Fuel let-down heat exchanger.

"Work performed under contract no. W-7405-Eng.-26."

Performance of Plate Type Heat Exchanger as Ammonia Condenser

In this study, I experimentally analyzed the performance of a commercial semi-welded plate type heat exchanger (PHE) for use with ammonia systems. I determined performance parameters such as overall heat transfer coefficient, capacity, and pressure drop of the semi-welded PHE. This was analyzed by varying different parameters which demonstrated changes in overall heat transfer coefficient, capacity, and pressure drop. Both water and ammonia flow rates to the semi-welded PHE were varied independently, and analyzed in order to understand how changes in flow rates affected performance. Inlet water temperature was also varied, in order to understand how raising condenser water inlet temperature would affect performance. Finally, pressure drop was monitored to better understand the performance limitations of the semi-welded PHE. Testing of the semi-welded will give insight as to the performance of the semi-welded PHE in a potential ocean thermal energy conversion system, and whether the semi-welded PHE is a viable choice for use as an ammonia condenser.

Second law analysis and simulation techniques for the energy optimization of buildings

The research activity described in this thesis is focused mainly on the study of finite-element techniques applied to thermo-fluid dynamic problems of plant components and on the study of dynamic simulation techniques applied to integrated building design in order to enhance the energy performance of the building. The first part of this doctorate thesis is a broad dissertation on second law analysis of thermodynamic processes with the purpose of including the issue of the energy efficiency of buildings within a wider cultural context which is usually not considered by professionals in the energy sector. In particular, the first chapter includes, a rigorous scheme for the deduction of the expressions for molar exergy and molar flow exergy of pure chemical fuels. The study shows that molar exergy and molar flow exergy coincide when the temperature and pressure of the fuel are equal to those of the environment in which the combustion reaction takes place. A simple method to determine the Gibbs free energy for non-standard values of the temperature and pressure of the environment is then clarified. For hydrogen, carbon dioxide, and several hydrocarbons, the dependence of the molar exergy on the temperature and relative humidity of the environment is reported, together with an evaluation of molar exergy and molar flow exergy when the temperature and pressure of the fuel are different from those of the environment. As an application of second law analysis, a comparison of the thermodynamic efficiency of a condensing boiler and of a heat pump is also reported. The second chapter presents a study of borehole heat exchangers, that is, a polyethylene piping network buried in the soil which allows a ground-coupled heat pump to exchange heat with the ground. After a brief overview of low-enthalpy geothermal plants, an apparatus designed and assembled by the author to carry out thermal response tests is presented. Data obtained by means of in situ thermal response tests are reported and evaluated by means of a finite-element simulation method, implemented through the software package COMSOL Multyphysics. The simulation method allows the determination of the precise value of the effective thermal properties of the ground and of the grout, which are essential for the design of borehole heat exchangers. In addition to the study of a single plant component, namely the borehole heat exchanger, in the third chapter is presented a thorough process for the plant design of a zero carbon building complex. The plant is composed of: 1) a ground-coupled heat pump system for space heating and cooling, with electricity supplied by photovoltaic solar collectors; 2) air dehumidifiers; 3) thermal solar collectors to match 70% of domestic hot water energy use, and a wood pellet boiler for the remaining domestic hot water energy use and for exceptional winter peaks. This chapter includes the design methodology adopted: 1) dynamic simulation of the building complex with the software package TRNSYS for evaluating the energy requirements of the building complex; 2) ground-coupled heat pumps modelled by means of TRNSYS; and 3) evaluation of the total length of the borehole heat exchanger by an iterative method developed by the author. An economic feasibility and an exergy analysis of the proposed plant, compared with two other plants, are reported. The exergy analysis was performed by considering the embodied energy of the components of each plant and the exergy loss during the functioning of the plants.

