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A drilling operation leads to thermal disturbances in the near-wellbore stress, which is an important cause of many undesired incidents in well drilling. A major cause of this thermal disturbance is the temperature difference between the drilling fluid and the downhole formation. It is critical for drilling engineers to understand this thermal impact to optimize their drilling plans. This thesis develops a numerical model using partially coupled thermoporoelasticity to study the effects of the temperature difference between the drilling fluid and formation in a drilling operation. This study focuses on the thermal impacts at the bit/formation interface. The model applies the finite-difference method for the pore pressure and temperature solutions, and the finite-element method for the deformation and stress solutions. However, the model also provides the thermoporoelastic effects at the wellbore wall, which involves wellbore fractures and wellbore instability. The simulation results show pronounced effects of the drilling fluid temperature on near-wellbore stresses. At the bottomhole area, a cool drilling fluid reduces the radial and tangential effective stresses in formation, whereas the vertical effective stress increases. The outcome is a possible enhancement in the drilling rate of the drill bit. At the wellbore wall, the cool drilling fluid reduces the vertical and tangential effective stresses but raises the radial effective stress. The result is a lower wellbore fracture gradient; however, it benefits formation stability and prevents wellbore collapse. Conversely, the simulation gives opposite induced stress results to the cooling cases when the drilling fluid is hotter than the formation.

Analysis of the drilling fluid temperature in a circulating well is the main objective of this study. Initially, an analytical temperature distribution model, which utilizes basic energy conservation principle, is presented for this purpose. A computer program is written in order to easily implement this model to different cases. Variables that have significant effect on temperature profile are observed. Since the verification of the analytical model is not probable for many cases, a computer program (ANSYS) that uses finite element method is employed to simulate different well conditions. Three different wells were modeled by using rectangular FLOTRAN CFD element that has four nodes. Maximum drilling fluid temperature data corresponding to significant variables is collectedfrom these models. This data is then used to develop an empirical correlation in order to determine maximum drilling fluid temperature. The proposed empirical correlation can estimate the temperature distribution within the wellbore with an average error of less than 16%, and maximum drilling fluid temperature with an average error of less than 7 %.

Made available in DSpace on 2016-08-17T14:53:11Z (GMT). No. of bitstreams: 1 Shirlen Viana Leal.pdf: 556717 bytes, checksum: 0c051baae450dc752c45ceb9e82ddd19 (MD5) Previous issue date: 2010-06-04 / Coordenação de Aperfeiçoamento de Pessoal de Nível Superior / The thermoresistive - based hot-wire anemometer operating at a controlled temperature is a classical architecture that is vastly found in the literature. Nevertheless, this architecture may present a problem due to dynamic range variation of its output voltage for significant variation of the fluid temperature. In this work, the classical architecture is revisited and the influence of the fluid temperature is verified. An alternative architecture of a controlled temperature anemometer implemented with a controlled current source with automatic compensation of the fluid temperature influence on the output voltage dynamic range is proposed. Simulations of the classical architecture and of the proposed system using the parameters from a commercial sensor are presented and compared. Results show that the output voltage dynamic range for the proposed architecture employing the automatic compensation is practically constant. / O anemômetro de fio quente, baseado em sensor termo-resistivo operando à temperatura constante, é uma arquitetura clássica que é vastamente encontrada na bibliografia. Todavia, esta arquitetura pode apresentar um problema devido à variação da faixa dinâmica de sua tensão de saída para variações significativas da temperatura do fluido. Neste trabalho, a arquitetura clássica foi revisada e a influência da temperatura do fluido foi observada. Uma arquitetura alternativa de um anemômetro à temperatura controlada, implementada com uma fonte de corrente com compensação automática da influência da temperatura do fluido na faixa dinâmica da tensão de saída é proposta. Simulações da arquitetura clássica e do sistema proposto usando parâmetros de um sensor comercial são apresentadas e comparadas. Concluise, a partir dos resultados obtidos, que a faixa dinâmica da tensão de saída para a arquitetura proposta, empregando a compensação automática, é praticamente constante.

