Relevant bibliographies by topics / Steam recovery

Academic literature on the topic 'Steam recovery'

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Published: 4 June 2021
Last updated: 20 February 2023

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Journal articles on the topic "Steam recovery"

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Ion, Ion V., Antoaneta Ene, and Gabriel Mocanu. "Boiler blowdown recovery." Annals of the ”Dunarea de Jos” University of Galati Fascicle II Mathematics Physics Theoretical Mechanics 44, no. 2 (December 29, 2021): 98–102. http://dx.doi.org/10.35219/ann-ugal-math-phys-mec.2021.2.03.

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One way to reduce the heat loss of the steam boiler is to reduce the blowdown rate and recover the heat from the purged water. Purging the boiler, although necessary, represents a loss of treated water and a loss of heat because the purged water is water brought to saturation. Blowdown recovery must be done according to the available users/consumers. The paper analyses the recovery of blowdown of a steam boiler of 420 t/h capacity by using a flash separator and a makeup water preheater. The flash steam is used for the feed water deaeration. The heat recovered from the blowdown can reach 97%, and the recovered water can reach 43%.
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Vivek, P., and P. Vijaya kumar. "Heat Recovery Steam Generator by Using Cogeneration." International Journal of Engineering Research 3, no. 8 (August 1, 2014): 512–16. http://dx.doi.org/10.17950/ijer/v3s8/808.

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Martínez-Gómez, Jonathan Enrique, Abraham Medina, Francisco J. Higuera, and Carlos A. Vargas. "Experiments on Water Gravity Drainage Driven by Steam Injection into Elliptical Steam Chambers." Fluids 7, no. 6 (June 16, 2022): 206. http://dx.doi.org/10.3390/fluids7060206.

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Based on a recently published theoretical model, in this work we experimentally studied the problem of gravity water drainage due to continuous steam injection into an elliptical porous chamber made of glass beads and embedded in a metallic, quasi-2D, massive cold slab. This configuration mimics the process of steam condensation for a given time period during the growth stage of the steam-assisted gravity drainage (SAGD) process, a method used in the recovery of heavy and extra-heavy oil from homogeneous reservoirs. Our experiments validate the prediction of the theoretical model regarding the existence of an optimal injected steam mass flow rate per unit length, ϕopt, to achieve the maximum recovery of a condensate (water). We found that the recovery factor is close to 85% when measured as the percentage of the mass of water recovered with respect to the injected mass. Our results can be extended to actual oil-saturated reservoirs because the model involves the formation of a film of condensates close to the chamber edge that allows for gravity drainage of a water/oil emulsion into the recovery well.
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Zhao, Litong. "Steam Alternating Solvent Process." SPE Reservoir Evaluation & Engineering 10, no. 02 (April 1, 2007): 185–90. http://dx.doi.org/10.2118/86957-pa.

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Summary A new heavy-oil-recovery process, the steam alternating solvent (SAS) process, is proposed and studied using numerical simulation. The process is intended to combine the advantages of the steam-assisted gravity drainage (SAGD) and vapor-extraction (vapex) processes to minimize the energy input per unit oil recovered. The SAS process involves injecting steam and solvent alternately, and the basic well configurations are the same as those in the SAGD process. Field-scale simulations were conducted to assess the SAS process performance under typical Cold Lake, Alberta, reservoir conditions. These results suggested that the oil-production rate of an SAS process could be higher than that of a SAGD process, while the energy input was 18% less than that of a SAGD process. By varying the length of the steam- and solvent-injection periods in a cycle, a different set of steam/oil and solvent/oil ratios may be obtained because the temperature profiles and solvent-concentration distributions in the vapor chamber can be affected by the injection pattern. The process therefore can be optimized for a specific reservoir under certain economic conditions. Introduction There are large heavy-oil and bitumen deposits in many areas of the world. The resources are especially enormous in northern Alberta, Canada. However, the high viscosity of these oils, usually more than 10 000 mPa×s, hinders the recovery of these resources. To recover such petroleum resources, two types of methods exist for the reduction of oil viscosity. The first is to increase oil temperature. This can be achieved by injecting a hot fluid, such as steam, into the formation, or by in-situ combustion through injecting oxygen-containing gases. The second method is to dilute the viscous petroleum by lower-viscosity hydrocarbon solvent. This method involves injecting a hydrocarbon solvent, such as propane or butane, or a mixture of hydrocarbons into the oil reservoir. As the solvent dissolves into viscous oil, the viscosity of the mixture becomes much lower than the original viscosity of the heavy oil. The diluted oil then can be recovered. The combinations of the above viscosity reduction methods and the horizontal-well technology have been the focus of research for the past 20 years. Two processes, SAGD and vapex, have been developed for the recovery of heavy-oil and bitumen resources (Butler et al. 1981; Butler and Mokrys 1991; Frauenfeld and Lillico 1999). The first has been tested successfully in the field and is currently the process of choice for commercial in-situ recovery (Edmunds et al. 1994; Mukherjee et al. 1995), while the second is starting initial field testing (Butler and Yee 2000). The advantage of the SAGD process is its high recovery and high oil-production rate. However, the high production rate is associated with excessive energy consumption, CO2 generation, and expensive post-production water treatment. The vapex process has the advantage of lower energy consumption (and, therefore, less CO2 generation) and much lower water-treatment costs. The major drawback of the vapex process, however, is its expected relatively lower oil-production rate and the uncertainty on reservoir retention of solvent. In the past several years, modifications have been proposed to improve SAGD's energy efficiency, either through injection of noncondensable gas with steam for reducing heat loss (Jiang et al. 1998) or through injection of solvents and steam together for increasing production rate (Nasr and Isaacs 2001). The combination of solvent with steam also has been studied in the steamflooding process (Farouq Ali and Abad 1976; Venturini and Mamora 2003).
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Sato, Takashi, and Shoji Hagiwara. "Heat recovery from TMP waste steam." JAPAN TAPPI JOURNAL 40, no. 4 (1986): 344–51. http://dx.doi.org/10.2524/jtappij.40.344.

