This work studies the performance of heat pipe solar collector for water heating. Experimental results are validated using numerical modeling. Homemade heat pipes with distilled water as a working fluid were used for experimental tests. Both natural and forced convective heat pipe condensing mechanisms are studied and their results are compared with conventional natural circulation solar water heating system. Cross flow and parallel flow heat exchanger were tested in forced type heat pipe condensing mechanism. Experimental and numerical results showed good agreement. Heat pipe solar collectors outperformed conventional solar collector because of their efficient heat transport method. Forced convective heat exchanger was found to give higher efficiency compared to natural convective heat pipe condensing system. However, natural convective heat pipe condensing is free from parasitic power and low system weight. It also showed appreciable system efficiency and can be further developed to be used in rural areas where grid electricity is scarce. Cross flow and parallel flow heat exchanger have been tested for forced convective heat pipe condensing mechanism and no appreciable difference was found due to higher fluid velocity in heat exchangers.

Un caloduc pulsé diphasique est un lien thermique composé d'un tube capillaire lisse sous forme de serpentin reliant un évaporateur à un condenseur, séparés par une partie adiabatique. Les conditions de température et de pression du fluide à l'intérieur du caloduc sont proches des conditions de changement de phase. De ce fait, et grâce aux dimensions capillaires du tube, le fluide se distribue en différentes parties liquide et vapeur distribuées de manière alternée. Les instabilités thermo-hydrauliques permanentes sont à l'origine d'un écoulement oscillant qui permet le transfert de chaleur de l'évaporateur jusqu'au condenseur.L'objectif du présent projet de recherche consiste à étudier le comportement thermo-hydraulique de trois caloducs cryogéniques pulsés diphasiques testés avec différents fluides cryogéniques (azote, néon et argon) pour le refroidissement d'aimants à haute température critique. De plus, un code numérique a été développé pour les futures simulations 2D des caloducs pulsés diphasiques.Au cours de ce projet de recherche, de nombreux tests expérimentaux ont été réalisés avec trois fluides cryogéniques différents: azote, néon et argon. Les résultats expérimentaux des tests avec une augmentation de puissance progressive dans l'évaporateur ont révélé des capacités de transfert thermiques très différentes en fonction du fluide, chaque fluide présentant un comportement thermo-hydraulique différent. L'état thermodynamique du fluide lors du fonctionnement stable du PHP et la phase d'assèchement (dry-out) ont été étudiés. Les différences dans le comportement des différents fluides ont été expliquées après l'analyse de leurs propriétés physiques. De plus, les taux de remplissage de fluide dans le PHP donnant les meilleures performances thermiques ont été définis. Ajouté à cela, de nombreux tests réalisés en configuration ouverte (avec le PHP connecté au volume tampon) et en configuration fermé (avec le PHP isolé du volume tampon) ont permis de conclure sur la capacité de régulation du volume tampon en cas de surpression dans le PHP. Aussi, les résultats expérimentaux des longs tests de stabilité ont permis de vérifier la stabilité du système PHP pendant des longues périodes de fonctionnement. Par ailleurs, des tests spécifiques ont été réalisés pour déterminer des conditions optimales de démarrage, l'influence de la température du condenseur dans les performances thermiques du système et l'influence du nombre de tubes en parallèle dans la capacité de transfert thermique du système. Finalement, une série de tests avec une forte puissance thermique imposée au niveau de l'évaporateur imitant une situation de quench dans un aimant supraconducteur ont données des précieuses informations sur les limites thermiques du système. Concernant les simulations numériques, un modèle a été développé avec le solveur Fluent pour des simulations dans une géométrie 2D axisymétrique en utilisant la méthode VOF. La dynamique du fluide dans un tube capillaire a été modélisée et les simulations thermiques ont permis de conclure que les instabilités thermodynamiques restent insuffisantes pour maintenir les oscillations du fluide. Ce modèle est présenté comme une nouvelle plateforme pour de futures modélisations 2D des caloducs pulsés diphasiques. / A pulsating (or oscillating) heat pipe (PHP or OHP) is a heat transfer device composed of a single capillary tube bent in many U-turns, connecting an evaporator to a condenser, separated by an adiabatic part. In the PHP, temperature and pressure conditions of the working fluid are close to phase-change conditions. Due to this and to the capillary dimensions of the tube, the fluid is distributed in alternating liquid slugs and vapor plugs. Permanent thermal instabilities in the PHP create the oscillating flow which allows the transfer of