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Artykuły w czasopismach na temat "Heat engineering"
Kolomeitsev, V. V., i E. F. Kolomeitseva. "Heat Engineering". Refractories and Industrial Ceramics 40, nr 1-2 (styczeń 1999): 64–69. http://dx.doi.org/10.1007/bf02762450.
Pełny tekst źródłaDobáková, Romana, Natália Jasminská, Tomáš Brestovič, Mária Čarnogurská i Marián Lázár. "Dimensional analysis application when calculating heat losses". International Journal of Engineering Research and Science 3, nr 9 (30.09.2017): 29–34. http://dx.doi.org/10.25125/engineering-journal-ijoer-sep-2017-5.
Pełny tekst źródłaAkhmetov, Dr Sairanbek, i Dr Anarbay Kudaykulov. "On the Method of Construction of the Dependence of the Heat Extension Coefficient on Temperature in Heat-resistant Alloys". International Journal of Engineering Research and Science 3, nr 8 (31.08.2017): 20–29. http://dx.doi.org/10.25125/engineering-journal-ijoer-aug-2017-4.
Pełny tekst źródłaGarimella, Srinivas, i Matthew Hughes. "Engineering for Heat Waves". American Scientist 111, nr 6 (2023): 328. http://dx.doi.org/10.1511/2023.111.6.328.
Pełny tekst źródłaVereshchagina, T., N. Loginov i A. Sorokin. "HEAT PIPES IN NUCLEAR ENGINEERING". PROBLEMS OF ATOMIC SCIENCE AND TECHNOLOGY. SERIES: NUCLEAR AND REACTOR CONSTANTS 2021, nr 4 (26.12.2021): 213–33. http://dx.doi.org/10.55176/2414-1038-2021-4-213-233.
Pełny tekst źródłaKotake, Susumu. "Molecular Engineering in Heat Transfer". International Journal of Fluid Mechanics Research 25, nr 4-6 (1998): 468–81. http://dx.doi.org/10.1615/interjfluidmechres.v25.i4-6.20.
Pełny tekst źródłaBall, Philip. "Computer engineering: Feeling the heat". Nature 492, nr 7428 (grudzień 2012): 174–76. http://dx.doi.org/10.1038/492174a.
Pełny tekst źródłaBansal, Pradeep. "Advances in Heat Transfer Engineering". Heat Transfer Engineering 31, nr 12 (październik 2010): 963–64. http://dx.doi.org/10.1080/01457631003638903.
Pełny tekst źródłaGlaeser, W. A. "Surface engineering and heat treatment". Tribology International 30, nr 3 (marzec 1997): 245–46. http://dx.doi.org/10.1016/s0301-679x(96)00035-7.
Pełny tekst źródłaProskuryakov, A. G., E. N. Videneev, V. N. Proselkov, V. P. Spasskov i K. V. Simonov. "Estimating VVÉR heat engineering reliability". Soviet Atomic Energy 68, nr 3 (marzec 1990): 187–91. http://dx.doi.org/10.1007/bf02074083.
Pełny tekst źródłaRozprawy doktorskie na temat "Heat engineering"
Razavinia, Nasimalsadat. "Waste heat recovery with heat pipe technology". Thesis, McGill University, 2010. http://digitool.Library.McGill.CA:80/R/?func=dbin-jump-full&object_id=94983.
Pełny tekst źródłaL'énergie d'haut grade de nos jours est produite principalement à base de combustion d'hydrocarbure et les réserves de cette énergie deviennent de plus en plus rare, mais certaines énergies alternatives connues gagnent des forces parmi les marchés incluant les sources d'énergie renouvelables et recyclées. Les usines pyrométallurgiques sont des consommateurs significatifs d'énergie d'haut grade. Ces procédés industriels relâches un montant important de chaleurs (perte) à l'environnement sans aucune récupération. Le but du projet est de concentrer, capturer et convertir cette chaleur résiduelle de basse qualité en énergie valable. Par contre, l'objectif principal du projet comme tel est de développer et de perfectionner un caloduc capable d'extraire cette chaleur parvenant des gaz effluents. Le point d'ébullition d'une substance (vapeur) est utilisé comme moyen de concentrer l'énergie contenu dans les effluents avec la technologie des caloducs. Pour maximiser les gains énergétiques, la conception de ce caloduc en particulier utilise des canaux de retour indépendant ainsi qu'un modificateur de débit dans l'évaporateur, lui permettant d'extraire un niveau supérieur de chaleur. Pendant les essais lors du projet, les éléments limitants des systèmes de caloducs ont été identifiés. Les configurations du système ont été ajustées et modifiés dans la phase expérimentale d'essai pour surmonter ces limitations et maximiser l'extraction de chaleur.