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Zhang, Yong Jie, Jian Yun Jiang, Jian Dong Ye, Meng Fu, and Fan Zhang. "Study on Waste Heat Recovery of Soy Sauce Production Process in Jinshilongmen Brewery." Advanced Materials Research 724-725 (August 2013): 925–31. http://dx.doi.org/10.4028/www.scientific.net/amr.724-725.925.

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Considering characteristics of soy sauce production process and the equipment in JinShiLongMen Brewery, a series of energy-saving technology solutions, including secondary recovery of residual steam in steaming process, heat recovery in high temperature soy sauce cooling process, insulation of high temperature salt water tank and insulation of steam pipeline, was developed. After the implementation of these solutions, the system runs stably and experimental testing analysis shows that the annual amount of residual heat recovered by secondary recovery of residual steam in steaming process was 9.635×108 kJ, amounting to reduce steam cost RMB79,100 Yuan, recovered in high temperature soy sauce cooling process was 1.839×109 kJ, amounting to reduce steam cost RMB151,100 Yuan. The results show that the energy saving technologies achieved good economic and environmental benefits and are applied to the same industry.
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Kumagai, Shogo, Tomoyuki Hosaka, Tomohito Kameda, and Toshiaki Yoshioka. "Steam Pyrolysis of Polyimides: Effects of Steam on Raw Material Recovery." Environmental Science & Technology 49, no. 22 (November 3, 2015): 13558–65. http://dx.doi.org/10.1021/acs.est.5b03253.

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Zhu, Da, Joule A. Bergerson, and Ian D. Gates. "On fingering of steam chambers in steam-assisted heavy oil recovery." AIChE Journal 62, no. 4 (December 15, 2015): 1364–81. http://dx.doi.org/10.1002/aic.15121.

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Palaniandy, Yoganathan, Nor Mariah Adam, Yiu Pang Hung, and Fatin Hana Naning. "Potential of Steam Recovery from Excess Steam in Sterilizer at Palm Oil Mill." Journal of Advanced Research in Fluid Mechanics and Thermal Sciences 79, no. 1 (December 15, 2020): 17–26. http://dx.doi.org/10.37934/arfmts.79.1.1726.

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Energy saving is something that being focus deeply either larger or smaller industry in this current era especially steam and electricity. In a crude palm oil mill, tons of fibers and woods are used for burning process as a boiler fuel to generate steam. As steam is good heat transfer medium, it is use for the regular process of heating the product or materials by direct and batch heating to raise the temperature in order to change the characteristic. In typical palm oil mill, every 1000kg of fresh fruits bunches (FFB) required 250kg of steam energy for the sterilization process. It is not surprising that the exhaust lost that release to the atmosphere from the total steam usage is about 70%, which can conclude as energy waste. By referring to this issue, the cost of replace consumable boiler fuel increase tremendously. Besides that, the huge amount of heat release caused the thermal pollution that may have significant effects in the ecological balance and lead to changes in the aquatic fauna and flora. This paper reviews and critically discusses the waste of steam energy and the morphology involved in excess steam from sterilizer. The system that combined with few steps of steam recovery were developed to recovery the low-pressure steam to form the mid-pressure steam that can able to reuse at the process plant. The steam ejector technology is use in this research to recover and reuse the excess steam leading to lower energy consumption and fuel costs. The overall idea is about combining the low-pressure excess steam with high-pressure steam that directly supply from back pressure receiver to form the mid-pressure steam. The Ansys software used as to identify the change of parameter of excess steam and through the software, the percentage of motive steam needed to combine with excess steam finalized. Via recovery and reuse the excess steam from sterilizer, the total energy consumption will be minimized at least 20% which can able to reduce the massive expenses for boiler fuel that benefit the palm oil mill owners.
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Huang, Ting, Kai Peng, Wenzhi Song, Changpeng Hu, and Xiao Guo. "Change Characteristics of Heavy Oil Composition and Rock Properties after Steam Flooding in Heavy Oil Reservoirs." Processes 11, no. 2 (January 18, 2023): 315. http://dx.doi.org/10.3390/pr11020315.

