig ned process and takes into account the space,weight,manufacturing technique and cost considerat ion as well as the thermal characteristics it exhibits. Fins cross section profiles have profo und influence on thermal characteristics of Annular Fins and the surface area changes with chan ge of cross section of fins. This study deals with studying the performance of various avai lable fins profiles. Widely used fins profile viz. Rectangular,Triangular,Trapezoidal,Circular,Rhombic,and Elliptical Fins. In Addition to the normal configuration of fins,to ne w configurations were designed and created.
An experimental study of heat transfer in a corrugated plate heat exchangerIAEME Publication
1. The document discusses an experimental study of heat transfer in a corrugated plate heat exchanger. Experiments were conducted to analyze heat transfer characteristics for different flow arrangements of hot and cold fluids through the heat exchanger.
2. The effectiveness and exergy loss of the heat exchanger were calculated for parallel and counter flow arrangements. The average effectiveness was found to be 48% higher and exergy loss 33% lower in the counter flow arrangement compared to the parallel flow arrangement.
3. Maximum heat transfer was observed at the highest hot fluid inlet temperature of 70°C, being 5% greater in the parallel flow arrangement. However, the non-dimensional exergy loss and log mean temperature difference were both lower in the
IRJET - Review of Entropy Generation Minimization in Heat ExchangerIRJET Journal
This document reviews entropy generation minimization in helically coiled heat exchangers. It derives a dimensionless function for the entropy generation number involving four dimensionless variables. It then minimizes the entropy generation number to derive analytical expressions for the optimal values of these variables for both laminar and turbulent flows. For laminar flow, it finds an optimal inner tube diameter ratio of 10 and shows the entropy generation is minimal for annulus diameter ratios from 3.5-5. For turbulent flow, it finds optimal inner tube and annulus diameter ratios of 16.5 and around 2, respectively.
Optimization of a Shell and Tube Condenser using Numerical MethodIJERA Editor
The purpose of this study was to investigate the effect of installation of the tube external surfaces, their parameter and variable in a shell-and-tube condenser. Variation of heat transfer coefficient with each variable of shell and tube condenser was measured each test. The optimization tube outside diameter size was analyzed and use extended surface area attached tube with tube material and tube layout and arrangement (Number of tube a triangular or hexagonal arrangement) on shell-and tube condenser. The computer programming was used to get faster output in less time. Results suggest that mean heat transfer coefficient in variable condition were mainly at velocity is fixed. And also average additional surfaces and tube layout and the arrangement comparison with the quantity of the heat transfer.
Heat transfer analysis is needed to optimally design heat exchangers and determine equipment sizes. It is essential for sizing nuclear reactor cores, aircraft performance, refrigeration applications, and solar equipment. Thermodynamic analysis determines the heat required for a state change, while heat transfer analysis evaluates the rate of heat transfer. The three methods of heat transfer are conduction through solids, convection through fluid movement, and radiation through electromagnetic waves. Extended surfaces like fins increase heat transfer area and rates.
This document describes a heat exchanger design project. It provides theory on heat exchanger design including heat transfer rate calculations. It then details the CFD simulation process used to model and analyze different heat exchanger designs. This included an initial 2D model, mesh refinement studies to determine optimal mesh size, and modeling variations in pipe spacing, flow direction, and a 3D design. Results were analyzed using temperature, turbulence, and velocity contours to evaluate design performance.
Experimental and computational investigation of low cost standing wave thermo...IAEME Publication
This document presents experimental and computational investigation of a low-cost standing wave thermoacoustic refrigerator. Experimentally, a maximum temperature difference of 11K was obtained using a glass fiber stack with glass capillary tube spacers located at 0.15m from the speaker inlet. Computational fluid dynamics analysis using similar conditions obtained a temperature difference of 6K, in good agreement with experimental results. The study aims to develop an inexpensive standing wave thermoacoustic refrigerator design using readily available materials.
Experimental and computational investigation of low cost standing wave thermo...IAEME Publication
This document presents experimental and computational investigation of a low-cost standing wave thermoacoustic refrigerator. Experimentally, a maximum temperature difference of 11K was obtained using a glass fiber stack with glass capillary tube spacers located at 0.15m from the speaker inlet. Computational fluid dynamics analysis using similar conditions obtained a temperature difference of 6K, in good agreement with experimental results. The study aims to develop an inexpensive standing wave thermoacoustic refrigerator design using readily available materials.
Experimental and computational investigation of low cost standing wave thermo...