Nyholm, Joakim. "Horizontal wastewater heat recovery heat exchanger, a model". Thesis, KTH, Energiteknik, 2019. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-263618.
Pełny tekst źródłaByggnads och servicesektorn står för cirka 40 procent av Sveriges energibehov. Av de 40 procenten består 90% av energibehov ifrån hushåll och kontorsbyggnader. Totalt sett 80 TWh används för uppvärmning av byggnader samt varmvatten. Då uppvärmning alltid varit en stor del av energibehovet i Sverige är det naturligt att det skett en rad förbättringar på vägen. Det finns en ny anläggning på Pennfäktaren 11 i Stockholm, en horisontell värmeväxlare för avloppsvatten. Den här uppsatsen fokuserar på att skapa en modell i TRNSYS av en värmeväxlare där parametrar som vattenflöde, temperatur, och mer kan användas för att bedöma den tekniska aspekten av en installation av värmeväxlare i en byggnad. Modellen kan simulera prestandan av en ensam värmeväxlare, med endast ett fåtal parametrar som behövs. Modellen baseras på mätdata ifrån anläggningen på Pennfäktaren, denna mätdata har sedan använts för att beräkna först massflödet av avloppsvatten men också för att bestämma hur mycket värme som är möjligt att återvinna utan att överskrida det byggnaden faktiskt kan använda. Då det bara finns data ifrån en källa fick den anses som korrekt, dock gjordes en del ändringar där data helt enkelt var omöjligt, t.ex. negativa avloppsflöden och flödesmängder så höga att de inte ska kunna vara möjliga. Den färdiga modellen använder mätdata tillsammans med de beräknade värdena. Detta används för att genom modellen beräkna temperaturvärden för utgående vatten och avlopp samt den totala mängden återvunnen värme. I referensscenariot kunde totalt 25,3 MWh värme återvinnas men det bästa scenariot med ökad avloppstemperatur och avloppsflöde kunde närmare 47,2 MWh återvinnas, nästan det dubbla från referensvärdet. För att sammanfatta ger modellens simulationer rimliga värden för värmeväxlaren. Det bör därför vara fullt möjligt att använda modellen för att bedöma ett hus rimlighet till en värmeväxlarinstallation.
Staats, Wayne Lawrence. "Active heat transfer enhancement in integrated fan heat sinks". Thesis, Massachusetts Institute of Technology, 2012. http://hdl.handle.net/1721.1/78179.
Pełny tekst źródłaThis electronic version was submitted by the student author. The certified thesis is available in the Institute Archives and Special Collections.
Cataloged from PDF version of thesis.
Includes bibliographical references (p. 205-211).
Modern computer processors require significant cooling to achieve their full performance. The "efficiency" of heat sinks is also becoming more important: cooling of electronics consumes 1% of worldwide electricity use by some estimates. Unfortunately, current cooling technologies often focus on improving heat transfer at the expense of efficiency. The present work focuses on a unique, compact, and efficient air cooled heat sink which addresses these shortcomings. While conventional air cooled heat sinks typically use a separate fan to force air flow over heated fins, the new design incorporates centrifugal fans directly into the body of a loop heat pipe with multiple planar condensers. These "integrated fans" rotate between the planar condensers, in close proximity to the hot surfaces, establishing a radially outward flow of cooling air. The proximity of the rotating impellers to the condenser surfaces results in a marked enhancement in the convective heat transfer coefficient without a large increase in input power. To develop an understanding of the heat transfer in integrated fan heat sinks, a series of experiments was performed to simultaneously characterize the fan performance and average heat transfer coefficients. These characterizations were performed for 15 different impeller profiles with various impeller-to-gap thickness ratios. The local heat transfer coefficient was also measured using a new heated-thin-film infrared thermography technique capable of applying various thermal boundary conditions. The heat transfer was found to be a function of the flow and rotational Reynolds numbers, and the results suggest that turbulent flow structures introduced by the fans govern the transport of thermal energy in the air. The insensitivity of the heat transfer to the impeller profile decouples the fan design from the convection enhancement problem, greatly simplifying the heat sink design process. Based on the experimental results, heat transfer and fan performance correlations were developed (most notably, a two-parameter correlation that predicts the dimensionless heat transfer coefficients across 98% of the experimental work to within 20% relative RMS error). Finally, models were developed to describe the scaling of the heat transfer and mechanical power consumption in multi-fan heat sinks. These models were assessed against experimental results from two prototypes, and suggest that future integrated fan heat sink designs can achieve a 4x reduction in thermal resistance and 3x increase in coefficient of performance compared to current state-of-the-art air cooled heat sinks.
by Wayne L. Staats, Jr.