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The thermal recovery method of steam flooding is one of the most common development methods for heavy oil reservoirs. However, after multiple rounds of steam injection development, the composition of crude oil and reservoir rock properties have changed greatly, which is unfavorable for the subsequent enhanced oil recovery. It is necessary to study the distribution of the remaining oil after the thermal recovery of heavy oil reservoirs, and clarify the change characteristics of the components of the crude oil under different steam injection conditions. At the same time, the change of porosity and the permeability of the rocks after steam flooding, and its influence on oil recovery, are investigated. In this paper, the composition changes of heavy oil before and after steam flooding are studied through experiments and numerical simulation methods. A numerical model is established to study the retention characteristics of heavy components in heavy oil reservoirs by the CMG software. The effects of different steam injection conditions, and heavy oil with different components on the residual retention of heavy components, are compared and studied. The changes of rock physical properties in heavy oil reservoirs after steam flooding is clarified. The results show that after steam flooding, the heavy components (resin and asphaltenes) of the recovered oil decrease, and the heavy components in the formation increase in varying degrees. With the increase of heavy components in the crude oil, the remaining oil in the formation increases after steam flooding, and the retention of heavy components increases; after steam flooding, the stronger the rock cementation strength, the higher the degree of reserve recovery, and it is difficult to form breakthrough channels; the greater the steam injection intensity, the earlier to see steam breakthrough in the production well, and the lower the degree of reserve recovery. The research reveals the changes of heavy oil components and rock properties after steam flooding, providing support for the subsequent enhanced oil recovery.
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Dissertations / Theses on the topic "Steam recovery"

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Al-Abbasi, Adel. "Steam-flood modelling." Thesis, University of Bath, 1988. https://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.383305.

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Jansson, Johan. "Economical optimization of steam data for recovery boilers." Thesis, Umeå universitet, Institutionen för tillämpad fysik och elektronik, 2017. http://urn.kb.se/resolve?urn=urn:nbn:se:umu:diva-144328.

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Pulp and paper mills are high power consuming industries. Pulp and integrated mills produce power via steam turbines in recovery boilers. Due to high power prices and the fact that biomass combusted in the recovery boiler is considered as green energy, there is today a desire to always increase the power generation when investing in new recovery boilers. In order to increase power output from the steam turbine the steam data (i.e temperature and pressure) needs to be increased. With higher steam temperature follows a higher risk of corrosion due to the non process element potassium in the boiler fuel. The uncertainties of high temperature corrosion and the unpredictable environment in the furnace makes it difficult to design recovery boilers. This results in higher investment cost and could lead to less profit for the mill buying the boiler. The question then stands whether the revenue obtained from the higher power generation, is higher than the investment made for the upgrade in order to produce the higher steam data over a certain time. And more specifically what steam data will be the most economical, when comparing revenue from power generation with investment cost? In this study, together with ÅF Industry AB, four boilers with different steam data (Boiler A: 38.5 bar, 450°C; Boiler B: 92 bar, 480°C; Boiler C: 106 bar, 500°C; Boiler D: 115 bar, 515°C) were compared. The boilers were compared for four potassium levels: 1.0wt%, 1.5wt%, 2.5wt%, 3.5wt%. And two values of power were used, 300 SEK/MWh and 700 SEK/MWh. The marginal differences between the boilers were: the amount of material used in the superheaters in order to produce different steam data; the type of material used in the superheaters and the furnace; whether an ash-treatment system was needed (in order to purge potassium from the process); the turbines and generators; whether a feed water demineralization equipment was needed; the yearly cost for make-up chemicals (due to usage of an ash-treatment system) and the amount of power generated. The boilers investment cost and net yearly revenue were compared in order to determine the marginal pay-off in years. The most economical choice of boiler for the different potassium levels for 300 SEK/MWh: 1.0wt%, Boiler D; 1.5wt%, Boiler C; 2.5wt%, Boiler B; 3.5wt%, Boiler D (A). And for 700 SEK/MWh: 1.0wt%, Boiler D; 1.5wt%, Boiler C; 2.5wt%, Boiler D (B); 3.5wt%, Boiler D. The conclusion in this thesis was that the deciding factor is whether the boiler is in need of an ash-treatment system. Higher steam data is preferable as long as ash-treatment can be avoided. However, when comparing two boilers with ash-treatment the one with higher steam data is more feasible. Low steam data, such as boiler A, will never be feasible, regardless of potassium level and value of power.
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Stuart, Paul R. (Paul René). "Kraft black liquor recovery usiung steam plasma technology." Thesis, McGill University, 1991. http://digitool.Library.McGill.CA:80/R/?func=dbin-jump-full&object_id=70341.

