Gotowe bibliografie tematyczne / Heat and mass transfer analysis

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Gotowa bibliografia na temat „Heat and mass transfer analysis”

Autor: Grafiati
Data publikacji: 6 września 2023

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Artykuły w czasopismach na temat "Heat and mass transfer analysis"

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Ishii, Koji, Yuji Kodama i Toru Maekawa. "Microscopic dynamic analysis of heat and mass transfer". Nonlinear Analysis: Theory, Methods & Applications 30, nr 5 (grudzień 1997): 2797–802. http://dx.doi.org/10.1016/s0362-546x(97)00369-6.

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Aziz Rohman Hakim, Abdul, i Engkos Achmad Kosasih. "ANALYSIS OF HEAT AND MASS TRANSFER ON COOLING TOWER FILL". Jurnal Forum Nuklir 14, nr 1 (29.03.2020): 25. http://dx.doi.org/10.17146/jfn.2020.14.1.5812.

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This paper discusses heat and mass transfer in cooling tower fill. In this research, dry bulb temperature at the bottom fill, ambient relative humidity, air stream velocity entering fill, dry bulb temperature leaving the fill, relative humidity of air leaving the fill, inlet and outlet water temperature of cooling tower were measured. Those data used in heat and mass transfer calculation in cooling tower fill. Then, do the heat and mass transfer calculation based on proposed approch. The results are compared with design data. The design and analogy method showed different result. The parameter which influence the heat transfer at cooling tower are represented by coefficient of heat transfer hl and coefficient of mass transfer k­l. The differencies result between design and analogy method shows that there is important parameter which different. Deeply study needed for it.
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Li, Qiong, Yong Sheng Niu, Yi Xiang Sun i Zhe Liu. "Heat and Mass Transfer Analysis of Mine Exhaust Air Heat Exchanger". Advanced Materials Research 765-767 (wrzesień 2013): 3018–22. http://dx.doi.org/10.4028/www.scientific.net/amr.765-767.3018.

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As a good energy resource, Mine exhaust air has an important value of recycling. In this paper, the heat and mass exchange mechanism and potential of the mine exhaust air heat exchanger (MEAHE) is mainly researched. The heat exchanger efficiency is affected by water and air temperature and flow in terms of double efficiency method. The result can provide the basis for the further determine the thermal calculation method for MEAHE, and lays the foundation for the mine comprehensive utilization of waste heat recovery system design.
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WANG, ZAN-SHE, ZHAO-LIN GU, GUO-ZHENG WANG, FENG CUI i SHI-YU FENG. "ANALYSIS ON MEMBRANE HEAT EXCHANGER APPLIED TO ABSORPTION CHILLER". International Journal of Air-Conditioning and Refrigeration 19, nr 03 (wrzesień 2011): 167–75. http://dx.doi.org/10.1142/s2010132511000557.

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A novel membrane heat exchanger was proposed and analyzed. It was expected that the novel heat exchanger could be applied to the lithium bromide absorption chiller. Polyvinylidene fluoride hollow fiber module was adopted as the solution heat exchanger. The hot feed solution from the generator flowed into the lumen side of the membranes while the cold feed solution from the absorber flowed away from the shell side. Heat transfer and mass transfer occurred simultaneously in the membrane module, and only water vapor could diffuse across the membrane pore due to the water vapor pressure difference between the inside and outside of the membrane. Mathematical equations of the heat and mass transfer processes in the membrane heat exchanger were built, and the parallel flow process and the counter flow process were compared by numerical simulation. The simulation results show that the counter flow process was the better flow mode because the mean temperature difference was larger and the mass transfer was more steadily from the lumen side to the shell side. The heat caused by water vapor mass transfer may account for one-third of the total heat transfer. As a result, the membrane heat exchanger not only reinforced the heat recovery but also enlarged the deflation range and reduced the circulation rate and the heat loads of the generator and absorber. Eventually, the coefficient of performance of the heat exchanger was increased.
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Chati, T., K. Rahmani, T. T. Naas i A. Rouibah. "Moist Air Flow Analysis in an Open Enclosure. Part A: Parametric Study". Engineering, Technology & Applied Science Research 11, nr 5 (12.10.2021): 7571–77. http://dx.doi.org/10.48084/etasr.4344.