Ph.D.
Meyer, Meyer. "Development of a range of air-to-air heat pipe heat recovery heat exchangers". Thesis, Stellenbosch : University of Stellenbosch, 2004. http://hdl.handle.net/10019.1/16389.
Pełny tekst źródłaENGLISH ABSTRACT: As the demand for less expensive energy is increasing world-wide, energy conservation is becoming a more-and-more important economic consideration. In light of this, means to recover energy from waste fluid streams is also becoming more-and-more important. An efficient and cost effective means of conserving energy is to recover heat from a low temperature waste fluid stream and use this heat to preheat another process stream. Heat pipe heat exchangers (HPHEs) are devices capable of cost effectively salvaging wasted energy in this way. HPHEs are liquid-coupled indirect transfer type heat exchangers except that the HPHE employs heat pipes or thermosyphons as the major heat transfer mechanism from the high temperature to the low-temperature fluid. The primary advantage of using a HPHE is that it does not require an external pump to circulate the coupling fluid. The hot and cold streams can also be completely isolated preventing cross-contamination of the fluids. In addition, the HPHE has no moving parts. In this thesis, the development of a range of air-to-air HPHEs is investigated. Such an investigation involved the theoretical modelling of HPHEs such that a demonstration unit could be designed, installed in a practical industrial application and then evaluated by considering various financial aspects such as initial costs, running costs and energy savings. To develop the HPHE theoretical model, inside heat transfer coefficients for the evaporator and condenser sections of thermosyphons were investigated with R134a and Butane as two separate working fluids. The experiments on the thermosyphons were undertaken at vertical and at an inclination angle of 45° to the horizontal. Different diameters were considered and evaporator to condenser length ratios kept constant. The results showed that R134a provided for larger heat transfer rates than the Butane operated thermosyphons for similar temperature differences despite the fact that the latent heat of vaporization for Butane is higher than that of R134a. As an example, a R134a charged thermosyphon yielded heat transfer rates in the region of 1160 W whilst the same thermosyphon charged with Butane yielded heat transfer rates in the region of 730 W at 23 °C . Results also showed that higher heat transfer rates were possible when the thermosyphons operated at 45°. Typically, for a thermosyphon with a diameter of 31.9 mm and an evaporator to condenser length ratio of 0.24, an increase in the heat transfer rate of 24 % could be achieved. Theoretical inside heat transfer coefficients were also formulated which were found to correlate reasonably well with most proposed correlations. However, an understanding of the detailed two-phase flow and heat transfer behaviour of the working fluid inside thermosyphons is difficult to model. Correlations proposing this behaviour were formulated and include the use of R134a and Butane as the working fluids. The correlations were formulated from thermosyphons of diameters of 14.99 mm, 17.272 mm, 22.225 mm and 31.9 mm. The evaporator to condenser length ratio for the 31.9 mm diameter thermosyphon was 0.24 whilst the other thermosyphons had ratios of 1. The heat fluxes ranged from 1800-43500 W/m2. The following theoretical inside heat transfer coefficients were proposed for vertical and inclined operations (READ CORRECT FORMULA IN FULL TEXT ABSTRACT) φ = 90° ei h = 3.4516x105Ja−0.855Ku1.344 φ = 45° ei h = 1.4796x105Ja−0.993Ku1.3 φ = 90° l l l ci l l v h x k g 1/ 3 2.05 2 4.61561 109Re 0.364 ν ρ ρ ρ − ⎡ ⎡ ⎛ ⎞⎤ ⎤ = ⎢ ⎢ ⎜ ⎟⎥ ⎥ ⎢ ⎢ ⎜ − ⎟⎥ ⎥ ⎣ ⎣ ⎝ ⎠⎦ ⎦ φ = 45° l l l ci l l v h x k g 1/ 3 1.916 2 3.7233 10 5Re 0.136 ν ρ ρ ρ − ⎡ ⎡ ⎛ ⎞⎤ ⎤ = ⎢ ⎢ ⎜ ⎟⎥ ⎥ ⎢ ⎢ ⎜ − ⎟⎥ ⎥ ⎣ ⎣ ⎝ ⎠⎦ ⎦ The theoretically modelled demonstration HPHE was installed into an existing air drier system. Heat recoveries of approximately 8.8 kW could be recovered for the hot waste stream with a hot air mass flow rate of 0.55 kg/s at an inlet temperature of 51.64 °C and outlet temperature of 35.9 °C in an environment of 20 °C. Based on this recovery, energy savings of 32.18 % could be achieved and a payback period for the HPHE was calculated in the region of 3.3 years. It is recommended that not withstanding the accuracies of roughly 25 % achieved by the theoretically predicted correlations to that of the experimental work, performance parameters such as the liquid fill charge ratios, the evaporator to condenser length ratios and the orientation angles should be further investigated.