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The objective of this study was to examine the possibility of producing white liquor directly from kraft black liquor using a single stage plasma reactor. An Atomized Suspension Technique Reactor was designed in which a fine spray of concentrated black liquor was fed co-currently with a jet of high-temperature steam, generated using plasma technology. The pilot scale reactor processed up to 23 kg/h black liquor solids on a dry basis during the experimental programme.
The most successful experiment simulated the case where the product gas from the plasma reactor would be recycled and used as the plasma gas. A high quality green liquor was produced: over 99% of the black liquor carbon was gasified, over 99% of the total sulphur was reduced to Na$ sb2$S, and near-complete sulphur recovery was achieved.
It is postulated that white liquor similar to that obtained in the conventional kraft recovery process would form in a plasma reactor following certain reactor modification including the elimination of alumina-containing refractory walls and the recycle of reactor effluent gases.
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Mokhber, A. R. "The steam drive process in enhanced oil recovery." Thesis, University of Strathclyde, 1986. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.381691.

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Chen, Hung-Lung. "Analytical modeling of thermal oil recovery by steam stimulation and steamflooding /." Access abstract and link to full text, 1987. http://0-wwwlib.umi.com.library.utulsa.edu/dissertations/fullcit/8725094.

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Nesse, Thomas. "Experimental comparison of hot water/propane injection to steam/propane injection for recovery of heavy oil." Thesis, Texas A&M University, 2004. http://hdl.handle.net/1969.1/1390.

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Generating enough heat to convert water into steam is a major expense for projects that inject steam into reservoirs to enhance hydrocarbon recovery. If the temperature of the injected fluid is lowered this expense would be reduced. In the past, attempts have been made to inject hot water instead of steam. The results have all been rather poor, the major problem being low sweep efficiency. The hot water just doesn’t enhance oil recovery enough. Adding propane to the steam injected in the reservoir lowers the boiling point of the light to intermediate hydrocarbon fractions, upgrading the oil and reducing viscosity. The goal of this investigation is to see if the same effects could be achieved when adding propane to hot water – making it a lower cost option for an injection operation. Results conclude that you need steam to achieve satisfactory recovery. These results reflect differences in heat injected by steam compared to that of hot water. Steam has a more penetrating effect, shooting into the reservoir where the hot water moves more slowly forward. The propane just doesn’t seem to have the same accelerating effect when used with water as it does when used with steam.
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Horkeby, Kristofer. "Simulation of Heat Recovery Steam Generator in a Combined Cycle Power Plant." Thesis, Linköpings universitet, Institutionen för systemteknik, 2012. http://urn.kb.se/resolve?urn=urn:nbn:se:liu:diva-75836.

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This thesis covers the modelling of a Heat Recovery Steam Generator (HRSG) in a Combined Cycle Power Plant(CCPP). This kind of power plant has become more and more utilized because of its high efficiency and low emissions. The HRSG plays a central role in the generation of steam using the exhaust heat from the gas turbine. The purpose of the thesis was to develop efficient dynamic models for the physical components in the HRSG using the modelling and simulation software Dymola. The models are then to be used for simulations of a complete CCPP.The main application is to use the complete model to introduce various disturbances and study their consequences inthe different components in the CCPP by analyzing the simulation results. The thesis is a part of an ongoingdevelopment process for the dynamic simulation capabilities offered by the Solution department at SIT AB. First, there is a theoretical explanation of the CCPP components and control system included in the scope of this thesis. Then the development method is described and the top-down approach that was used is explained. The structure and equations used are reported for each of the developed models and a functional description is given. Inorder to ensure that the HRSG model would function in a complete CCPP model, adaptations were made and tuning was performed on the existing surrounding component models in the CCPP. Static verifications of the models are performed by comparison to Siemens in-house software for static calculations. Dynamic verification was partially done, but work remains to guarantee the validity in a wide operating range. As a result of this thesis efficient models for the drum boiler and its control system have been developed. An operational model of a complete CCPP has been built. This was done integrating the developed models during the work with this thesis together with adaptations of already developed models. Steady state for the CCPP model is achieved during simulation and various disturbances can then be introduced and studied. Simulation time for a typical test case is longer than the time limit that has been set, mainly because of the gas turbine model. When using linear functions to approximate the gas turbine start-up curves instead, the simulation finishes within the set simulation time limit of 5 minutes for a typical test case.
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Tavakkoli, Osgouei Yashar. "An Experimental Study On Steam Distillation Of Heavy Oils During Thermal Recovery." Master's thesis, METU, 2013. http://etd.lib.metu.edu.tr/upload/12615574/index.pdf.