Alpema standards9
1. B Defined by Equation (13), Chapter 7 - -
C Coefficient, defined by Equation (14), Chapter 7 W/m3
K Btu/ft2
F
Cp Specific heat J/kg K Btu/lb F
dh Hydraulic diameter of passage m ft
f Fanning friction factor - -
F Force N lb
Gm Mass flux/velocity of a stream kg/m2
s lb/ft2
hr
h Fin height mm in
H Stacking height of a core mm in
j Colburn factor for a finned passage - -
K Expansion/contraction/turning loss coefficient - -
lp Passage length mm in
L Core length mm in
LMTD Logarithmic mean temperature difference K F
M Moment Nm lb ft
MTD Mean temperature difference K F
p Fin pitch mm in
Pr Prandtl number - -
Q Overall heat duty; heat to be transferred W Btu
r Fouling resistance m2
K/W ft2
F hr/Btu
s Distance between the extreme bolts in a given plane mm in
t Fin thickness mm in
U Overall heat transfer coefficient between streams W/m2
K Btuhr ft2
F
W Width of core mm in
X Required clearance distance mm in
Greek
l Coefficient of linear expansion at average temperature m/m K ft/ft F
o Effective heat transfer coefficient of a stream W/m2
K Btuhr ft2
F
Heat transfer coefficient of a stream W/m2
K Btuhr ft2
F
Defined by Equation (11), Chapter 7 - -
Defined by Equation (12), Chapter 7 - -
P Overall pressure drop N/m2
(Pa) lb/in2
TR Temperature range at support K F
1 Passage fin efficiency for single banking - -
2 Passage fin efficiency for double banking - -
m Thermal conductivity of fin material W/m K Btuhr ft F
Density of stream kg/m3
lb/ft3
Unperforated fraction of fin - -
Notation
Notation
SI IMPERIAL
A Effective heat transfer surface of a passage or layer m2
ft2
Ad Designed or estimated overall effective heat transfer surface m2
ft2
Ar Required overall effective heat transfer surface m2
ft2
A1 Primary heat transfer surface of a stream m2
ft2
A2 Secondary heat transfer surface of a stream m2
ft2
ls Serration length or distance between crests on herringbone fins mm in
n Fin density m-1
in-1
V Volume of heat exchanger or exchangers m3
ft3
T Local temperature difference between warm and cold streams K F
Subscripts
c Cold stream w Warm stream
i Section x,y,z Direction
STANDARDS OF THE BRAZED ALUMINIUM PLATE-FIN HEAT EXCHANGER MANUFACTURER'S ASSOCIATION 63
2.
3. References
References
(1) Ward, J.A., "Effectiveness-NTU Relationships", Data Item 86018, Engineering Sciences Data
Unit, London, 1986.
(2) Kays, W.M. and London, A.L., "Compact Heat Exchangers", McGraw Hill, New York, Third
Edition, 1984.
(3) Taborek, J. and Spalding, D.B., "Heat Exchanger Design Handbook", Hemisphere Publishing
Corporation, 1983.
(4) Taylor, M.A., "Plate-Fin Heat Exchangers - Guide to Their Specification and Use", HTFS, 392.7
Harwell, Oxon, OX11 0RA, UK. 1987.
STANDARDS OF THE BRAZED ALUMINIUM PLATE-FIN HEAT EXCHANGER MANUFACTURER'S ASSOCIATION 65
4.
5. Index
Index
Acceptable Fluids ...........................................2
AD-Merkblätter .............................................35
Aftercooler ......................................................2
Air Separation Unit(ASU)................................2
Air test ..........................................................36
Ammonia .................................................... 2, 3
Angle Bracket Support Arrangement ............ 26
Argon...............................................................3
AS 1210........................................................35
ASME VIll, Div. 1 ..........................................35
Asphyxiation .................................................32
Atmospheric Corrosion .................................62
Banking
Multiple .....................................................46
Single........................................................46
Beams
Support .....................................................23
Block (core) ....................................................4
Blocking of Layers ........................................22
Burst test method..........................................41
Butane .............................................................3
Cap sheet .......................................................4
Cap Sheets...................................................41
Carbon Dioxide........................................... 2, 3
Carbon Monoxide ....................................... 2, 3
Cascade Cooling...............................................3
Chillers ...........................................................2
Chlorine..........................................................2
Choice of Fin Geometry................................54
Cleaning ................................................. 20, 59
Solvent......................................................59
CODAP.........................................................35
Code Data Reports.......................................19
Codes for Construction .................................35
Coefficient of Thermal Expansion ................. 28
Colburn Factor..............................................50
Cold Boxes ...................................................32
Components
of an Exchanger..........................................4
of Manifolded Exchangers...........................5
Condenser
Overhead ....................................................2
Condensers ....................................................2
Connection Options
Flanges.......................................................6
Stub Ends ...................................................6
Transition Joints..........................................6
CONTRACTUAL INFORMATION................. 17
Cool-down ....................................................31
Core (block)....................................................4
Core Volume
Estimation .................................................52
Corrosion ......................................................60
Acidic Environments..................................61
Alkaline Environments...............................61
Atmospheric or Environmental...................62
Environments containing Mercury..............61
Water ........................................................60
Corrosion Allowances ...................................38
Damage........................................................33
Definition.......................................................35
Dephlegmators ...............................................2
Deplugging....................................................60
Description
General .......................................................1
DESIGN
HYDRAULIC .......................................45–55
THERMAL ...........................................45–55
Design Code.................................................17
Design Pressures..........................................35
Design Temperature .....................................37
Distributor
Central ......................................................10
Diagonal....................................................10
Double Entry/Exit.......................................10
End..............................................................9
Intermediate ................................................9
Mitre..........................................................10
Side.............................................................9
Special ........................................................9
Split Flow...................................................10
Distributor fins.................................................4