heat from one end (the evaporator) to the other (the condenser).The objective of the present work consists in characterizing the thermo-hydraulic behavior of the meter-scale horizontal cryogenic pulsating heat pipes as a cooling solution for space superconducting magnets. To this, several experiments have been conducted in a cryogenic facility containing three different horizontal pulsating heat pipes. In addition, a numerical 2D model has been proposed for future horizontal pulsating heat pipes simulations.During the research project, numerous tests have been performed using three different working fluids: nitrogen, neon and argon. From experimental results of progressive heat load tests it has been possible to compare the maximum heat load transfer capacity of the PHP with each fluid and the corresponding thermal performance. It has also been noticed that each fluid presents a specific behavior concerning the fluid oscillations. In addition, the thermodynamic state of the fluid in operating conditions and the dry-out process have been characterized. Differences between fluid's behaviors have been partly explained by analyzing the evolution of the fluid physical properties related to the movement and the heat transfer capacity. Furthermore, it has been possible to conclude about the relation between the liquid filling ratio in the PHP and its thermal performance, determining the filling ratios giving the highest thermal performances. Moreover, similar tests have been performed in open configuration (with the PHP connected to the buffer volume) and closed configuration (with the PHP isolated from the buffer volume). From this, it has been possible to conclude about the regulation made by the buffer volume in case of overpressure in the PHP. Also, experimental results from long stability tests have confirmed that these pulsating heat pipe are able to work in stable conditions during long periods as a reliable cooling system. In addition to that, specific tests have been done to determine the optimum start-tup conditions, the influence of the temperature of the condenser in the thermal performance and the influence of the number of turns in the global heat transfer capacity. A final series of tests have been achieved with a sudden extra heat load at the surface of the evaporator while the PHP is operating in stable conditions, simulating a quench event of a superconducting magnet. Experimental results gave us precious information about the transient thermal behavior and operating limits of this kind of device during transient heat loads like quench situations. Concerning the numerical part, a numerical model has been proposed for transient simulations with a pressure-based Fluent solver using the Volume of Fluid (VOF) method in a 2D axisymmetric geometry. Certain characteristics of fluid dynamics in capillary tubes have been confirmed. It has also been noticed that thermodynamic instabilities are not enough to generate the fluid oscillations in capillary tubes. Even if the 2D axisymmetric simulation is still at its early stages, several aspects of the models have been validated after analyzing the evolution of different parameters, suggesting that this kind of model can be considered as a new platform for future 2D pulsating heat pipes simulations.

Flat plate heat pipes are very efficient passive two-phase heat transport devices. Their high e'ciency and low mass are desirable in the aerospace and electronics industries. The highly competitive nature of the thermal management industry results in little awareness of the capabilities of at plate heat pipes, which has resulted in only a few applications of the technology. In the year 2000 a research and development project sponsored by Space Dynamics Laboratory was launched to investigate building carbon-based at heat pipes. The at conguration is desireable to incorporate many components onto one thermal management system. Development led to the adoption of the term "Channel Panel" because of the orthogonal grid of channels used as the capillary structure. Work to date has veried the utility and basic function of this technology but has not resulted in a standard method for the design and fabrication of channel panels. This study investigates and evaluates currently available and relevent models useful for the design of channel panels, investigates issues with fabrication, and makes suggestions for future development. Shallow pool boiling is shown to be an appropriate model for the critical heat ux of boiling in at plate heat pipes and provides a means for estimating the convective heat transfer coe'cient. Previous work by Neal Hubbard is modied and shown to accurately couple the geometry and operating limits of a channel panel. Experiments verify the analytical predictions of these models. Issues in the fabrication of channel panels are reported as well as standard procedures for cleaning and lling. The nal result is a standard method for the initial design phase of channel panel at plate heat pipes.

No description available.

No description available.