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Thermal recovery methods are frequently used to enhance the production of heavy crude oils. Steam-based processes are the most economically popular and effective methods for heavy oil recovery for several decades. In general, there are various mechanisms over steam injection to enhance and have additional oil recovery. However, among these mechanisms, steam distillation plays pivotal role in the recovery of crude oil during thermal recovery process. In this study, an experimental investigation was carried out to investigate the role of various minerals present in both sandstone and carbonate formations as well as the effect of steam temperature on steam distillation process. Two different types of dead-heavy crude oils were tested in a batch autoclave reactor with 30 % water and the content of the reactor (crude oil, 10 % rock and mineral). The results were compared as the changes in the density, viscosity and chemical composition (SARA and TPH analyses) of heavy crude oil. Five different mineral types (bentonite, sepiolite, kaolinite, illite and zeolite) were added into the original crude oil and reservoir rocks to observe their effects on the rheological and compositional changes during steam distillation process. Analysis of the results of experiments with Camurlu and Bati Raman heavy crude oils in the presence of different minerals such as Bentonite, Zeolite, Illite, Sepiolite, and Kaolinite in both sandstone and limestone reservoir rocks indicate that steam distillation produces light end condensates which can be considered as solvent or condensate bank during steam flooding operation. It was also illustrated that minerals in reservoir formations perform the function of producing distilled light oil compounds, resulting in enhancement of heavy crude oils recovery in steam flooding. Measurements showed that the remaining oil after steam distillation has higher viscosity and density. On the other hand, the effect of steam distillation is more pronounced in limestone reservoirs compared to sandstone reservoirs for the given heavy crude oil and steam temperature. Among the five different minerals tested, kaolinite found to be the most effective mineral in terms of steam distillation.
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Vytla, Veera Venkata Sunil Kumar. "CFD Modeling of Heat Recovery Steam Generator and its Components Using Fluent." UKnowledge, 2005. http://uknowledge.uky.edu/gradschool_theses/336.

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Combined Cycle power plants have recently become a serious alternative for standard coal- and oil-fired power plants because of their high thermal efficiency, environmentally friendly operation, and short time to construct. The combined cycle plant is an integration of the gas turbine and the steam turbine, combining many of the advantages of both thermodynamic cycles using a single fuel. By recovering the heat energy in the gas turbine exhaust and using it to generate steam, the combined cycle leverages the conversion of the fuel energy at a very high efficiency. The heat recovery steam generator forms the backbone of combined cycle plants, providing the link between the gas turbine and the steam turbine. The design of HRSG has historically largely been completed using thermodynamic principles related to the steam path, without much regard to the gas-side of the system. An effort has been made using resources at both UK and Vogt Power International to use computational fluid dynamics (CFD) analysis of the gas-side flow path of the HRSG as an integral tool in the design process. This thesis focuses on how CFD analysis can be used to assess the impact of the gas-side flow on the HRSG performance and identify design modifications to improve the performance. An effort is also made to explore the software capabilities to make the simulation an efficient and accurate.
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PINTO, RAPHAEL GUIMARAES DUARTE. "SIMULATION OF HEAT RECOVERY STEAM GENERATOR OPERATING IN A COMBINED CYCLE PLANT." PONTIFÍCIA UNIVERSIDADE CATÓLICA DO RIO DE JANEIRO, 2012. http://www.maxwell.vrac.puc-rio.br/Busca_etds.php?strSecao=resultado&nrSeq=20769@1.