Drawings.......................................................18
Approval and Change................................18
for Record .................................................18
Information ................................................18
Proprietary Rights......................................19
Drying ...........................................................20
Dummy Passages.........................................20
Dutch Pressure Vessel Code ........................35
Ethane .............................................................3
Ethylene...........................................................3
Exchanger
block (core) .................................................1
cap sheets...................................................1
inlet ports.....................................................1
layers (passages) ........................................1
multi-stream ................................................1
outlet ports ..................................................1
parting sheets..............................................1
side bars......................................................1
size..............................................................1
FABRICATION........................................17–22
Failure Mechanism........................................57
STANDARDS OF THE BRAZED ALUMINIUM PLATE-FIN HEAT EXCHANGER MANUFACTURER'S ASSOCIATION 67
6. Index
Field Testing................................................. 29
Filters ........................................................... 31
Fin Corrugations............................................. 8
Fin Dimensions............................................... 9
Definition..................................................... 9
Fins Per Inch (FPI)...................................... 9
Percentage Perforation ............................... 9
Fin Geometry
Choice of................................................... 54
Fin Types........................................................ 8
Fins .............................................................. 41
Herringbone................................................ 8
Perforated................................................... 8
Plain............................................................ 8
Serrated...................................................... 8
Wavy........................................................... 8
Fixing Bolts................................................... 27
Flange Protection ......................................... 20
Flanges ........................................................ 40
Flow Arrangements ...................................... 11
Co-Current Flow........................................ 11
Counterflow............................................... 11
Cross-Counterflow .................................... 11
Crossflow.................................................. 11
Flow Fluctuations.......................................... 57
Flow Velocities in Nozzles ............................ 39
Fluids
Acceptable.................................................. 2
Fouling ......................................................... 58
Fouling Resistance....................................... 51
Freeze Spots................................................ 32
Freon............................................................... 3
General Description........................................ 1
GENERAL DESCRIPTION....................... 1–11
GOOD PRACTICE ................................. 57–62
Guarantees................................................... 19
Consequential Damage............................. 19
Corrosion .................................................. 19
Thermal and Mechanical........................... 19
Guide Frame
Sliding....................................................... 24
Handling ....................................................... 23
Header
Dome.......................................................... 7
Inclined Ends .............................................. 7
Mitred Ends................................................. 7
Standard ..................................................... 7
Header/Nozzle Configurations........................ 6
Headers.......................................... 4, 6, 38, 41
Heat Transfer Coefficient of a Stream........... 50
Heat transfer fins ............................................ 4
Heat Transfer Surface .................................. 47
Height............................................................. 4
Stacking...................................................... 1
Helium ............................................................. 3
Helium Leak Test.......................................... 34
Helium Recovery...............................................3
Helium test....................................................36
Hexane ............................................................3
HYDRAULIC DESIGN ............................45–55
Hydrogen .........................................................3
Hydrogen Sulphide .........................................2
Inactive Areas...............................................20
Injury.............................................................33
Inspection .....................................................17
Manufacturer’s ..........................................17
Purchaser’s ...............................................17
Third Party ................................................17
INSTALLATION ......................................23–34
Insulation ......................................................30
Japanese HPGS Law....................................35
Layer Arrangements .....................................40
Leak Detection..............................................32
Leak Rate .....................................................37
Leak Test......................................................36
Air .............................................................36
Helium.......................................................36
Length ............................................................4
Lifting............................................................23
Lifting Devices ..............................................21
Lifting lugs ....................................................21
Limits of Use
Maximum working pressure.........................2
Maximum working temperature ...................2
Minimum design temperature......................2
Liquefaction ......................................................3
Liquefied Natural Gas ........................................3
Liquefied Natural Gas (LNG)...............................3
Liquefied Petroleum Gas (LPG)...........................3
Liquefiers........................................................2
Liquified Natural Gas (LNG)............................2
Logarithmic Mean Temperature Difference...50
Main Exchanger..............................................2
Maintenance .................................................32
MAINTENANCE......................................23–34
MATERIALS ...........................................43–44
Materials of Construction ........................35, 43
Mean Temperature Difference ......................47
MECHANICAL STANDARDS ................. 35–42
Mercury.....................................................3, 61
Metal Temperature Limitations......................37
Methane...........................................................3