Thesis (MScEng)--Stellenbosch University, 2013. / ENGLISH ABSTRACT: High temperature heat sources are becoming an ever-increasing imperative in the process industry for the production of plastics, ammonia and fertilisers, hydrogen, coal-toliquid fuel and process heat. Currently, high temperature reactor (HTR) technology is capable of producing helium temperatures in excess of 950°C; however, at these temperatures, tritium, which is a radioactive contaminant found in the helium coolant stream, is able to diffuse though the steel retaining wall of the helium-to-steam heat exchanger. To circumvent this radioactivity problem, regulations require an intermediate heat exchange loop between the helium and the process heat streams. In this paper, the use of a uniquely designed sodium-charged heat pipe heat exchanger is considered, and has the distinct advantage of having almost zero exergy loss as it eliminates the intermediate heat exchange circuit. In order to investigate this novel heat pipe heat exchanger concept, a special intermediate-temperature (± 240°C) experimental heat pipe heat exchanger (HPHE) was designed. This experimental HPHE uses Dowtherm A as working fluid and has two glass windows to enable visual observation of the boiling and condensation two-phase flow processes. A high temperature air-burner supply simulates the high temperature stream, and the cold stream is provided by water from a constant-heat supply tank. This experimental apparatus can be used to evaluate the validity of steady-state and start-up transient theoretical models that have been developed. This paper will highlight the special design aspects of this HPHE, the theoretical model and the solution algorithm described. Experimental results will be compared with the theoretically calculated results. The theoretical model will then be used to predict the performance of a high temperature (sodium working fluid at 850°C) HPHE will be undertaken and conclusions and recommendation made. / AFRIKAANSE OPSOMMING: Hoë temperatuur hitte bronne is besig om ‘n toenemende noodsaaklikheid te raak in die proses industrie vir die vervaardiging van plastieke, ammoniak, kunsmis, waterstof, steenkool-tot-vloeibare brandstof en proses hitte. Huidige hoë temperatuur reaktor tegnologie is in staat om helium te verhit tot temperature hoër as 950°C, maar by sulke hoë temperature is die vorming van tritium, wat ‘n radioaktiewe produk is, in die helium verkoeling stroom wat deur die reaktor vloei, ‘n probleem. Die tritium is in staat om deur die staal wand van ‘n enkel fase warmte uitruiler te diffundeer. Om hierdie radioaktiewe probleem te uitoorlê, stel huidige regulasies voor dat ‘n oorgangs hitte uitruil lus gebruik raak tussen die helium en proses strome van die reaktor stelsel. In hierdie tesis word ‘n unieke natrium gevulde hitte pyp warmte uitruiler nagevors, hierdie ontwerp het die voordeel dat dit geen “exergy” verlies het omdat dit nie ‘n oorgangs hitte uitruil lus benodig nie. Hierdie unieke konsep was nagevors deur ‘n spesiale oorgangs temperatuur (± 230°C) eksperimentiële hitte pyp warmte uitruiler te ontwerp. Hierdie eksperimentiële hitte pyp warmte uitruiler gebruik Dowtherm A as oordrags medium tussen die warm en koue strome en het twee glas venters waardeur die kook en kondensasie van die oorgangs medium dop gehou kan word. ‘n Hoë temperatuur verbrander simuleer die warm stroom deur die reaktor en die koue stroom word gesimuleer deur koue water. Die eksperimentiële opstelling sal gebruik word om die tyd afhangklike en tyd onafhangklike teoretiese wiskundige modele te valideer. Hierdie tesis sal die spesiale ontwerp aspekte van die hitte pyp warmte uitruiler, teoretiese modelle en oplos algoritme te bespreek. Eksperimentiele resultate sal met die teoretiese resultate vergelyk word en dan sal die teoretiese modelle gebruik word om ‘n natrium gevulde warmte uitruiler te simuleer. Gevolgtrekkings en aanbevelings sal in die lig van die resultate verskaf word.