AFRIKAANSE OPSOMMING: As gevolg van die groeiende aanvraag na goedkoper energie, word die behoud van energie ‘n al hoe belangriker ekonomiese oorweging. Dus word die maniere om energie te herwin van afval-vloeierstrome al hoe meer intensief ondersoek. Een effektiewe manier om energie te herwin, is om die lae-temperatuur-afval-vloeierstroom (wat sou verlore gaan) se hitte te gebruik om ‘n ander vloeierstroom mee te verhit. Hier dien dit dan as voorverhitting van die ander, kouer, vloeierstroom. Hittepyp hitteruilers (HPHR’s) is laekoste toestelle wat gebruik kan word vir hierdie doel. ‘n HPHR is ‘n vloeistof-gekoppelde indirekte-oordrag hitteruiler, behalwe vir die feit dat dié hitteruiler gebruik maak van hittepype (of hittebuise) wat die grootste deel van sy hitteoordragsmeganisme uitmaak. Die primêre voordele van ‘n HPHR is dat dit geen bewegende dele het nie, die koue- en warmstrome totaal geïsoleer bly van mekaar en geen eksterne pomp benodig word om die werkvloeier mee te sirkuleer nie. In hierdie tesis word ‘n ondersoek gedoen oor die ontwikkeling van ‘n bestek van lug-totlug HPHR’s. Hierdie ondersoek het die teoretiese modellering van so ‘n HPHR geverg, sodat ‘n demonstrasie eenheid ontwerp kon word. Hierdie demonstrasie eenheid is geïnstalleer in ‘n praktiese industriële toepassing waar dit geïvalueer is deur na aspekte soos finansiële voordele en energie-besparings te kyk. Om die teoretiese HPHR model te kon ontwikkel, moes daar gekyk word na die binnehitteoordragskoëffisiënte van die verdamper- en kondensordeursneë, asook R134a en Butaan as onderskeie werksvloeiers. Die eksperimente met die hittebuise is gedoen in die vertikale en 45° (gemeet vanaf die horisontaal) posisies. Verskillende diameters is ook ondersoek, maar met die verdamper- en kondensor-lengteverhouding wat konstant gehou is. Die resultate wys dat R134a as werksvloeier in die hittebuise voorsiening maak vir groter hitteoordragstempo’s in vergelyking met Butaan as werksvloeier by min of meer dieselfde temperatuur verskil – dít ten spyte van die feit dat Butaan ‘n hoër latente-hittetydens- verdampings eienskap het. As voorbeeld gee ‘n R134a-gelaaide hittebuis ‘n hitteoordragstempo van omtrent 1160 W terwyl dieselfde hittebuis wat met Butaan gelaai is, slegs ongeveer 730 W lewer by 23 °C. Die resultate wys ook duidelik dat hoër hitteoordragstempo’s verkry word indien die hittebuis bedryf word teen ‘n hoek van 45°. ‘n Tipiese toename in hitteoordragstempo is ongeveer 24 % vir ‘n hittebuis met ‘n diameter van 31.9 mm en ‘n verdamper- tot kondensor-lengteverhouding van 0.24. Teoretiese binne-hitteoordragskoëffisiënte is ook geformuleer. Dié waardes stem redelik goed ooreen met die meeste voorgestelde korrelasies. Nieteenstaande die feit dat gedetailleerde twee-fase-vloei en die hitteoordragsgedrag van die werksvloeier binne hittebuise nog nie goed deur die wetenskaplike wêreld verstaan word nie. Korrelasies wat hierdie gedrag voorstel is geformuleer en sluit weereens die gebruik van R134a en Butaan as werksvloeiers in. Die korrelasies is geformuleer vanaf hittebuise met diameters van onderskeidelik 14.99 mm, 17.272 mm, 22.225 mm en 31.9 mm. Die verdamper- tot kondensor-lengteverhoudings vir die 31.9 mm deursnit hittebuis was 0.24 terwyl die ander hittebuise ‘n verhouding van 1 gehad het. Die hitte-vloede het gewissel van 1800-45300 W/m2. Die volgende teoretiese geformuleerde binne-hitteoordragskoëffisiënte word voorgestel vir beide