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Heat and mass transfer in many systems are widely accomplished applying natural convection process due to their low cost, reliability, and easy support. Typical applications include different mechanisms in various fields such as (solar energy, solar distiller, stream cooling, etc…). Numerical results of turbulent natural convection and mass transfer in an open enclosure for different aspect ratios (AR = 0.5, 1, and 2) with a humid-air are carried out. Mass fraction and local Nusselt number were proposed to investigate the heat and mass transfer. A heat flux boundary conditions were subjected to the lateral walls and the bottom one make as an adiabatic wall, while the top area was proposed as a free surface. Effect of Rayleigh numbers (106≤????????≤108) on natural convection and mass flow behavior are analyzed. The governing equations are solved using CFD Fluent code based on the SIMPLE algorithm. The results showed that the cavity with an aspect ratio of AR = 2 has a significant enhancement to raise the rates of both heat and mass transfer. When the Rayleigh number increases, maximum heat transfer rates were observed due to the fluid flow becomes more vigorous. However, mass transfer improves as the Rayleigh number decreases.
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Magherbi, M., H. Abbassi, N. Hidouri i A. Brahim. "Second Law Analysis in Convective Heat and Mass Transfer". Entropy 8, nr 1 (2.02.2006): 1–17. http://dx.doi.org/10.3390/e8010001.

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TANOUE, Ken-ichiro, Tatsuo NISHIMURA, Koichi GODA i Junichi NODA. "Heat and Mass Transfer Analysis During Torrefaction of Bamboo". Journal of Smart Processing 5, nr 3 (2016): 160–65. http://dx.doi.org/10.7791/jspmee.5.160.

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Bertola, V., i E. Cafaro. "Scale-Size Analysis of Heat and Mass Transfer Correlations". Journal of Thermophysics and Heat Transfer 17, nr 2 (kwiecień 2003): 293–95. http://dx.doi.org/10.2514/2.6768.

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Ye, Hong, Zhi Yuan i Shuanqin Zhang. "The Heat and Mass Transfer Analysis of a Leaf". Journal of Bionic Engineering 10, nr 2 (czerwiec 2013): 170–76. http://dx.doi.org/10.1016/s1672-6529(13)60212-7.

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ALKLAIBI, A., i N. LIOR. "Heat and mass transfer resistance analysis of membrane distillation". Journal of Membrane Science 282, nr 1-2 (5.10.2006): 362–69. http://dx.doi.org/10.1016/j.memsci.2006.05.040.

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Rozprawy doktorskie na temat "Heat and mass transfer analysis"

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Mattingly, Brett T. (Brett Thomas). "Containment analysis incorporating boundary layer heat and mass transfer techniques". Thesis, Massachusetts Institute of Technology, 1999. http://hdl.handle.net/1721.1/84749.

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Tien, Hwa-Chong. "Analysis of flow, heat and mass transfer in porous insulations /". The Ohio State University, 1989. http://rave.ohiolink.edu/etdc/view?acc_num=osu1487672631599499.

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Haq, Inam Ul. "Heat and mass transfer analysis for crud coated PWR fuel". Thesis, Imperial College London, 2011. http://hdl.handle.net/10044/1/6373.

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In water-cooled nuclear reactors, various species are present in the coolant, either in ionic solution, or entrained as very fine particles. Most arise from corrosion of primary circuit surfaces, or from chemicals, such as boric acid, lithium hydroxide, zinc and hydrogen, deliberately added to the coolant. These materials deposit on the surfaces of fuel pins, typically in the upper regions of the core, forming what is generally termed “crud”. This thesis reports a study of the thermal-hydraulic consequences of this deposit. These crud deposits are generally found to contain a large population of through-thickness chimneys, and it is believed that this gives rise to a wick-boiling mechanism of heat transfer. A coupled two-dimensional model of the processes of heat conduction, advection and species diffusion in the crud has been developed. An iterative scheme has been employed to solve the set of coupled equations of each process. The wick boiling process has been found to be an efficient heat transfer mode, taking away about 80% of the heat generated. It has also been found that consideration of heat transfer in the clad can increase the predicted solute concentration in the crud. The effects of some important parameters, such as chimney density, chimney radius, porosity of the crud, crud thickness, clad heat flux and boron concentration in the coolant have been investigated. The fuel thermal performance has been characterized in terms of an effective crud thermal conductivity, and the non-linear dependence this has on parameters such as crud thickness and chimney density had been determined. Lastly, it is observed that plausible pore sizes of the crud, coupled with higher temperatures in the crud, may be such that a film of vapour is generated at the base of the crud. Initial estimates are presented of the cladding temperatures and solute concentration that may be generated as a consequence of this vapour layer.
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Hublitz, Inka. "Heat and mass transfer of a low pressure Mars greenhouse simulation and experimental analysis /". [Gainesville, Fla.] : University of Florida, 2006. http://purl.fcla.edu/fcla/etd/UFE0013488.