Thesis (MEng) -- Stellenbosch University, 2014. / ENGLISH ABSTRACT: This project investigates aspects of a novel inherently safe nuclear power steam supply system as safety is of paramount importance. The system envisaged has unique features namely: a) a two-phase flow flash-tube type natural circulating primary loop (also the secondary radioactive particle containment); b) a twophase flow thermosyphon heat pipe type heat exchanger secondary loop is used to transfer heat from the primary loop to the steam generators, thereby physically separating the two flow streams from one another; c) a natural convection air cooled condenser for the removal of the reactor’s residual heat; d) a unique core using TRISO type fuel (acting as the primary radioactive particle containment) with life of at least 8.9 years; e) a steel containment vessel acting as a tertiary radioactive product containment; f) a concrete containing structure with air vents to allow air to pass over the main steel containment vessel for cooling purposes in the case of an emergency, and for the removal of parasitic heat during operation. In particular the primary and secondary loops of the proposed system are investigated. This is done by design, construction and testing of a small scale experimental set-up of the primary and secondary loops as well as the development of theoretical models for the two loops. A literature survey focusing on nuclear technology, thermosyphon loops, natural circulating loop instabilities, heat pipes, and two-phase flow modelling is presented to give a brief overview of the technologies as well as tools used in the work undertaken. Observations of the inside flow behaviour of the primary loop experimental set-up were made possible by windows providing many insights into the inner workings, such as plume formation and geysering. The transient response of the secondary heat pipe loop start-up is also investigated. A thermal resistance theoretical model was developed for the secondary loop using heat transfer formulae from theory as well as experimentally semiempirical correlated formula. Different states of operation of the secondary loop were observed during testing with the theoretical model of the condensing regime correlating well, two-phase regime correlating acceptably and liquid regime correlating poorly to experimental results and thus were modelled using an experimentally determined overall heat transfer coefficient. The secondary loop model of the liquid regime is coupled with the primary loop theoretical model to predict the system’s performance. A homogeneous, one-dimensional, simple theoretical model for the primary loop was derived and computer simulated. The results did not compare well with experimental results for single phase flow and failed to capture the onset of two-phase flow. The assumptions of one dimensional model with a unidirectional flow, a hydrostatic pressure problem, a constant volumetric flow rate and the inability of the implementation of the code to handle expansion are noted as some of the flaws in the theoretical model. The following recommendations are made: a more advanced design of the pressuriser should be incorporated into the experiment; the secondary loop’s theoretical model should be characterised under a broader set of operating conditions; the computer program can be used as the basis for further research and implementation of alternative solution algorithms and models. / AFRIKKANSE OPSOMMING: Hierdie projek ondersoek aspekte van ’n ongewone, essensieel veilige kernkrag stoomtoevoer-stelsel, omdat veiligheid van kardinale belang is. Die stelsel wat voorgestel is, het unieke eienskappe, naamlik: a) ’n twee-fasevloei flits-buistipe natuurlik sirkulerende primêre lus (wat ook die sekondêre inperking van radioaktiewe materiaal bevat); b) ’n twee-fasevloei termo-heweleffek sekondêre lus hitte-pyp hitte-uitruiler word gebruik om die hitte vanaf die primêre lus oor te dra na die stoomkragopwekkers en daardeur word die twee strome se vloei fisies geskei van mekaar; c) ’n natuurlike konveksie lugverkoelde kondensor word gebruik vir die verwydering van die reaktors se oortollige hitte; d) ’n unieke kern gebruik TRISO-tipe brandstof (wat as die primêre inperking van radioaktiewe materiaal optree) met ’n lewe van minstens 8.9 jaar; e) ’n inperkingshouer van staal wat optree as ’n tersiêre radioaktiewe produkhouer; f) ’n betonstruktuur met lugventilasie om toe te laat dat lug oor die hoof staalhouer vloei vir verkoeling in ’n noodgeval, en vir die verwydering van parasitiese hitte tydens werking. Hoofsaaklik word die primêre en sekondêre lusse van die voorgestelde stelsel ondersoek. Dit word gedoen deur die ontwerp, konstruksie en die toets van ’n eksperimentele opstelling van die primêre en sekondêre lusse op klein skaal, sowel as die ontwikkeling van teoretiese modelle vir die twee lusse. ’n Literatuurstudie wat fokus op kerntegnologie, termo-heweleffeklusse, natuurlik sirkulerende lus instabiliteit, hitte-pype, en twee-fase vloeimodellering word aangebied om ’n kort oorsig te gee van die tegnologie, sowel as gereedskap gebruik in die werk wat onderneem is. Om die interne vloeigedrag van die primêre lus se eksperimentele opstelling waar te neem, word daar gebruik gemaak van vensters wat dien as ’n manier om die innerlike werking van die proses soos pluimvorming en die kook van die water in die warmwaterkolom te toon. Die oorgangsreaksie van die sekondêre hittepyplus aanvangs is ook ondersoek. ’n Teoretiese termiese weerstandmodel is ontwikkel vir die sekondêre lus met behulp van hitte-oordragformules waarvoor hitte-oordragteorie gebruik is, wat met eksperimentele semi-empiriese formules gekorreleer is. Verskillende toestande van die sekondêre lus se werking is waargeneem gedurende die toetse. Die teoretiese model het goed met die kondensasiestaat gekorreleer, terwyl by die twee-fasewerkswyse aanvaarbare korrellasies aangetref is en die uiteindelike vloeitoestand swakker gekorrelleer het met eksperimentele resultate en dus gemodelleer is met behulp van die NTU-effektiwiteitsmetode. Die sekondêre lusmodel van die vloeistoftoestand is gekoppel met die primêre lus teoretiese model om die werking van die stelsels te voorspel. ’n Homogene een-dimensionele eenvoudige teoretiese model van die primêre lus is afgelei en ’n rekenaar simulasie is uitgevoer. Die resultate vergelyk nie goed met die eksperimentele resultate vir enkelfasevloei en kon nie die aanvang van twee-fasevloei beskryf nie. Die aannemings van ’n een-dimensionele model met eenrigting vloei, ’n hidrostatiese druk probleem, ’n konstant volumetries vloeitempo en die onvermoë van die implementering van die kode om uitbreiding te hanteer is bekend as ’n paar van die foute in die teoretiese model. Die volgende aanbevelings word gemaak: ’n meer gevorderde ontwerp van drukreëlaar moet in die eksperiment ingesluit word; die sekondêre lus se teoretiese model moet gekenmerk word onder ’n wyer stel bedryfsomstandighede, en die rekenaar program kan gebruik word as die basis vir verdere navorsing en die implementering van alternatiewe algoritmes en modelle.