Analisi della stabilità dei risultati dei test di risposta termica: prove in campo, confronto e analisi critica per diversi metodi di esecuzione e modellizzazione

Il Test di Risposta Termica (Thermal Response Test-TRT) (Mogenson,1983) è il test esistente con il più alto grado di accuratezza per la caratterizzazione del reservoir geotermico superficiale. Il test consiste in una simulazione in situ del funzionamento di un sistema a circuito chiuso di sfruttamento dell’energia geotermica, per un periodo limitato di tempo, attraverso l’iniezione o estrazione di calore a potenza costante all’interno del geo-scambiatore (Borehole Heat Exchanger-BHE). Dall’analisi della variazione delle temperature del fluido circolante, è possibile avere una stima delle proprietà termiche medie del volume del reservoir geotermico interessato dal test. Le grandezze principali per la caratterizzazione di un serbatoio geotermico sono la conduttività termica (λ), la capacità termica volumetrica (c), la temperatura indisturbata del suolo (Tg) e la resistenza termica del pozzo (Rb); la loro determinazione è necessaria per il corretto progettazione degli geo-scambiatori. I risultati del TRT sono tuttavia sensibili alle condizioni al contorno spazio-temporali quali ad es.: variazione della temperatura del terreno, movimento d’acqua di falda, condizioni metereologiche, eventi stagionali, ecc. Questo lavoro vuole: i) introdurre uno studio sui problemi di caratterizzazione del reservoir geotermico superficiale, in particolare analizzando l’effetto che il movimento d’acqua di falda ha sui parametri termici; ii) analizzare la sensitività dei risultati del test alle variabilità dei parametri caratteristici del funzionamento delle attrezzature. Parte del lavoro della mia tesi è stata svolta in azienda per un periodo di 4 mesi presso la “Groenholland Geo Energy systems” che ha sede ad Amsterdam in Olanda. Tre diversi esperimenti sono stati realizzati sullo stesso sito (stratigrafia nota del terreno: argilla, sabbia fine e sabbia grossa) usando una sonda profonda 30 metri e diversi pozzi per l’estrazione d’acqua e per monitorare gli effetti in prossimità del geo scambiatore. I risultati degli esperimenti sono stati molto diversi tra di loro, non solo in termini di dati registrati (temperature del fluido termovettore), ma in termini dei valori dei parametri ottenuti elaborando i dati. In particolare non è sufficiente adottare il modello classico della sorgente lineare infinita (Infinite Line Source Solution- ILS) (Ingersoll and Plass, 1948), il quale descrive il trasferimento di calore per conduzione in un mezzo omogeneo indefinito a temperatura costante. Infatti, lo scambio di calore avviene anche tramite convezione causata dal movimento d’acqua di falda, non identificabile mediante gli approcci classici tipo CUSUM test (Cumulative Sum test) (Brown e altri,1975) Lo studio della tesi vuole dare un quadro di riferimento per correlare la variabilità dei risultati con la variabilità delle condizioni al contorno. L’analisi integra le metodologie classiche (ILS) con un approccio geostatistico utile a comprendere i fenomeni e fluttuazioni che caratterizzano il test. Lo studio delle principali variabili e parametri del test, quali temperatura in ingresso e uscita del fluido termovettore, portata del fluido e potenza iniettata o estratta, è stato sviluppato mediante: il variogramma temporale, ovvero la semivarianza dell’accrescimento, che esprime il tipo di autocorrelazione temporale della variabile in esame; la covarianza incrociata temporale, ovvero la covarianza fra due variabili del sistema, che ne definisce quantitativamente il grado di correlazione in funzionamento del loro sfasamento temporale. L’approccio geostatistico proposto considera la temperatura del fluido Tf come una funzione aleatoria (FA) non stazionaria nel tempo (Chiles, 1999), il cui trend è formalmente definito, ma deve essere identificato numericamente. Si considera quindi un classico modello a residuo; in cui la FA è modellizzata come la somma di un termine deterministico, la media (il valore atteso) m(t),coincidente col modello descritto dalla teoria della sorgente lineare infinità, e di un termine aleatorio, la fluttuazione, Y(t). Le variabili portata e potenza sono invece considerate delle funzioni aleatorie stazionarie nel tempo, ovvero a media costante. Da questo studio di Tesi si sono raggiunte delle conclusioni molto importanti per lo studio del TRT: Confronto tra gli esperimenti in estrazione di calore, con e senza movimento d’acqua di falda: si studia l’effetto indotto dalla falda sul TRT. E’ possibile caratterizzare quantitativamente l’incremento della conducibilità termica equivalente legata a fenomeni convettivi dovuti al movimento d’acqua di falda. Inoltre, i variogrammi sperimentali evidenziano periodicità simili nei due casi e legate al funzionamento della pompa di calore e della componentistica associata ed alla circolazione del fluido termovettore all’interno della sonda. Tuttavia, la componente advettiva ha un effetto di smorzamento sulle piccole periodicità dei variogrammi, ma di aumento dell’ampiezza delle periodicità maggiori a causa del funzionamento della pompa di calore che deve fornire maggiore energia al sistema per bilanciare le dispersioni dovute al movimento d’acqua di falda. Confronto fra estrazione ed iniezione di calore, con movimento d’acqua di falda: si studia la significatività dei risultati nei due casi. L’analisi delle variografie evidenzia significative differenze nella struttura dei variogrammi sperimentali. In particolare, nel test con iniezione di calore i variogrammi sperimentali delle temperature hanno valori sistematicamente inferiori, circostanza che assicura una migliore precisione nella stima dei parametri termici. Quindi eseguire il TRT in iniezione di calore risulta più preciso. Dall’analisi dei variogrammi sperimentali delle singole variabili quali temperatura del fluido in ingresso e uscita all’interno del geoscambiatore è stato confermato il fenomeno di smorzamento delle oscillazioni da parte del terreno. Dall’analisi delle singole variabili del test (temperature, potenza, portata) è stata confermata l’indipendenza temporale fra portate e temperature. Ciò è evidenziato dalle diverse strutture dei variogrammi diretti e dalle covarianze incrociate prossime a zero. Mediante correlogrami è stato dimostrato la possibilità di calcolare il tempo impiegato dal fluido termovettore per circolare all’interno della sonda. L’analisi geostatistica ha permesso quindi di studiare in dettaglio la sensitività dei risultati del TRT alle diverse condizioni al contorno, quelle legate al reservoir e quelle legate al funzionamento delle attrezzature