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Bohra, Lalit Kumar. "Analysis of Binary Fluid Heat and Mass Transfer in Ammonia-Water Absorption". Diss., Georgia Institute of Technology, 2007. http://hdl.handle.net/1853/19780.

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An investigation of binary fluid heat and mass transfer in ammonia-water absorption was conducted. Experiments were conducted on a horizontal-tube falling-film absorber consisting of four columns of six 9.5 mm (3/8 in) nominal OD, 0.292 m (11.5 in) long tubes, installed in an absorption heat pump. Measurements were recorded at both system and local levels within the absorber for a wide range of operating conditions (nominally, desorber solution outlet concentrations of 5 - 40% for three nominal absorber pressures of 150, 345 and 500 kPa, for solution flow rates of 0.019 - 0.034 kg/s.). Local measurements were supplemented by high-speed, high-resolution visualization of the flow over the tube banks. Using the measurements and observations from videos, heat and mass transfer rates, heat and vapor mass transfer coefficients for each test condition were determined at the component and local levels. For the range of experiments conducted, the overall film heat transfer coefficient varied from 923 to 2857 W/m2-K while the vapor and liquid mass transfer coefficients varied from 0.0026 to 0.25 m/s and from 5.51×10-6 to 3.31×10-5 m/s, respectively. Local measurements and insights from the video frames were used to obtain the contributions of falling-film and droplet modes to the total absorption rates. The local heat transfer coefficients varied from 78 to 6116 W/m2-K, while the local vapor and liquid mass transfer coefficients varied from -0.04 to 2.8 m/s and from -3.59×10-5 (indicating local desorption in some cases) to 8.96×10-5 m/s, respectively. The heat transfer coefficient was found to increase with solution Reynolds number, while the mass transfer coefficient was found to be primarily determined by the vapor and solution properties. Based on the observed trends, correlations were developed to predict heat and mass transfer coefficients valid for the range of experimental conditions tested. These correlations can be used to design horizontal tube falling-film absorbers for ammonia-water absorption systems.
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Ojada, Ejiro Stephen. "Analysis of mass transfer by jet impingement and study of heat transfer in a trapezoidal microchannel". [Tampa, Fla] : University of South Florida, 2009. http://purl.fcla.edu/usf/dc/et/SFE0003297.

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Duda, Anna. "Numerical analysis of heat and mass transfer processes within an infant radiant warmer". Thesis, University of Leeds, 2011. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.555901.

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An optimal thermal environment is regarded as a priority in the medical care of newborn infants (neonatology). Survival of each neonate (newborn infant) depends on the ability to regulate its temperature. Preterm and small neonates often cannot respond to the environmental temperature changes. For this reason, maintenance of neonates bodies within a narrow temperature range is essential for their survival and growth. However, there is one major concern when using radiant warmers, namely the neonates often become severely dehydrated when nursed in these devices. For this reason, the major objective of this thesis is to find a solution to this difficulty. In order to achieve this goal, numerical techniques including Computational Fluid Dynamics and conjugate heat transfer were employed. Mathematical mod- els applied to living organisms can provide a better understanding of the thermal processes occurring i~side a human body, together with their interactions with the surrounding environment. Therefore, in this thesis we focus on developing a model of a neonate under a radiant warmer that incorporates both heat and mass transfer processes in order to provide a better understanding of how a radiative heat source interacts with a neonate. The numerical models were prepared in ANSYS FLUENT and ANSYS CFX commercial softwares. The flow was assumed to be turbulent, and radiation cal- culations were performed as they are a crucial part of this analysis. Moreover, a semi-analytical ray tracking method was developed for the purpose of validating the numerical results. A good general agreement was observed when comparing the ray tracking results with the numerical ones. Next, a heat generation within the newborn was considered, and the numerical data was validated against the analytical calculations, and this comparison showed a good agreement of the results obtained using these two different techniques. Finally, several modifications to the geometry and operation of the radiant warmer are introduced in order to assist with the difficulty of high temperature gradients being obtained on the skin of the newborns nursed under the radiant warmer. It was found that the proposed modifications reduce the large temperature differences on the skin of the newborn. A more uniform temperature field on the skin will result in decreasing the evaporative loss. The proposed modifications in- clude to different approaches. Namely, the first solution, being a high conductivity blanket, can be easily implemented by the staff of the hospital. The second solution introduces modifications to the design of the radiant warmer, and it could be of interest to the producer of the device. Therefore, the main goal of this project, namely to find a solution to newborns becoming dehydrated when nursed under radiant warmers, has been successfully achieved.
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Subramaniam, Vishwanath. "Computational analysis of binary-fluid heat and mass transfer in falling films and droplets". Diss., Atlanta, Ga. : Georgia Institute of Technology, 2008. http://hdl.handle.net/1853/26485.