O objetivo deste trabalho consiste na análise teórica e experimental do desempenho térmico de dois arranjos de micro tubos de calor. Os arranjos diferem entre si pelo material base de fabricação, que são Acrilonitrila Butadieno Estireno (ABS) e latão, pelo número de canais e pelas dimensões. O fluido de trabalho utilizado foi R134a. A literatura indica micro tubos de calor como soluções proeminentes e de destaque para resfriamento de micro sistemas. Estes dispositivos podem ser adaptados a diferentes condições térmicas através da mudança de fluidos de trabalho, geometrias e materiais base do trocador. O estudo teórico foi baseado no modelo de circuitos térmicos proposto no presente trabalho, que visa calcular indicadores de desempenho térmico, sendo condutividade térmica efetiva e resistência térmica equivalente dos micro tubos de calor a partir das temperaturas obtidas experimentalmente. O estudo experimental foi baseado em obter distribuições de temperaturas dos dispositivos propostos sob diferentes condições de trabalho, variando-se a fração de enchimento de fluido de trabalho, inclinação e temperatura do condensador. Os resultados obtidos para o arranjo de micro tubos de calor em latão demonstrou uma razão de aumento de até 1482% na capacidade de transporte de calor, enquanto que o arranjo de micro tubos de calor em ABS apresentou uma razão de aumento de 247%. Os melhores desempenhos de ambos os casos foram observados para ângulos positivos com baixas frações de enchimento. / The purpose of this work is the theoretical and experimental study on the thermal performance of two micro heat pipes arrays. The differences between the arrays are the base substrate, which are Acrylonitrile Butadiene Styrene (ABS) and brass, the number of channels and their dimensions. The working fluid used was R134a. Previous works indicate micro heat pipes as prominent solutions for the cooling of micro systems. These devices can be adapted to different thermal conditions by changing the working fluids, geometries and base materials of the heat exchanger. The theoretical study was based on the thermal circuits model presented in this work, that aims on computing thermal performance indicators, such as the effective thermal conductivities and the equivalent thermal resistances of the micro heat pipes from the temperatures obtained experimentally. The experimental study was based on obtaining temperature distributions of the micro heat pipes under different working conditions, by varying the working fluid filling ratio, tilt angle and the temperature of the cooling water at the condenser. The results obtained for the brass micro heat pipe array showed a performance ratio increase up to 1482% in heat transfer capacity, while the ABS micro heat pipe array showed a performance ratio increase of 247%. The best performance for both cases were observed for positive tilt angles with low working fluid filling ratios.