This dissertation describes the development of an intelligent non-invasive thermal energy flow rate sensor for laminar and turbulent pipe flows. Energy flow rate is the thermal energy that is carried by a fluid, for example, in a pipe to heat or cool a space in a building. It can be measured by an energy flow rate sensor which consists of a volume flow rate meter and supply and return fluid temperature sensors to bill the users for their energy usage. A non-invasive, low-cost, and easy to install thermal energy flow rate sensor based on thermal interrogation transient heat flux and temperature measurements has been developed to measure fluid velocity and fluid temperature in pipes. This sensor can be used for different pipe diameters, different pipe materials, and different viscous fluids. The transient measurements are made on the outer surface of a pipe by using a heat flux sensor and a thin-film thermocouple which are covered by a thin-film heater. A one-dimensional transient thermal model is applied before and during activation of the external heater along with a parameter estimation code to provide estimates of the fluid heat transfer coefficient and apparent thermal resistance between the thermocouple and the pipe surface. This dissertation contributes to the sensor's development in three ways. First, a new design is developed by using a single layer of Kapton tape with an adhesive (dielectric material) between the thermocouple foils and the pipe wall to isolate the thermocouple electrically from the pipe surface. This new design gives accurate and reliable estimates of the internal mean fluid temperature without environmental interference. Second, this new sensor design is tested for turbulent pipe flows with two different pipe diameters ( = 25.4 mm and = 12.7 mm) and two different viscous fluids (diesel oil and water). Experiments are completed over a large range of fluid velocity from 0.2 m/s to 5.5 m/s and a range of fluid temperature from 20 ℃ to 50 ℃. The estimated parameters, heat transfer coefficient and apparent thermal resistance, are correlated with the fluid velocity and fluid temperature. This sensor gives a good correlation, repeatability, and sensitivity between the estimated parameters and the fluid velocities with an accurate estimation of the fluid temperatures without environmental interference. Third, this sensor is tested for laminar flow in pipes over a range of fluid velocity from 0.049 m/s to 0.45 m/s and a range of fluid temperature from 20 ℃ to 50 ℃. A new empirical correlation between the estimated parameters and the laminar fluid velocity has been developed. The results show that this sensor gives lower sensitivity and accuracy between the estimated parameters and the fluid velocity and fluid temperature for the laminar flow. / Doctor of Philosophy / Heating or cooling is responsible for approximately 50% of the total energy consumption in a building. Budlings' energy consumption can be measured by energy flow rate sensors (measuring both fluid velocity and fluid temperature). Current energy flow rate sensors are invasive (requiring installation inside the system and disturbing the flow) which create unacceptable risks, such as fluid leaks and damage the equipment. Other energy flow rate sensors based on ultrasonic and electromagnetic technologies are non-invasive which can be installed on the outside of the pipe without disturbing the flow, however, they are expensive to buy, difficult to install, and hard to calibrate. Therefore, developing new sensor techniques is necessary, preferably non-invasive, low-cost, and easy to install. In this dissertation, a new non-invasive, low-cost, and easy to install thermal energy flow rate sensor has been designed, developed, and tested. This thermal sensor is based on transient heat flux and temperature measurements which are made on the outside of a copper pipe surface by using a heat flux sensor and a thermocouple. This sensor is used to estimate the energy consumption by measuring a fluid velocity and a fluid temperature in heating and cooling pipe applications for different pipe diameters, different fluids, and different pipe materials. A parameter estimation code is developed to match the analytical and experimental sensor temperature values and to estimate the unknown system parameters. These parameters are correlated with the fluid velocity and fluid temperature. Experiments are completed over a large range of fluid velocity from 0.049 m/s to 5.5 m/s and a range of fluid temperature from 20℃ to 50℃. The encouraging measurement results show that this sensor gives a good correlation, repeatability, accuracy, and sensitivity between the estimated parameters and the fluid velocities with an accurate estimation of the fluid temperatures to allow calculation of the thermal energy consumption.

This work presents the development of a novel and non-invasive method that measures fluid flow rate and temperature in pipes. While current non-invasive flow meters are able to measure pipe flow rate, they cannot simultaneously measure the internal temperature of the fluid flow, which limits their widespread application. Moreover, devices that are able to determine flow temperature are primarily intrusive and require constant maintenance, which can shut down operation, resulting in downtime and economic loss. Consequently, non-invasive flow rate and temperature measurement systems are becoming increasingly attractive for a variety of operations, including for use in leak detection, energy metering, energy optimization, and oil and gas production, to name a few. In this work, a new solution method and parameter estimation scheme are developed and deployed to non-invasively determine fluid flow rate and temperature in a pipe. This new method is utilized in conjunction with a sensor-based apparatus--"namely, the Combined Heat Flux and Temperature Sensor (CHFT+), which employs simultaneous heat flux and temperature measurements for non-invasive thermal interrogation (NITI). In this work, the CHFT+ sensor embodiment is referred to as the British Thermal Unit (BTU) Meter. The fluid's flow rate and temperature are determined by estimating the fluid's convection heat transfer coefficient and the sensor-pipe thermal contact resistance. The new solution method and parameter estimation scheme were validated using both simulated and experimental data. The experimental data was validated for accuracy using a commercially available FR1118P10 Inline Flowmeter by Sotera Systems (Fort Wayne, IN) and a ThermaGate sensor by ThermaSENSE Corp. (Roanoke, VA). This study's experimental results displayed excellent agreement with values estimated from the aforementioned methods. Once tested in conjunction with the non-invasive BTU Meter, the proposed solution and parameter estimation scheme displayed an excellent level of validity and reliability in the results. Given the proposed BTU Meter's non-invasive design and experimental results, the developed solution and parameter estimation scheme shows promise for use in a variety of different residential, commercial, and industrial applications. / MS

The goal of this master’s thesis is creating a model of the attenuation of the fluid temperature fluctuations using methods described in the thesis. PCM is used to attenuation of fluctuations. This thesis is example of utilization PCM in technical practice. Numerical calculation of PCM phase change uses the method of effective heat capacity and enthalpy method. A part of this thesis also forms a theoretical basis for heat transfer described by differential equations. The final part of the thesis is dedicated to the optimization of the model and the description of the optimization methods.