Module Construction.......................................6
Mounting Bolts..............................................27
MTBE ..............................................................3
Multi-Component Refrigerants...........................3
Multiple Banking ...........................................46
Multi-Stream .................................................46
Nameplate ....................................................17
Data ..........................................................18
Manufacturer’s ..........................................17
Purchaser’s ...............................................18
68 STANDARDS OF THE BRAZED ALUMINIUM PLATE-FIN HEAT EXCHANGER MANUFACTURER'S ASSOCIATION
7. Structure ...................................................17
Supplementary Information .......................18
Natural Gas Processing (NGP)...................2, 3
Nitrogen ...........................................................3
Nitrogen Dioxide .............................................2
Nitrogen Rejection Unit (NRU) ............................3
NOMENCLATURE.................................... 1–11
Nomenclature of the Components ..................4
Nonconformity Rectification ..........................21
Non-Destructive Testing ...............................29
Nozzle
Inclined .......................................................7
Radial..........................................................7
Tangential ...................................................7
Nozzle loadings ............................................39
Nozzle Type....................................................6
Nozzles........................................... 4, 6, 39, 41
Flow Velocities in ......................................39
Loadings ...................................................39
Operation......................................................31
OPERATION .......................................... 23–34
Overall Heat Transfer ...................................47
Overhead Condenser .....................................2
Oxygen ............................................................3
Particulate Matter..........................................31
Parting sheet ..................................................4
Parting Sheets..............................................41
Pentane ...........................................................3
Petrochemical Production...................................3
Piping .............................................................6
Plant Upsets .................................................57
Plugging ................................................. 58, 59
from dust ..................................................... 3
from molecular sieve dust ...........................3
from particulates..........................................3
Pressure Loss...............................................52
Single-Phase.............................................53
Two-Phase................................................54
Pressure Relief Device .................................31
Pressure Relieving Devices..........................31
Pressure Test ......................................... 33, 36
Hydrostatic................................................36
Pneumatic.................................................36
Pressure Testing ..........................................29
Pressure Vessel ...........................................41
Pressurising..................................................20
Primary Heat Transfer Surface ..................... 45
Production Process.......................................40
Proof Pressure Testing .................................29
Propane ...........................................................3
Propylene.........................................................3
Pulsing..........................................................31
Raccolta .......................................................35
Rare Gases ......................................................3
Reboilers ........................................................2
Rectification
Index
Leak ..........................................................22
Nonconformity ...........................................21
Rectification of Leaks....................................22
Refrigeration Systems........................................3
Repair of Leaks.............................................34
Reversing Exchanger......................................2
Safety ...........................................................33
Scope of Supply............................................20
Secondary Heat Transfer Surface.................45
Services..........................................................2
Shear Plate Support Arrangement ................25
Shipment.......................................................19
Shop Operation.............................................17
Shut-down.....................................................32
Side bars...................................................4, 41
Single Banking..............................................46
Single-Phase Pressure Loss.........................53
Site leak Detection........................................33
Sliding Guide Frame .....................................24
Solvent Injection System...............................59
Spare parts ...................................................21
Special Features...........................................42
Specification Sheets ...............................47–49
Stacking Arrangement...................................55
Stacking height ...............................................1
Standard Sizes .............................................38
Cap Sheets ...............................................38
Fins ...........................................................38
Parting Sheets...........................................38
Side Bars...................................................38
STANDARDS
MECHANICAL.....................................35–42
Start-up.........................................................31
Subcooler Reboiler .........................................2
Sulphur Dioxide...............................................2
Supply
Scope of....................................................20
Support Arrangement
Angle Bracket............................................26
Shear Plate ...............................................25
Support Beams .............................................23
Support Insulation.........................................24
Supports .......................................................21
Surface Area.................................................47
Surging .........................................................31
Swedish Pressure Vessel Code....................35
Temperature
Design.......................................................37
Temperature Differences
Permissible................................................37
Temperature Limitations ...............................37
Testing..........................................................36
Field ..........................................................29
Non-Destructive.........................................29
Pressure....................................................29
THERMAL DESIGN................................45–55
STANDARDS OF THE BRAZED ALUMINIUM PLATE-FIN HEAT EXCHANGER MANUFACTURER'S ASSOCIATION 69
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