O objetivo deste trabalho consiste na análise teórica e experimental do desempenho térmico de dois arranjos de micro tubos de calor. Os arranjos diferem entre si pelo material base de fabricação, que são Acrilonitrila Butadieno Estireno (ABS) e latão, pelo número de canais e pelas dimensões. O fluido de trabalho utilizado foi R134a. A literatura indica micro tubos de calor como soluções proeminentes e de destaque para resfriamento de micro sistemas. Estes dispositivos podem ser adaptados a diferentes condições térmicas através da mudança de fluidos de trabalho, geometrias e materiais base do trocador. O estudo teórico foi baseado no modelo de circuitos térmicos proposto no presente trabalho, que visa calcular indicadores de desempenho térmico, sendo condutividade térmica efetiva e resistência térmica equivalente dos micro tubos de calor a partir das temperaturas obtidas experimentalmente. O estudo experimental foi baseado em obter distribuições de temperaturas dos dispositivos propostos sob diferentes condições de trabalho, variando-se a fração de enchimento de fluido de trabalho, inclinação e temperatura do condensador. Os resultados obtidos para o arranjo de micro tubos de calor em latão demonstrou uma razão de aumento de até 1482% na capacidade de transporte de calor, enquanto que o arranjo de micro tubos de calor em ABS apresentou uma razão de aumento de 247%. Os melhores desempenhos de ambos os casos foram observados para ângulos positivos com baixas frações de enchimento. / The purpose of this work is the theoretical and experimental study on the thermal performance of two micro heat pipes arrays. The differences between the arrays are the base substrate, which are Acrylonitrile Butadiene Styrene (ABS) and brass, the number of channels and their dimensions. The working fluid used was R134a. Previous works indicate micro heat pipes as prominent solutions for the cooling of micro systems. These devices can be adapted to different thermal conditions by changing the working fluids, geometries and base materials of the heat exchanger. The theoretical study was based on the thermal circuits model presented in this work, that aims on computing thermal performance indicators, such as the effective thermal conductivities and the equivalent thermal resistances of the micro heat pipes from the temperatures obtained experimentally. The experimental study was based on obtaining temperature distributions of the micro heat pipes under different working conditions, by varying the working fluid filling ratio, tilt angle and the temperature of the cooling water at the condenser. The results obtained for the brass micro heat pipe array showed a performance ratio increase up to 1482% in heat transfer capacity, while the ABS micro heat pipe array showed a performance ratio increase of 247%. The best performance for both cases were observed for positive tilt angles with low working fluid filling ratios.

Interest in the use of heat pipe technology for heat recovery and energy saving in a vast range of engineering applications has been on the rise in recent years. Heat pipes are playing a more important role in many industrial applications, especially in increasing energy savings in commercial applications and improving the thermal performance of heat exchangers. Computational techniques play an important role in solving complex flow problems for a large number of engineering applications due to their universality, flexibility, accuracy and efficiency. However, up to now, computational studies on heat pipes are still at an early stage due to the complexity of multiphase flow characteristics and heat and mass transfer phase changes. Therefore, the main objective of this study is to develop a CFD modelling that includes the complex physical phenomena of both the heat transfer processes of evaporation and condensation and the mass transfer process of phase change during the pool boiling and film condensation. In this thesis, two novel numerical models were developed in ANSYS FLUENT. In the first, a two-dimensional CFD model was developed to visualise the two-phase flow and the evaporation, condensation and heat transfer phenomena during the operation of a wickless heat pipe, that otherwise could not be visualised by empirical or experimental work. An in-house code was developed using user-defined functions (UDFs) to enhance the ability of FLUENT to simulate the phase change occurring inside the heat pipe. Three different fluids, water, R134a and R404a, were selected as the working fluids of the investigated wickless heat pipe. The cooling system of the condenser section was simulated separately as a three-dimensional CFD model of a parallel-flow double pipe heat exchanger to model the heat transfer across the condenser section's heat exchanger and predict the heat transfer coefficients. The overall effective thermal resistance along with the temperature profile along the wickless heat pipe have been investigated. An experimental apparatus was built to carry out a thermal performance investigation on a typical wickless heat pipe for the purpose of validating the CFD simulation. A theoretical model based on empirical correlations was developed to predict the heat transfer thermal resistances in the evaporator and the condenser section. The second model was developed to combine the two-dimensional CFD simulation of the wickless heat pipe and the three-dimensional CFD simulation of the condenser section's heat exchanger to simulate the two-phase flow phenomena of boiling and condensation and the cooling system of the condenser section through a comprehensive three-dimensional CFD model of a wickless heat pipe. Two fluids, water and R134a, were selected as the working fluids of the investigated wickless heat pipe. This model was validated using a transparent glass wickless heat pipe to visualise the phenomena of pool boiling and comparing the results with the three-dimensional CFD flow visualisation. This study demonstrated that the proposed CFD models of a wickless heat pipe can successfully reproduce the complex physical phenomena of both the heat transfer process of evaporation and condensation and the mass transfer process of phase change during the pool boiling that takes place in the evaporator section and the filmwise condensation that takes place in the condenser section. The CFD simulation was successful in modelling and visualising the multiphase flow characteristics for water, R134a and R404a, emphasising the difference in pool boiling behaviour between these working fluids. The CFD simulation results were compared with experimental measurements, with good agreement obtained between predicted temperature profiles and experimental temperature data.