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Thesis (Ph.D)--Mechanical Engineering, Georgia Institute of Technology, 2009.
Committee Chair: Garimella, Srinivas; Committee Member: Fuller, Tom; Committee Member: Jeter, Sheldon; Committee Member: Lieuwen, Tim; Committee Member: Wepfer, William. Part of the SMARTech Electronic Thesis and Dissertation Collection.
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Olanrewaju, Anuoluwapo Mary. "Analysis of boundary layer flow of nanofluid with the characteristics of heat and mass transfer". Thesis, Cape Peninsula University of Technology, 2011. http://hdl.handle.net/20.500.11838/2157.

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Thesis (MTech (Mechanical Engineering))--Cape Peninsula University of Technology, 2011.
Nanofluid, which was first discovered by the Argonne laboratory, is a nanotechnology- based heat transfer fluid. This fluid consists of particles which are suspended inside conventional heat transfer liquid or base fluid. The purpose of this suspension is for enhancing thermal conductivity and convective heat transfer performance of this base fluid. The name nanofluid came about as a result of the nanometer- sized particles of typical length scales 1-100nm which are stably suspended inside of the base fluids. These nanoparticles are of both physical and chemical classes and are also produced by either the physical process or the chemical process. Nanofluid has been discovered to be the best option towards accomplishing the enhancement of heat transfer through fluids in different unlimited conditions as well as reduction in the thermal resistance by heat transfer liquids. Various manufacturing industries and engineering processes such as transportation, electronics, food, medical, textile, oil and gas, chemical, drinks e.t.c, now aim at the use of this heat transfer enhancement fluid. Advantages such organisations can obtain from this fluid includes, reduced capital cost, reduction in size of heat transfer system and improvement of energy efficiencies. This research has been able to solve numerically, using Maple 12 which uses a fourth- fifth order Runge -kutta- Fehlberg algorithm alongside shooting method, a set of nonlinear coupled differential equations together with their boundary conditions, thereby modelling the heat and mass transfer characteristics of the boundary layer flow of the nanofluids. Important properties of these nanofluids which were considered are viscosity, thermal conductivity, density, specific heat and heat transfer coefficients and microstructures (particle shape, volume concentration, particle size, distribution of particle, component properties and matrixparticle interface). Basic fluid dynamics equations such as the continuity equation, linear momentum equation, energy equation and chemical species concentration equations have also been employed.
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Torres, Alvarez Juan Felipe. "A study of heat and mass transfer in enclosures by phase-shifting interferometry and bifurcation analysis". Thesis, Ecully, Ecole centrale de Lyon, 2014. http://www.theses.fr/2014ECDL0001/document.