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PONTIFÍCIA UNIVERSIDADE CATÓLICA DO RIO DE JANEIRO
A evolução das turbinas a gás industriais resultou em um processo de combustão mais eficiente que permitiu a elevação da temperatura dos gases na exaustão dessa máquina. Assim, caldeiras de recuperação de calor cada vez mais complexas foram desenvolvidas com o intuito de aproveitar ao máximo o potencial energético na exaustão das turbinas. Dessa forma, modelos computacionais capazes de prever as condições de operação do equipamento se mostraram necessários de maneira a analisar o comportamento da máquina em diferentes situações, visando à máxima eficiência do processo. Esta dissertação descreve um modelo computacional capaz de simular o funcionamento fora do ponto de projeto, em regime permanente, de uma caldeira de recuperação de calor operando em uma usina de ciclo combinado, enfatizando sua utilização em sistemas de diagnóstico. As rotinas foram desenvolvidas em FORTRAN e os trocadores de calor presentes na HRSG foram modelados individualmente e calibrados através de um sistema de otimização utilizando algoritmos genéticos, responsável por minimizar o desvio do modelo. O programa desenvolvido foi validado contra dados de operação de uma usina real e mostrou resultados satisfatórios, que confirmam a robustez e fidelidade do modelo de simulação.
The heavy duty gas turbines evolution and, consequently, a more efficient combustion process, allowed the temperature rising of the machines’ exhaust gases. Thus, more complex heat recovery steam generators were developed in order to maximize the use of that energy potential. Therefore, computational models capable to predict the operational conditions of the equipment may be needed in order to analyze the machine’s behavior for different situations, in a way to maximize the process efficiency. This thesis describes a computational model able to simulate the off-design behavior of a heat recovery steam generator operation in a combined cycle plant, emphasizing its utilization in diagnostics systems. The routines were developed using FORTRAN, each heat exchanger inside the Heat Recovery Steam Generator (HRSG) was designed individually and the calibration was done by a genetic algorithm responsible for minimizing the model’s deviations. The developed program was validated against operational data from a real plant and showed satisfactory results, confirming the robustness and fidelity of this simulation model.
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Books on the topic "Steam recovery"

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Vakkilainen, Esa K. Offdesign operation of kraft recovery boiler. Lappeenranta: Lappeenranta University of Technology, 1993.

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Industrial boilers and heat recovery steam generators: Design, applications, and calculations. New York: Marcel Dekker, 2003.

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Hyne, J. B. Aquathermolysis: A synopsis of work on the chemical reaction between water (steam) and heavy oil sands during simulated steam stimulation. [Edmonton, Alberta: AOSTRA Library and Information Service], 1986.

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Alberta. Scientific and Engineering Services and Research Division. Development of a coal-fired boiler for steam injection in heavy oil recovery. Edmonton, AB: Alberta Energy, Scientific and Engineering Services and Research Division, 1989.

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Castaldini, Carlo. Environmental assessment of an enhanced oil recovery steam generator equipped with a low-NOx burner. Research Triangle Park, NC: U.S. Environmental Protection Agency, Air and Energy Engineering Research Laboratory, 1986.

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Someshwar, Arun V. A review of NOx emission control strategies for industrial boilers, Kraft recovery furnaces, and lime kilns. New York: National Council of the Paper Industry for Air and Stream Improvement, 1999.

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Hayes, Gillian D., and Timothy S. Flores. Stream restoration: Halting disturbances, assisted recovery, and managed recovery. Edited by Hayes Gillian D and Flores Timothy S. Hauppauge, N.Y: Nova Science Publishers, 2009.

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Assembly, Canada Legislature Legislative. Bill: An act to provide for the taxation and recovery of arbitrator's fees. Quebec: Hunter, Rose & Lemieux, 2003.

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Simon, Andrew. Geomorphic and vegetative recovery processes along modified stream channels of west Tennessee. Nashville, Tenn: U.S. Geological Survey, 1992.

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Simon, Andrew. Geomorphic and vegetative recovery processes along modified stream channels of west Tennessee. Nashville, Tenn: U.S. Geological Survey, 1992.

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Book chapters on the topic "Steam recovery"

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Isaacs, E. E., J. Ivory, and M. K. Green. "Steam-Foams for Heavy Oil and Bitumen Recovery." In Advances in Chemistry, 235–58. Washington, DC: American Chemical Society, 1994. http://dx.doi.org/10.1021/ba-1994-0242.ch006.

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Sharma, Achintya, Meeta Sharma, Anoop Kumar Shukla, and Nitin Negi. "Evaluation of Heat Recovery Steam Generator for Gas/Steam Combined Cycle Power Plants." In Lecture Notes in Mechanical Engineering, 189–200. Singapore: Springer Singapore, 2019. http://dx.doi.org/10.1007/978-981-13-6416-7_18.

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Wang, Tao. "Experimental Study on Steam Distillation Mechanism of Steam Flooding to Enhance Oil Recovery." In Proceedings of the International Field Exploration and Development Conference 2021, 1028–35. Singapore: Springer Nature Singapore, 2022. http://dx.doi.org/10.1007/978-981-19-2149-0_92.

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Chantasiriwan, Somchart, and Sarocha Charoenvai. "Using Superheated Steam Dryer for Cogeneration System Improvement and Water Recovery." In Transition Towards 100% Renewable Energy, 59–68. Cham: Springer International Publishing, 2018. http://dx.doi.org/10.1007/978-3-319-69844-1_6.