vertikale sowel as nie-vertikale toepassing (LEES KORREKTE FORMULE IN VOLTEKS OPSOMMING) φ = 90° ei h = 3.4516x105Ja−0.855Ku1.344 φ = 45° ei h = 1.4796x105Ja−0.993Ku1.3 φ = 90° l l l ci l l v h x k g 1/ 3 2.05 2 4.61561 109Re 0.364 ν ρ ρ ρ − ⎡ ⎡ ⎛ ⎞⎤ ⎤ = ⎢ ⎢ ⎜ ⎟⎥ ⎥ ⎢ ⎢ ⎜ − ⎟⎥ ⎥ ⎣ ⎣ ⎝ ⎠⎦ ⎦ φ = 45° l l l ci l l v h x k g 1/ 3 1.916 2 3.7233 10 5Re 0.136 ν ρ ρ ρ − ⎡ ⎡ ⎛ ⎞⎤ ⎤ = ⎢ ⎢ ⎜ ⎟⎥ ⎥ ⎢ ⎢ ⎜ − ⎟⎥ ⎥ ⎣ ⎣ ⎝ ⎠⎦ ⎦ Die wiskundig-gemodelleerde demostrasie HPHR is geïnstalleer binne ‘n bestaande lugdroër-sisteem. Drywing van om en by 8.8 kW kon herwin word vanaf die warm-afvalvloeierstroom met ‘n massa vloei van 0.55 kg/s teen ‘n inlaattemperatuur van 51.64 °C en ‘n uitlaattemperatuur van 35.9 °C binne ‘n omgewing van 20 °C. Na aanleiding van hierdie herwinning, kan energiebesparings van tot 32.18 % verkry word. Die HPHR se installasiekoste kan binne ‘n berekende tydperk van ongeveer 3.3 jaar gedelg word deur hierdie besparing. Verdamper- tot kondensator-lengteverhouding, vloeistofvulverhouding en die oriëntasiehoek vereis verdere ondersoek, aangesien daar slegs ‘n akkuraatheid van 25 % verkry is tussen teoretiese voorspellings en praktiese metings.
Phillips, Bren Andrew. "Nano-engineering the boiling surface for optimal heat transfer rate and critical heat flux". Thesis, Massachusetts Institute of Technology, 2011. http://hdl.handle.net/1721.1/76536.
Pełny tekst źródłaCataloged from PDF version of thesis.
Includes bibliographical references (p. 130-133).
The effects on pool boiling characteristics such as critical heat flux and the heat transfer coefficient of different surface characteristics such as surface wettability, roughness, morphology, and porosity are not well understood. Layer-by-layer nanoparticle coatings were used to modify the surface of a sapphire heater to control the surface roughness, the layer thickness, and the surface chemistry. The surface was then tested in a water boiling test at atmospheric pressure while imaging the surface with high speed infrared thermography yielding a 2D time dependent temperature profile. The critical heat flux and heat transfer coefficient were enhanced by over 100% by optimizing the surface parameters. It was found that particle size of the nanoparticles in coating, the coating thickness, and the wettability of the surface have a large impact on CHF and the heat transfer coefficient. Surfaces were also patterned with hydrophobic "islands" within a hydrophilic "sea" by coupling the Layer-by-layer nanoparticle coatings with an ultraviolet ozone technique that patterned the wettability of the surface. The patterning was an attempt to increase the nucleation site density with hydrophobic dots while still maintaining a large hydrophilic region to allow for rewetting of the surface during the ebullition cycle and thus maintaining a high critical heat flux. The patterned surfaces exhibited similar critical heat fluxes and heat transfer coefficients to the surfaces that were only modified with layer-by-layer nanoparticle coatings. However, the patterned surfaces also exhibited highly preferential nucleation from the hydrophobic regions demonstrating an ability to control the nucleation site layout of a surface and opening an avenue for further study.
by Bren Andrew Phillips.
S.M.
Sivanantharaja, G. (Geethanchali). "Effect of surface roughness on heat transfer in heat exchanger". Bachelor's thesis, University of Oulu, 2017. http://urn.fi/URN:NBN:fi:oulu-201712143310.