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Des questions fondamentales concernant les propriétés de diffusion des systèmes biologiques dans des conditions isothermes et non-isothermes restent en suspens en raison de l’absence de techniques expérimentales capables de visualiser et de mesurer les phénomènes de diffusion avec une très bonne précision. Il existe en conséquence un besoin de développer de nouvelles techniques expérimentales permettant d’approfondir notre compréhension des phénomènes de diffusion. La convection naturelle en cavité tridimensionnelle inclinée est elle-aussi très peu étudiée. Cette inclinaison de la cavité peut correspondre à un léger défaut expérimental ou être imposée volontairement. Dans cette thèse, nous étudions les phénomènes de transport de chaleur et de masse en cavité parallélépipédique, nous intéressant particulièrement à la thermodiffusion en situation sans convection et à la convection naturelle en fluide pur (sans thermodiffusion). La diffusion de masse est étudiée à l’aide d’une nouvelle technique optique, tandis que la convection naturelle est tout d’abord étudiée en détails avec une méthode numérique sophistiquée, puis visualisée expérimentalement à l’aide du même système optique que pour les mesures de diffusion. Nous présentons l’interféromètre optique de haute précision développé pour les mesures de diffusion. Cet interféromètre comprend un interféromètre polarisé de Mach–Zehnder, un polariseur tournant, une caméra CCD et un algorithme de traitement d’images original. Nous proposons aussi une méthode pour déterminer le coefficient de diffusion isotherme en fonction de la concentration. Cette méthode, basée sur une analyse inverse couplée à un calcul numérique, permet de déterminer les coefficients de diffusion à partir des profils de concentration transitoires obtenus par le système optique. Mentionnons de plus que c’est la première fois que la thermodiffusion est visualisée dans des solutions aqueuses de protéines. La méthode optique proposée présente trois avantages principaux par rapport aux autres méthodes similaires : (i) un volume d’échantillon réduit, (ii) un temps de mesure court, (iii) une stabilité hydrodynamique améliorée. Toutes ces méthodes ont été validées par des mesures sur des systèmes de référence. La technique optique est d’abord utilisée pour étudier la diffusion isotherme dans des solutions de protéines : (a) dans des solutions binaires diluées, (b) dans des solutions binaires sur un large domaine de concentration, (c) dans des solutions ternaires diluées. Les résultats montrent que (a) le coefficient de diffusion isotherme dans les systèmes dilués décroit avec la masse moléculaire, comme prédit grossièrement par l’équation de Stokes-Einstein ; (b) la protéine BSA a un comportement diffusif de type sphère dure et la protéine lysozyme de type sphère molle ; (c) l’effet de diffusion croisée est négligeable dans les systèmes ternaires dilués. La technique optique est aussi utilisée (d) dans des solutions binaires diluées non-isothermes, révélant que les molécules d’aprotinin (6.5 kDa) et de lysozyme (14.3 kDa) sont, respectivement, thermophiliques et thermo-phobiques, quand elles sont en solutions aqueuses à température ambiante. Enfin, la technique optique est utilisée pour l’étude de la convection de Rayleigh-Bénard en cavité cubique horizontale. Puisque la convection peut aussi être étudiée de façon réaliste en utilisant les équations de Navier-Stokes, une analyse numérique de bifurcation est proposée, permettant une étude approfondie de la convection naturelle dans des cavités tridimensionnelles parallélépipédiques. Pour cela, une méthode de continuation a été développée à partir d’un code aux éléments finis spectraux. La méthode numérique proposée est particulièrement bien adaptée aux études de convection correspondant à des diagrammes de bifurcation complexes. [...]
Fundamental questions concerning the mass diffusion properties of biological systems under isothermal and non-isothermal conditions still remain due to the lack of experimental techniques capable of visualizing and measuring mass diffusion phenomena with a high accuracy. As a consequence, there is a need to develop new experimental techniques that can deepen our understanding of mass diffusion. Moreover, steady natural convection in a tilted three-dimensional rectangular enclosure has not yet been studied. This tilt can be a slight defect of the experimental device or can be imposed on purpose. In this dissertation, heat and mass transfer phenomena in parallelepiped enclosures are studied focusing on convectionless thermodiffusion and on natural convection of pure fluids (without thermodiffusion). Mass diffusion is studied with a novel optical technique, while steady natural convection is first studied in detail with an improved numerical analysis and then with the same optical technique initially developed for diffusion measurements. A construction of a precise optical interferometer to visualize and measure mass diffusion is described. The interferometer comprises a polarizing Mach–Zehnder interferometer, a rotating polariser, a CCD camera, and an original image-processing algorithm. A method to determine the isothermal diffusion coefficient as a function of concentration is proposed. This method uses an inverse analysis coupled with a numerical calculation in order to determine the diffusion coefficients from the transient concentration profiles measured with the optical system. Furthermore, thermodiffusion of protein molecules is visualized for the first time. The proposed method has three main advantages in comparison to similar methods: (i) reduced volume sample, (ii) short measurement time, and (iii) increased hydrodynamic stability of the system. These methods are validated by determining the thermophysical properties of benchmark solutions. The optical technique is first applied to study isothermal diffusion of protein solutions in: (a) dilute binary solutions, (b) binary solutions with a wide concentration range, and (c) dilute ternary solutions. The results show that (a) the isothermal diffusion coefficient in dilute systems decreases with molecular mass, as roughly predicted by the Stokes-Einstein equation; (b) BSA protein has a hard-sphere-like diffusion behaviour and lysozyme protein a soft sphere characteristic; and (c) the cross-term effect between the diffusion species in a dilute ternary system is negligible. The optical technique is then applied to (d) non-isothermal dilute binary solutions, revealing that that the aprotinin (6.5 kDa) and lysozyme (14.3 kDa) molecules are thermophilic and thermophobic, respectively, when using water as solvent at room temperature. Finally, the optical technique is applied to study Rayleigh-Bénard convection in a horizontal cubical cavity. Since natural convection can be studied in more depth by solving the Navier-Stokes equations, a bifurcation analysis is proposed to conduct a thorough study of natural convection in three-dimensional parallelepiped cavities. Here, a continuation method is developed from a three-dimensional spectral finite element code. The proposed numerical method is particularly well suited for the studies involving complex bifurcation diagrams of three-dimensional convection in rectangular parallelepiped cavities. This continuation method allows the calculation of solution branches, the stability analysis of the solutions along these branches, the detection and precise direct calculation of the bifurcation points, and the jump to newly detected stable or unstable branches, all this being managed by a simple continuation algorithm. This can be used to calculate the bifurcation diagrams describing the convection in tilted cavities. [...]
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Książki na temat "Heat and mass transfer analysis"