Bestimmung thermischer Untergrundparameter in Erdwärmesondenfeldern und Evaluierung tiefenaufgelöster Thermal-Response-Tests durch thermohydraulische Modellierungen

Die oberflächennahe Geothermie leistet im Bereich der Nutzung regenerativer Wärme einen wichtigen Beitrag zum Klima- und Umweltschutz. Um die technische Nutzung oberflächennaher Geothermie zu optimieren, ist die Kenntnis der Beschaffenheit des geologischen Untergrundes ausschlaggebend. Die vorliegende Dissertation befasst sich mit der Bestimmung verschiedener Untergrundparameter an einem Erdwärmesondenfeld. Es wurden Untersuchungen zur Bestimmung der Wärmeleitfähigkeit wie der enhanced Thermal Response Test (eTRT), sowie eine Untergrund-Temperaturüberwachung im ersten Betriebsjahr durchgeführt. Die Überwachung zeigte keine gegenseitige Beeinflussung einzelner Sonden. Ein Vergleich zwischen dem geplanten und dem tatsächlichem Wärmebedarf des ersten Betriebsjahres ergab eine Abweichung von ca. 35%. Dies zeigt, dass die Nutzungsparameter der Anlage deren Effizienz maßgeblich beeinflussen können. Der am Beispielobjekt praktisch durchgeführte eTRT wurde mittels numerischer Modellierung auf seine Reproduzierbarkeit hin überprüft. Bei einem rein konduktiven Wärmetransport im Untergrund betrug die maximale Abweichung der Messung selbst unter ungünstigen Bedingungen lediglich ca. 6% vom zu erwartenden Wert. Die Detektion von grundwasserdurchflossenen Schichten ist in den Modellen ebenfalls gut abbildbar. Problematisch bleibt die hohe Abhängigkeit des Tests von einer konstanten Wärmezufuhr. Lediglich die Bestimmung der Wärmeleitfähigkeit über das Relaxationsverhalten des Untergrundes liefert bei Wärmeeintragsschwankungen hinreichend genaue Ergebnisse. Die mathematische Nachbearbeitung von fehlerhaften Temperaturkurven bietet einen Einstiegspunkt für weiterführende Forschung.