Pełny tekst źródłaLämmönvaihdin on laite, joka siirtää lämpöä fluidista toiseen tai fluidin ja ympäristön välillä. Viimeisimpien vuosikymmenten aikana lämmönvaihtimien rooli on kasvanut lämmön talteenottoprosesseissa ja uusien energialähteiden käyttöönotossa. Lämmönvaihtimien pinnankarheudella, jolla tarkoitetaan seinämän pintakuvion korkeuden muutosta verrattuna tasaiseen pintaan, on merkittävä rooli lämmönvaihtimen tehokkuudessa. Pinnankarheuden vaikutusta lämmönsiirtoon onkin tarkasteltu useissa tutkimuksissa. Pinnankarheus voi olla osa lämmönvaihdinrakennetta tai johtua ei haluttujen materiaalien kerrostumisesta pinnalle. Tällöin puhutaan likaantumisesta, joka heikentää lämmönvaihtimen lämmönsiirtoa, lisää painehäviötä ja voi aiheuttaa korroosiota. Dimensiottomat korrelaatiot, kuten Nusseltin luku antavat tietoa pinnankarheuden aiheuttamasta vaikutuksen lämmönsiirtoon. Tässä kandidaatintyössä on tarkasteltu kirjallisuudessa esitettyjä Nusseltin luvun korrelaatioita ja niiden soveltuvuutta eri pinnankarheuden muotoihin sekä tutkittu niiden soveltuvuutta todellisen lämmönvaihtimen tapauksessa. Tästä tutkimuksessa tarkastelluista korrelaatioista Nunnerin korrelaatio soveltui parhaiten likaantuneen lämmönvaihtimen lämmönsiirron tarkasteluun. Sainin ym. korrelaatio arvioitiin soveltuvan paremmin keinotekoisen pinnankarheuden kuin likaantuneen pinnan lämmönsiirron tarkasteluun
Behbahani, Reza M. "Heat transfer and heat transfer fouling in phosphoric acid evaporators". Thesis, University of Surrey, 2003. http://epubs.surrey.ac.uk/842710/.
Pełny tekst źródłaHolzaepfel, Gregory M. "Convective Heat Transfer in Parallel Plate Heat Sinks". Ohio University / OhioLINK, 2011. http://rave.ohiolink.edu/etdc/view?acc_num=ohiou1292521397.
Pełny tekst źródłaGari, Abdullatif Abdulhadi. "Analysis of conjugate heat transfer in tube-in-block heat exchangers for some engineering applications". [Tampa, Fla] : University of South Florida, 2006. http://purl.fcla.edu/usf/dc/et/SFE0001716.
Pełny tekst źródłaBotos, Peter A. (Peter Alex). "The heat pipe injection lance /". Thesis, McGill University, 1992. http://digitool.Library.McGill.CA:80/R/?func=dbin-jump-full&object_id=56782.
Pełny tekst źródłaKsiążki na temat "Heat engineering"
Janna, William S. Engineering heat transfer. Boston, Mass: PWS Engineering, 1986.
Znajdź pełny tekst źródłaJanna, William S. Engineering heat transfer. Wyd. 3. Boca Raton: CRC Press, 2008.
Znajdź pełny tekst źródłaJanna, William S. Engineering heat transfer. Wyd. 2. Boca Raton, Fla: CRC Press, 2000.
Znajdź pełny tekst źródłaJanna, William S. Engineering heat transfer. Boston: Van Nostrand Reinhold International, 1988.
Znajdź pełny tekst źródłaRathore, M. M. Engineering heat transfer. Wyd. 2. Sudbury, Mass: Jones & Bartlett Learning, 2010.
Znajdź pełny tekst źródłaSuryanarayana, N. V. Engineering heat transfer. Minneapolis/St. Paul: West Pub. Co., 1995.
Znajdź pełny tekst źródłaSuryanarayana, N. V. Engineering heat transfer. Minneapolis/St. Paul: West Pub. Co, 1995.
Znajdź pełny tekst źródłaAnnaratone, Donatello. Engineering Heat Transfer. Berlin, Heidelberg: Springer Berlin Heidelberg, 2010. http://dx.doi.org/10.1007/978-3-642-03932-4.
Pełny tekst źródłaSimonson, J. R. Engineering Heat Transfer. London: Macmillan Education UK, 1988. http://dx.doi.org/10.1007/978-1-349-19351-6.