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Eckert, E. R. G. Analysis of heat and mass transfer. Washington: Hemisphere Pub. Corp., 1987.

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1966-, Robinson Anne Skaja, i Wagner Norman Joseph 1962-, red. Mass and heat transfer: Analysis of mass contactors and heat exchangers. Cambridge: Cambridge University Press, 2008.

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Alifanov, O. M. Inverse heat transfer problems. Berlin: Springer-Verlag, 1994.

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An introduction to mass and heat transfer: Principles of analysis and design. New York: John Wiley & Sons, 1998.

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Necati, Özışık M., red. Unified analysis and solutions of heat and mass diffusion. New York: Dover, 1994.

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Delgado, J. M. P. Q., Antonio Gilson Barbosa de Lima i Marta Vázquez da Silva, red. Numerical Analysis of Heat and Mass Transfer in Porous Media. Berlin, Heidelberg: Springer Berlin Heidelberg, 2012. http://dx.doi.org/10.1007/978-3-642-30532-0.

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Barbosa, Lima Antonio Gilson, Silva Marta Vázquez i SpringerLink (Online service), red. Numerical Analysis of Heat and Mass Transfer in Porous Media. Berlin, Heidelberg: Springer Berlin Heidelberg, 2012.

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Shang, De-Yi. Free Convection Film Flows and Heat Transfer: Laminar free Convection of Phase Flows and Models for Heat-Transfer Analysis. Wyd. 2. Berlin, Heidelberg: Springer Berlin Heidelberg, 2012.

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Luo, Lingai. Heat and Mass Transfer Intensification and Shape Optimization: A Multi-scale Approach. London: Springer London, 2013.

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Yarin, L. P. The Pi-Theorem: Applications to Fluid Mechanics and Heat and Mass Transfer. Berlin, Heidelberg: Springer Berlin Heidelberg, 2012.

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Części książek na temat "Heat and mass transfer analysis"

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Shang, De-Yi. "New Similarity Analysis Method for Laminar Free Convection Boundary Layer and Film Flows". W Heat and Mass Transfer, 53–71. Berlin, Heidelberg: Springer Berlin Heidelberg, 2012. http://dx.doi.org/10.1007/978-3-642-28983-5_4.

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De Angelis, Alessandra, Onorio Saro, Giulio Lorenzini, Stefano D’Elia i Marco Medici. "Numerical Analysis". W Simplified Models for Assessing Heat and Mass Transfer in Evaporative Towers, 69–75. Cham: Springer International Publishing, 2013. http://dx.doi.org/10.1007/978-3-031-79360-8_9.

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Barman, H., i R. S. Das. "Simultaneous Heat and Mass Transfer Analysis in Falling Film Absorber". W Advances in Mechanical Engineering, 1001–11. Singapore: Springer Singapore, 2020. http://dx.doi.org/10.1007/978-981-15-0124-1_89.