Numerical simulations of particle deposition in metal foam heat exchangers

Australia is a high-potential country for geothermal power with reserves currently estimated in the tens of millions of petajoules, enough to power the nation for at least 1000 years at current usage. However, these resources are mainly located in isolated arid regions where water is scarce. Therefore, wet cooling systems for geothermal plants in Australia are the least attractive solution and thus air-cooled heat exchangers are preferred. In order to increase the efficiency of such heat exchangers, metal foams have been used. One issue raised by this solution is the fouling caused by dust deposition. In this case, the heat transfer characteristics of the metal foam heat exchanger can dramatically deteriorate. Exploring the particle deposition property in the metal foam exchanger becomes crucial. This paper is a numerical investigation aimed to address this issue. Two dimensional (2D) numerical simulations of a standard one-row tube bundle wrapped with metal foam in cross-flow are performed and highlight preferential particle deposition areas.

Numerical simulations of particle deposition in metal foam heat exchangers

Australia is a high potential country for geothermal power with reserves currently estimated in the tens of millions of petajoules, enough to power the nation for at least 1000 years at current usage.However, these resources are mainly located in isolated arid regions where water is scarce. Therefore, wet cooling systems for geothermal plants in Australia are the least attractive solution and thus air-cooled heat exchangers are preferred. In order to increase the efficiency of such heat exchangers, metal foams have been used. One issue raised by this solution is the fouling caused by dust deposition. In this case, the heat transfer characteristics of the metal foam heat exchanger can dramatically deteriorate. Exploring the particle deposition property in the metal foam exchanger becomes crucial. This paper is a numerical investigation aimed to address this issue. Two-dimensional(2D numerical simulations of a standard one-row tube bundle wrapped with metal foam in cross-flow are performed and highlight preferential particle deposition areas.

Fouling of waste heat recovery : numerical and experimental results

Numerical results are presented to investigate the performance of a partly-filled porous heat exchanger for waste heat recovery units. A parametric study was conducted to investigate the effects of inlet velocity and porous block height on the pressure drop of the heat exchanger. The focus of this work is on modelling the interface of a porous and non-porous region. As such, numerical simulation of the problem is conducted along with hot-wire measurements to better understand the physics of the problem. Results from the two sources are then compared to existing theoretical predictions available in the literature which are unable to predict the existence of two separation regions before and after the porous block. More interestingly, a non-uniform interface velocity was observed along the streamwise direction based on both numerical and experimental data.

Synthesis of Cost-Optimal Shell-and-Tube Heat Exchangers

Synthesis of cost-optimal shell-and-tube heat exchangers is a difficult task since it involves a large number of parameters. An attempt is made in this article to simplify the process of choosing the parameter values that will minimize the cost of any heat exchanger satisfying a given heat duty and a particular set of constraints. The simplification is based on decoupling of the geometric and the thermal aspects of the problem. The concept of curves for cost-optimal design is introduced and is shown to simplify the synthesis process for shell-and-tube heat exchangers.