Pełny tekst źródłaFoumeny, E. A. Heat exchange engineering. New York: Ellis Horwood, 1991.
Znajdź pełny tekst źródłaCzęści książek na temat "Heat engineering"
Bolton, William. "Heat". W Engineering Science, 141–60. Seventh edition. | Abingdon, Oxon; New York, NY: Routledge, 2021.: Routledge, 2020. http://dx.doi.org/10.1201/9781003093596-8.
Pełny tekst źródłaBrenn, Günter. "Heat Transfer". W Mathematical Engineering, 189–237. Berlin, Heidelberg: Springer Berlin Heidelberg, 2016. http://dx.doi.org/10.1007/978-3-662-51423-8_8.
Pełny tekst źródłaField, Robert W. "Heat Transfer". W Chemical Engineering, 62–90. London: Macmillan Education UK, 1988. http://dx.doi.org/10.1007/978-1-349-09840-8_4.
Pełny tekst źródłaDash, Sanjaya K., Pitam Chandra i Abhijit Kar. "Heat Exchange". W Food Engineering, 241–64. Boca Raton: CRC Press, 2023. http://dx.doi.org/10.1201/9781003285076-19.
Pełny tekst źródłaZudin, Yuri B. "Variable Heat Transfer Coefficient (Heat Conduction Problem)". W Mathematical Engineering, 335–70. Cham: Springer International Publishing, 2023. http://dx.doi.org/10.1007/978-3-031-25167-2_13.
Pełny tekst źródłaLakshminarayanan, P. A., i Yogesh V. Aghav. "Heat Transfer". W Mechanical Engineering Series, 79–82. Dordrecht: Springer Netherlands, 2009. http://dx.doi.org/10.1007/978-90-481-3885-2_6.
Pełny tekst źródłaHoldsworth, S. Donald, i Ricardo Simpson. "Heat Transfer". W Food Engineering Series, 17–88. Cham: Springer International Publishing, 2015. http://dx.doi.org/10.1007/978-3-319-24904-9_2.
Pełny tekst źródłaLakshminarayanan, P. A., i Yogesh V. Aghav. "Heat Transfer". W Mechanical Engineering Series, 95–100. Singapore: Springer Singapore, 2022. http://dx.doi.org/10.1007/978-981-16-6742-8_6.
Pełny tekst źródłaSimonson, J. R. "Heat exchangers". W Engineering Heat Transfer, 176–207. London: Macmillan Education UK, 1988. http://dx.doi.org/10.1007/978-1-349-19351-6_12.
Pełny tekst źródłaAlmenas, K., i R. Lee. "Core Heat Removal". W Nuclear Engineering, 433–86. Berlin, Heidelberg: Springer Berlin Heidelberg, 1992. http://dx.doi.org/10.1007/978-3-642-48876-4_10.
Pełny tekst źródłaStreszczenia konferencji na temat "Heat engineering"
Takamatsu, Hiroshi, i Kosaku Kurata. "Engineering Approach to Irreversible Electroporation". W The 15th International Heat Transfer Conference. Connecticut: Begellhouse, 2014. http://dx.doi.org/10.1615/ihtc15.kn.000005.
Pełny tekst źródłaGridchin, Victor A., Vladimir M. Lubibsky i Oleg V. Lobach. "Microelectronic transducers for heat-power engineering". W 2007 International Forum on Strategic Technology. IEEE, 2007. http://dx.doi.org/10.1109/ifost.2007.4798518.
Pełny tekst źródłaLobach, Roman V., Oleg V. Lobach i Regina P. Dikareva. "Microelectronic transducer for heat-power engineering". W 2008 9th International Workshop and Tutorials on Electron Devices and Materials. IEEE, 2008. http://dx.doi.org/10.1109/sibedm.2008.4585871.
Pełny tekst źródła"Section X Heat and power engineering". W 2008 International Conference - Modern Technique and Technologies. IEEE, 2008. http://dx.doi.org/10.1109/spcmtt.2008.4897518.
Pełny tekst źródłaVilemas, Jurgis. "THERMOPHYSICS, THERMAL ENGINEERING IN LITHUANIA AND ACADEMICIAN ALGIRDAS ZUKAUSKAS". W Advances in Heat Transfer Engineering. Connecticut: Begellhouse, 2023. http://dx.doi.org/10.1615/bht4.10.
Pełny tekst źródłaMcCullough, Charles R., Scott M. Thompson i Heejin Cho. "Heat Recovery With Oscillating Heat Pipes". W ASME 2013 International Mechanical Engineering Congress and Exposition. American Society of Mechanical Engineers, 2013. http://dx.doi.org/10.1115/imece2013-66241.