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Buchholz, Niklas, i Andrea Luke. "Analysis of the Influence of Thermophysical Properties on the Coupled Heat and Mass Transfer in Pool Boiling". W Advances in Heat Transfer and Thermal Engineering, 147–50. Singapore: Springer Singapore, 2021. http://dx.doi.org/10.1007/978-981-33-4765-6_27.

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Khan, Shafat Ahmad, Fazia Taj, Samira Habib, Falak Shawl, Aamir Hussain Dar i Madhuresh Dwivedi. "CFD Analysis of Drying of Cereal, Fruits, and Vegetables". W Advanced Computational Techniques for Heat and Mass Transfer in Food Processing, 235–46. Boca Raton: CRC Press, 2022. http://dx.doi.org/10.1201/9781003159520-11.

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Zgurovsky, M. Z., i V. S. Mel’nik. "Mathematical Formalization and Computational Realization of Diffusion and Heat-Mass Transfer Processes". W Nonlinear Analysis and Control of Physical Processes and Fields, 451–500. Berlin, Heidelberg: Springer Berlin Heidelberg, 2004. http://dx.doi.org/10.1007/978-3-642-18770-4_10.

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Zgurovsky, M. Z., i V. S. Mel’nik. "Problems of Control of Physical Processes of Diffusion and Heat-Mass Transfer". W Nonlinear Analysis and Control of Physical Processes and Fields, 431–49. Berlin, Heidelberg: Springer Berlin Heidelberg, 2004. http://dx.doi.org/10.1007/978-3-642-18770-4_9.

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Selimefendigil, Fatih, Seda Özcan Çoban i Hakan F. Öztop. "Convective Drying Analysis of Different Shaped Moving Porous Objects in a Channel with Area Expansion by Using Finite Element Method". W Advanced Computational Techniques for Heat and Mass Transfer in Food Processing, 67–90. Boca Raton: CRC Press, 2022. http://dx.doi.org/10.1201/9781003159520-4.

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Ghoulem, Marouen, Khaled El Moueddeb i Ezzedine Nehdi. "Numerical Analysis of Heat and Mass Transfer in a Naturally Ventilated Greenhouse with Plants". W Advances in Science, Technology & Innovation, 265–68. Cham: Springer International Publishing, 2022. http://dx.doi.org/10.1007/978-3-031-00808-5_61.

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Dey, Debasish, i Madhurya Hazarika. "Entropy Generation Analysis of MHD Fluid Flow Over Stretching Surface with Heat and Mass Transfer". W Emerging Technologies in Data Mining and Information Security, 57–67. Singapore: Springer Nature Singapore, 2022. http://dx.doi.org/10.1007/978-981-19-4193-1_6.

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Streszczenia konferencji na temat "Heat and mass transfer analysis"

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Vermeersch, B., i G. De Mey. "Sinusoidal regime analysis of heat transfer in microelectronic systems". W HEAT AND MASS TRANSFER 2006. Southampton, UK: WIT Press, 2006. http://dx.doi.org/10.2495/ht060431.

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Ciambelli, P., M. G. Meo, P. Russo i S. Vaccaro. "Sensitivity analysis of a computer code for modelling confined fires". W HEAT AND MASS TRANSFER 2006. Southampton, UK: WIT Press, 2006. http://dx.doi.org/10.2495/ht060301.

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Serag-Eldin, M. A. "Analysis of a new solar chimney plant design for mountainous regions". W HEAT AND MASS TRANSFER 2006. Southampton, UK: WIT Press, 2006. http://dx.doi.org/10.2495/ht060421.

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Yuan, J., C. Wilhelmsson i B. Sundén. "Analysis of water condensation and two-phase flow in a channel relevant for plate heat exchangers". W HEAT AND MASS TRANSFER 2006. Southampton, UK: WIT Press, 2006. http://dx.doi.org/10.2495/ht060341.

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Kulkarni, Ratnakar, i Paul Cooper. "NATURAL CONVECTION IN AN ENCLOSURE WITH LOCALISED HEATING AND COOLING: COMPARISON OF FLOW ELEMENT ANALYSIS AND EXPERIMENTS". W Heat and Mass Transfer Australasia. Connecticut: Begellhouse, 2023. http://dx.doi.org/10.1615/978-1-56700-099-3.80.