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Pleshanov, Konstantin A., Kirill Sterkhov, Dmitry A. Khokhlov, and Mikhail N. Zaichenko. "Pressurized Heat Recovery Steam Generator Design for CCGT with Gas Turbine GT-25PA and Steam Turbine T-100." In Lecture Notes in Mechanical Engineering, 27–37. Singapore: Springer Nature Singapore, 2022. http://dx.doi.org/10.1007/978-981-16-9376-2_3.

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Zheng, Wei, Xianhong Tan, Taichao Wang, and Yuting Bai. "Thermal Recovery Effect Evaluation of Cyclic Steam Stimulation in Offshore Heavy Oilfield." In Proceedings of the International Petroleum and Petrochemical Technology Conference 2020, 327–33. Singapore: Springer Singapore, 2021. http://dx.doi.org/10.1007/978-981-16-1123-0_31.

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Galceran, M. T., and F. J. Santos. "Evaluation of Steam Distillation-Extraction Procedure for the Recovery of Phenols in Water." In Organic Micropollutants in the Aquatic Environment, 46–51. Dordrecht: Springer Netherlands, 1988. http://dx.doi.org/10.1007/978-94-009-2989-0_5.

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Ramesh, V. K., V. Chintala, and Suresh Kumar. "Direct Steam Generation by an Enclosed Solar Parabolic Trough for Enhanced Oil Recovery." In Recent Advances in Mechanical Infrastructure, 189–98. Singapore: Springer Singapore, 2019. http://dx.doi.org/10.1007/978-981-32-9971-9_19.

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Higuera, F. J., and A. Medina. "A Simple Model of the Flow in the Steam Chamber in SAGD Oil Recovery." In Communications in Computer and Information Science, 337–45. Cham: Springer International Publishing, 2019. http://dx.doi.org/10.1007/978-3-030-38043-4_26.

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Wu, Michael M., Kevin Chang, David J. Gregg, Abdel Boussaid, Rodger P. Beatson, and John N. Saddler. "Optimization of Steam Explosion to Enhance Hemicellulose Recovery and Enzymatic Hydrolysis of Cellulose in Softwoods." In Twentieth Symposium on Biotechnology for Fuels and Chemicals, 47–54. Totowa, NJ: Humana Press, 1999. http://dx.doi.org/10.1007/978-1-4612-1604-9_5.

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Conference papers on the topic "Steam recovery"

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Cokar, Marya, Michael Kallos, and Ian Donald Gates. "Reservoir Simulation of Steam Fracturing in Early Cycle Cyclic Steam Stimulation." In SPE Improved Oil Recovery Symposium. Society of Petroleum Engineers, 2010. http://dx.doi.org/10.2118/129686-ms.

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Hedden, Ralf, Marco Verlaan, and Vaclav Lastovka. "Solvent Enhanced Steam Drive." In SPE Improved Oil Recovery Symposium. Society of Petroleum Engineers, 2014. http://dx.doi.org/10.2118/169070-ms.

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Bautista, L. S., and Francois Friedmann. "Water-Alternating-Steam Process (WASP) Alleviates Downdip Steam Migration in Cymric Field." In SPE/DOE Improved Oil Recovery Symposium. Society of Petroleum Engineers, 1994. http://dx.doi.org/10.2118/27794-ms.

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Trigos, E. M., M. E. Lozano, and A. M. Jimenez. "Cyclic Steam Stimulation Enhanced with Nitrogen." In SPE Improved Oil Recovery Conference. Society of Petroleum Engineers, 2018. http://dx.doi.org/10.2118/190173-ms.

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Ross, T. S., H. Rahnema, C. Nwachukwu, O. Alebiosu, and B. Shabani. "Steam Injection in Tight Oil Reservoir." In SPE Improved Oil Recovery Conference. Society of Petroleum Engineers, 2018. http://dx.doi.org/10.2118/190289-ms.

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Best, D. A., R. P. Lesage, and J. E. Arthur. "Steam Circulation in Horizontal Wellbores." In SPE/DOE Enhanced Oil Recovery Symposium. Society of Petroleum Engineers, 1990. http://dx.doi.org/10.2118/20203-ms.

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Murtaza, Muhammad, and Hassan Dehghanpour. "Three-Phase Flow during Steam Chamber Rise." In SPE Improved Oil Recovery Symposium. Society of Petroleum Engineers, 2012. http://dx.doi.org/10.2118/154287-ms.

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Lau, Hon-chung. "Alkaline Steam Foam: Concepts and Experimental Results." In SPE Enhanced Oil Recovery Conference. Society of Petroleum Engineers, 2011. http://dx.doi.org/10.2118/144968-ms.

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Kay, Brian. "Direct Contact Steam Generation Reduces Carbon Intensity." In SPE Improved Oil Recovery Conference. SPE, 2022. http://dx.doi.org/10.2118/209350-ms.