Pełny tekst źródłaDrost, Kevin. "Mesoscopic Heat-Actuated Heat Pump Development". W ASME 1999 International Mechanical Engineering Congress and Exposition. American Society of Mechanical Engineers, 1999. http://dx.doi.org/10.1115/imece1999-0803.
Pełny tekst źródłaAgonafer, Damena, Juan Ibarra, Kendrick McGee, Frank Platt, Kendall Harris i Dereje Aganofer. "Heat Pipe Optimization Team: The Heat Pipe Assisted Heat Sink Project". W ASME 2004 International Mechanical Engineering Congress and Exposition. ASMEDC, 2004. http://dx.doi.org/10.1115/imece2004-62480.
Pełny tekst źródłaVasiliev, Leonard L. "APPLICATION OF HEAT PIPES IN MODERN HEAT EXCHANGERS". W Advances in Heat Transfer Engineering. Connecticut: Begellhouse, 2023. http://dx.doi.org/10.1615/bht4.100.
Pełny tekst źródłaLittle, W. A., J. G. Weisend, John Barclay, Susan Breon, Jonathan Demko, Michael DiPirro, J. Patrick Kelley i in. "HEAT TRANSFER EFFICIENCY OF KLEEMENKO CYCLE HEAT EXCHANGERS". W ADVANCES IN CRYOGENIC ENGINEERING: Transactions of the Cryogenic Engineering Conference - CEC, Vol. 52. AIP, 2008. http://dx.doi.org/10.1063/1.2908605.
Pełny tekst źródłaRaporty organizacyjne na temat "Heat engineering"
Kruger, P. Heat Extraction Project, geothermal reservoir engineering research at Stanford. Office of Scientific and Technical Information (OSTI), styczeń 1989. http://dx.doi.org/10.2172/5247981.
Pełny tekst źródłaCapell, B. M., M. G. Houts, D. I. Poston i M. Berte. Engineering design aspects of the heat-pipe power system. Office of Scientific and Technical Information (OSTI), październik 1997. http://dx.doi.org/10.2172/663582.
Pełny tekst źródłaKrajewski, R. F. Oil Heat Vent Analysis Program (OHVAP) users manual and engineering report. Office of Scientific and Technical Information (OSTI), listopad 1996. http://dx.doi.org/10.2172/420406.
Pełny tekst źródłaHendricks, Terry, i William T. Choate. Engineering Scoping Study of Thermoelectric Generator Systems for Industrial Waste Heat Recovery. Office of Scientific and Technical Information (OSTI), listopad 2006. http://dx.doi.org/10.2172/1218711.
Pełny tekst źródłaWahiduzzaman, S., i T. Morel. Effect of translucence of engineering ceramics on heat transfer in diesel engines. Office of Scientific and Technical Information (OSTI), kwiecień 1992. http://dx.doi.org/10.2172/7267573.
Pełny tekst źródłaAltseimer, J. H., i F. J. Edeskuty. A survey of geothermal process heat applications in Guatemala: An engineering survey. Office of Scientific and Technical Information (OSTI), sierpień 1988. http://dx.doi.org/10.2172/6833051.
Pełny tekst źródłaOri, Naomi, i Jason W. Reed. Engineering parthenocarpic fruit production in tomato. Israel: United States-Israel Binational Agricultural Research and Development Fund, 2021. http://dx.doi.org/10.32747/2021.8134175.bard.
Pełny tekst źródłaCarter, Michael L., Geojoe Kuruvila, Yuk Woo, Kei Y. Lau i Kevin G. Bowcutt. Hypersonic Engineering Aerothermodynamic Trajectory Tool Kit (HEAT-TK). Delivery Order 0009: Software User's Manual. Fort Belvoir, VA: Defense Technical Information Center, styczeń 2005. http://dx.doi.org/10.21236/ada455794.
Pełny tekst źródłaWahiduzzaman, S., i T. Morel. Effect of translucence of engineering ceramics on heat transfer in diesel engines. Final report. Office of Scientific and Technical Information (OSTI), kwiecień 1992. http://dx.doi.org/10.2172/10175396.
Pełny tekst źródłaWahiduzzaman, S., i T. Morel. Effect of translucence of engineering ceramics on heat transfer in diesel engines: Final report. Office of Scientific and Technical Information (OSTI), październik 1987. http://dx.doi.org/10.2172/5712724.
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