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Slavica, Eremic, Ilic Mirjana, Vasiljevic Bogosav i Vranic Kosta. "Analysis Of Influence Of Leading Away The Heat From The Prosthetic Appliances Upon The Feeling Of Their Users". W Heat and Mass Transfer Australasia. Connecticut: Begellhouse, 2023. http://dx.doi.org/10.1615/978-1-56700-099-3.650.

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Shin, Chee Burm, Eun Kyum Kim i Lae Hyun Kim. "HEAT TRANSFER ANALYSIS OF PIPE COOLING FOR MASS CONCRETE". W International Heat Transfer Conference 11. Connecticut: Begellhouse, 1998. http://dx.doi.org/10.1615/ihtc11.2590.

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Vala, J., i S. Št’astník. "On Two‐Scale Modelling of Heat and Mass Transfer". W NUMERICAL ANALYSIS AND APPLIED MATHEMATICS: International Conference on Numerical Analysis and Applied Mathematics 2008. American Institute of Physics, 2008. http://dx.doi.org/10.1063/1.2990989.

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Yue, Min, Katherine Dunphy, Jerry Jenkins, Christopher Dames, Guanghua Wu i Arun Majumdar. "A Microfluidic Device for Studying Mass Transfer Effects in Biomolecular Analysis". W International Heat Transfer Conference 12. Connecticut: Begellhouse, 2002. http://dx.doi.org/10.1615/ihtc12.3990.

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Jancskar, I., i A. Ivanyi. "Wavelet Analysis of IR-images of a Turbulent Steam Flow". W Turbulence, Heat and Mass Transfer 5. Proceedings of the International Symposium on Turbulence, Heat and Mass Transfer. New York: Begellhouse, 2006. http://dx.doi.org/10.1615/ichmt.2006.turbulheatmasstransf.440.

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Raporty organizacyjne na temat "Heat and mass transfer analysis"

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Pesaran, A. A. Heat and mass transfer analysis of a desiccant dehumidifier matrix. Office of Scientific and Technical Information (OSTI), lipiec 1986. http://dx.doi.org/10.2172/5438707.

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Maclaine-Cross, I. L., i A. A. Pesaran. Heat and Mass Transfer Analysis of Dehumidifiers Using Adiabatic Transient Tests. Office of Scientific and Technical Information (OSTI), kwiecień 1986. http://dx.doi.org/10.2172/1129251.

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Zyvoloski, G., Z. Dash i S. Kelkar. FEHM: finite element heat and mass transfer code. Office of Scientific and Technical Information (OSTI), marzec 1988. http://dx.doi.org/10.2172/5495517.

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Zyvoloski, G., Z. Dash i S. Kelkar. FEHMN 1.0: Finite element heat and mass transfer code. Office of Scientific and Technical Information (OSTI), kwiecień 1991. http://dx.doi.org/10.2172/138080.

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Goldstein, R. J., i M. Y. Jabbari. The impact of separated flow on heat and mass transfer. Office of Scientific and Technical Information (OSTI), styczeń 1990. http://dx.doi.org/10.2172/6546146.

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Bell, J., i L. Hand. Calculation of Mass Transfer Coefficients in a Crystal Growth Chamber through Heat Transfer Measurements. Office of Scientific and Technical Information (OSTI), kwiecień 2005. http://dx.doi.org/10.2172/918405.

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Drost, Kevin, Goran Jovanovic i Brian Paul. Microscale Enhancement of Heat and Mass Transfer for Hydrogen Energy Storage. Office of Scientific and Technical Information (OSTI), wrzesień 2015. http://dx.doi.org/10.2172/1225296.

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Zyvoloski, G., Z. Dash i S. Kelkar. FEHMN 1.0: Finite element heat and mass transfer code; Revision 1. Office of Scientific and Technical Information (OSTI), maj 1992. http://dx.doi.org/10.2172/138419.

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Kukuck, S. Heat and mass transfer through gypsum partitions subjected to fire exposures. Gaithersburg, MD: National Institute of Standards and Technology, 2009. http://dx.doi.org/10.6028/nist.ir.7461.

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Prucha, R. H. Heat and mass transfer in the Klamath Falls, Oregon, geothermal system. Office of Scientific and Technical Information (OSTI), maj 1987. http://dx.doi.org/10.2172/6247658.

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