Design options reduce exchanger cost

Heat exchanger design is a complex task involving the selection of a large number of interdependent design parameters. There are no established general techniques for optimizing the design, though a few earlier attempts provide computer software based on gradient methods, case study methods, etc. The authors felt that it would be useful to determine the nature of the optimal and near-optimal feasible designs to devise an optimization technique. Therefore, in this article they have obtained a large number of feasible designs of shell and tube heat exchangers, intended to perform a given heat duty, by an exhaustive search method. They have studied how their capital and operating costs varied. The study reveals several interesting aspects of the dependence of capital and total costs on various design parameters. The authors considered a typical shell and tube heat exchanger used in an oil refinery. Its heat duty, inlet temperature and other details are given.

Constrained optimization of heat exchangers

Optimizing a shell and tube heat exchanger for a given duty is an important and relatively difficult task. There is a need for a simple, general and reliable method for realizing this task. The authors present here one such method for optimizing single phase shell-and-tube heat exchangers with given geometric and thermohydraulic constraints. They discuss the problem in detail. Then they introduce a basic algorithm for optimizing the exchanger. This algorithm is based on data from an earlier study of a large collection of feasible designs generated for different process specifications. The algorithm ensures a near-optimal design satisfying the given heat duty and geometric constraints. The authors also provide several sub-algorithms to satisfy imposed velocity limitations. They illustrate how useful these sub-algorithms are with several examples where the exchanger weight is minimized.

Convective heat dissipation with lattice-frame materials

This paper presents experimental results on heat transfer and pressure drop for a compact heat sink made of fully triangulated, lightweight (porosity∼0.938), aluminum lattice-frame materials (LFMs). Due to the inherent structural anisotropy of the LFMs, two mutually perpendicular orientations were selected for the measurements. Constant heat flux was applied to the heat sink under steady state conditions, and dissipated by forced air convection. The experimental data were compared with those predicted from an analytical model based on fin analogy. The experimental results revealed that pressure drop is strongly dependent upon the orientation of the structure, due mainly to the flow blockage effect. For heat transfer measurements, typical local temperature distributions on the substrate under constant heat flux conditions were captured with infrared camera. The thermal behavior of LFMs was found to follow closely that of cylinder banks, with early transition Reynolds number (based on strut diameter) equal to about 300. The Nusselt number prediction from the fin-analogy correlates well with experimental measurements, except at low Reynolds numbers where a slightly underestimation is observed. Comparisons with empty channels and commonly used heat exchanger media show that the present LFM heat sink can remove heat approximately seven times more efficient than an empty channel and as efficient as a bank of cylinders at the same porosity level. The aluminum LFMs are extremely stiff and strong, making them ideal candidates for multifunctional structures requiring both heat dissipation and mechanical load carrying capabilities. © 2003 Elsevier Ltd. All rights reserved.

Risk based lifetime costs assessment of a ground source heat pump (GSHP) system design: Methodology and case study

Space heating accounts for a large portion of the world's carbon dioxide emissions. Ground Source Heat Pumps (GSHPs) are a technology which can reduce carbon emissions from heating and cooling. GSHP system performance is however highly sensitive to deviation from design values of the actual annual energy extraction/rejection rates from/to the ground. In order to prevent failure and/or performance deterioration of GSHP systems it is possible to incorporate a safety factor in the design of the GSHP by over-sizing the ground heat exchanger (GHE). A methodology to evaluate the financial risk involved in over-sizing the GHE is proposed is this paper. A probability based approach is used to evaluate the economic feasibility of a hypothetical full-size GSHP system as compared to four alternative Heating Ventilation and Air Conditioning (HVAC) system configurations. The model of the GSHP system is developed in the TRNSYS energy simulation platform and calibrated with data from an actual hybrid GSHP system installed in the Department of Earth Science, University of Oxford, UK. Results of the analysis show that potential savings from a full-size GSHP system largely depend on projected HVAC system efficiencies and gas and electricity prices. Results of the risk analysis also suggest that a full-size GSHP with auxiliary back up is potentially the most economical system configuration. © 2012 Elsevier Ltd.