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Abstract:
Abstract Steam for enhanced oil recovery is typically generated using Once-Through-Steam-Generators (OTSG) produced at large central facilities with the steam then pipelined to each injection well. As much as 50% of the energy can be lost before it reaches the well bore with the combustion emissions vented to atmosphere. Direct Contact Steam Generation (DCSG) injects both steam and hot combustion flue gases into the reservoir. Oil production is increased by reducing oil viscosity through heat while repressuring the reservoir with flue gases and improving miscibility with the CO2 that remains in the reservoir. This combination greatly improves the Steam-Oil-Ratio (SOR) for increased oil recovery as well as delivering environmental benefits related to reduced water requirements and lower emissions resulting in a much lower carbon intensity. DCSG water requirements are 11% less than OTSG methods as water is created by the combustion process, this water is then injected into the reservoir rather than lost to the atmosphere. As most of the DCSG process emissions are indirect, emissions can be further reduced by as much as 30% with the use of low carbon intensity grid electricity for compression. Pilot results show that DCSG used less water, with 70% of the CO2 retained in the formation. Lower SOR and CO2 retained in the reservoir demonstrates lower carbon intensity relative to OTSG. DCSG offers heavy oil operators a novel, viable, method to economically extract currently uncoverable reservoirs at a lower carbon intensity than traditional methods.
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Kumar, J., C. Caubit, J. Bothua, and B. Corre. "Comparison of Coreflooding Experiments – Steam Injection with Steam & Solvent Injection." In IOR 2011 - 16th European Symposium on Improved Oil Recovery. Netherlands: EAGE Publications BV, 2011. http://dx.doi.org/10.3997/2214-4609.201404754.

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Reports on the topic "Steam recovery"

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Skone, Timothy J. Steam injection for oil recovery. Office of Scientific and Technical Information (OSTI), August 2013. http://dx.doi.org/10.2172/1509451.

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Reis, J., and M. Miller. Oil recovery from naturally fractured reservoirs by steam injection methods. Office of Scientific and Technical Information (OSTI), January 1991. http://dx.doi.org/10.2172/6180458.

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Reis, J. C., and M. A. Miller. Oil recovery from naturally fractured reservoirs by steam injection methods. Final report. Office of Scientific and Technical Information (OSTI), May 1995. http://dx.doi.org/10.2172/49829.

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Panicker, Nithin, Marco Delchini, Thomas Sambor, and Adrian Sabau. COMPUTATIONAL FLUID DYNAMICS SIMULATIONS TO PREDICT OXIDATION IN HEAT RECOVERY STEAM GENERATOR TUBES. Office of Scientific and Technical Information (OSTI), March 2022. http://dx.doi.org/10.2172/1888933.

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Diwan, Utpal, and Anthony R. Kovscek. An Analytical Model for Simulating Heavy-Oil Recovery by Cyclic Steam Injection Using Horizontal Wells, SUPRI TR-118. Office of Scientific and Technical Information (OSTI), August 1999. http://dx.doi.org/10.2172/9330.

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Schamel, Steven. Reactivation of an Idle Lease to Increase Heavy Oil Recovery through Application of Conventional Steam Drive Technology in a Low Dip Slope & Reservoir in the Midway-Sunset Field, San Jaoquin Basin, California. Office of Scientific and Technical Information (OSTI), November 1999. http://dx.doi.org/10.2172/14429.

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Schamel, Steven. Reactivation of an Idle Lease to Increase Heavy Oil Recovery through Application of Conventional Steam Drive Technology in a Low Dip Slope and Reservoir in the Midway-Sunset Field, San Jaoquin Basin, California. Office of Scientific and Technical Information (OSTI), July 1999. http://dx.doi.org/10.2172/8524.

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Deo, M., C. Forster, C. Jenkins, S. Schamel, D. Sprinkel, and R. and Swain. Reactivation of an Idle Lease to Increase Heavy Oil Recovery through Application of Conventional Steam Drive Technology in a Low Dip Slope and Basin Reservoir in the Midway-Sunset Field, San Jaoquin Basin, California. Office of Scientific and Technical Information (OSTI), February 1999. http://dx.doi.org/10.2172/3258.

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Schamel, Steven. Reactivation of an Idle Lease to Increase Heavy Oil Recovery Through Application of Conventional Steam Drive Technology in a Low Dip Slope and Basin Reservoir in the Midway-Sunset Field, San Jaoquin Basin, California. Office of Scientific and Technical Information (OSTI), July 1997. http://dx.doi.org/10.2172/1471.

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Steven Schamel. Reactivation of an Idle Lease to Increase Heavy Oil Recovery Through Application of Conventional Steam Drive Technology in a Low Dip Slope and Basin Reservoir in the Midway-Sunset Field, San Jaoquin Basin, California. Office of Scientific and Technical Information (OSTI), March 1998. http://dx.doi.org/10.2172/1472.

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