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Energies, Volume 12, Issue 4 (February-2 2019) – 193 articles

Cover Story (view full-size image): Network operators are aiming to provide widespread network visibility at a justifiable cost across a sprawling and diverse network. The proposed solution uses frequency modulation of the voltage and current with immediate injection into the power line. The method is low-cost yet can monitor magnitude and synchronized phase across a network. View this paper.
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19 pages, 2739 KiB  
Article
Energy Embedded in Food Loss Management and in the Production of Uneaten Food: Seeking a Sustainable Pathway
by Daniel Hoehn, María Margallo, Jara Laso, Isabel García-Herrero, Alba Bala, Pere Fullana-i-Palmer, Angel Irabien and Rubén Aldaco
Energies 2019, 12(4), 767; https://doi.org/10.3390/en12040767 - 25 Feb 2019
Cited by 28 | Viewed by 7076
Abstract
Recently, important efforts have been made to define food loss management strategies. Most strategies have mainly been focused on mass and energy recovery through mixed food loss in centralised recovery models. This work aims to highlight the need to address a decentralised food [...] Read more.
Recently, important efforts have been made to define food loss management strategies. Most strategies have mainly been focused on mass and energy recovery through mixed food loss in centralised recovery models. This work aims to highlight the need to address a decentralised food loss management, in order to manage the different fractions and on each of the different stages of the food supply chain. For this purpose, an energy flow analysis is made, through the calculation of the primary energy demand of four stages and 11 food categories of the Spanish food supply chain in 2015. The energy efficiency assessment is conducted under a resource use perspective, using the energy return on investment (EROI) ratio, and a circular economy perspective, developing an Energy return on investment – Circular economy index (EROIce), based on a food waste-to-energy-to-food approach. Results suggest that the embodied energy loss consist of 17% of the total primary energy demand, and related to the food categories, the vegetarian diet appears to be the most efficient, followed by the pescetarian diet. Comparing food energy loss values with the estimated energy provided for one consumer, it is highlighted the fact that the food energy loss generated by two to three persons amounts to one person's total daily intake. Moreover, cereals is the category responsible for the highest percentage on the total food energy loss (44%); following by meat, fish and seafood and vegetables. When the results of food energy loss and embodied energy loss are related, it is observed that categories such as meat and fish and seafood have a very high primary energy demand to produce less food, besides that the parts of the food supply chain with more energy recovery potential are the beginning and the end. Finally, the EROIce analysis shows that in the categories of meat, fish and seafood and cereals, anaerobic digestion and composting is the best option for energy recovery. From the results, it is discussed the possibility to developed local digesters at the beginning and end of the food supply chain, as well as to developed double digesters installations for hydrogen recovery from cereals loss, and methane recovery from mixed food loss. Full article
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Figure 1
<p>Conceptual diagram of the proposal of this work, recovering energy from food loss with a circular economy approach.</p>
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<p>System boundaries, including the outline of the different considered scenarios.</p>
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<p>Methodology of the study.</p>
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<p>Sankey diagram for primary energy demand of the different food categories throughout the food supply chain. Values expressed in kilojoules per capita per day.</p>
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<p>Food energy loss (FEL) and embodied energy loss (EEL) by stage of the food supply chain. Values expressed in kilojoules per capita per day (left and right ordinate axis).</p>
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<p>Food energy loss (FEL) of the different food categories throughout the supply chain. Values expressed in kilojoules per capita per day.</p>
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<p>Embodied energy loss (EEL) of the different food categories throughout the supply chain. Values expressed in kilojoules per capita per day.</p>
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<p>Primary energy demand values for the considered scenarios expressed in kilojoules per kilogram.</p>
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<p>Energy return on investment–Circular economy index for the considered scenarios.</p>
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<p>Outline of the proposed energy recovery strategies.</p>
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11 pages, 2322 KiB  
Article
Modelling Load Profiles of Heat Pumps
by Jochen Conrad and Simon Greif
Energies 2019, 12(4), 766; https://doi.org/10.3390/en12040766 - 25 Feb 2019
Cited by 11 | Viewed by 8796
Abstract
Approximately one quarter of energy-related emissions in Germany are caused by the domestic sector. At 81%, the largest share of these emissions is due to heat supply. Many measures are available to reduce these emissions. One of these measures, which is considered to [...] Read more.
Approximately one quarter of energy-related emissions in Germany are caused by the domestic sector. At 81%, the largest share of these emissions is due to heat supply. Many measures are available to reduce these emissions. One of these measures, which is considered to play an important role in many studies, is the replacement of fossil-fired boilers with electric heat pumps. In order to be able to analyse the impact of high penetrations of heat pumps on the energy system, the coefficient of performance (COP) must be modelled with high temporal resolution. In this study, a methodology is presented on how to calculate high-resolution COPs and the electrical load of heat pumps based on thermal load curves and temperature time series. The COP is determined by the reciprocal Carnot factor. Since heat pumps are often designed bivalently due to the cost structure, the methodology described can also be used for evaluating the combination of immersion heater and heat pump (here for the air/water heat pump). As a result the theoretical hourly COPs determined are calibrated with annual performance factors from field tests. The modelled COPs show clear differences. Currently, mostly air source heat pumps are installed in Germany. If this trend continues, the maximum electrical load of the heat supply will increase more than would be the case with higher shares of ground source heat pumps. Full article
(This article belongs to the Special Issue Energy Efficiency in Plants and Buildings 2019)
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<p>Emissions caused by domestic sector in 2014 (temperature adjusted).</p>
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<p>Schematic overview of the stock-and-flow model of domestic sector.</p>
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<p>Ambient air temperature (T<sub>a</sub>) and floor temperature (T<sub>fl</sub>) of an air source heat pump in a single family house of the building age class before 1979 (<b>a</b>) and a multi-family house with seven to 12 apartments of the building age class 1995 to 2020 (<b>b</b>).</p>
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<p>Comparison of the COP and the generated heat of an air source heat pump and a ground source heat pump for a single family house before 1979 (<b>a</b>) and a multi-family house of the building age class 1995–2020 (<b>b</b>).</p>
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<p>Generated heat, electric load and COP of an air source heat pump system in a single family house before 1979 (<b>a</b>) and a multi family house of the building age class 1995–2020 (<b>b</b>).</p>
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11 pages, 820 KiB  
Article
Assessment of Energy Efficiency and Its Determinants for Drinking Water Treatment Plants Using A Double-Bootstrap Approach
by María Molinos-Senante and Ramón Sala-Garrido
Energies 2019, 12(4), 765; https://doi.org/10.3390/en12040765 - 25 Feb 2019
Cited by 11 | Viewed by 3718
Abstract
To achieve energy and climate goals, the energy performance of current and future drinking water treatment plants (DWTPs) must be improved. A few studies have evaluated the energy efficiency of these facilities using data envelopment analysis (DEA), however, they have ignored the deterministic [...] Read more.
To achieve energy and climate goals, the energy performance of current and future drinking water treatment plants (DWTPs) must be improved. A few studies have evaluated the energy efficiency of these facilities using data envelopment analysis (DEA), however, they have ignored the deterministic nature of the DEA method. To overcome this limitation, a double-bootstrap DEA approach was used in this study to estimate the energy efficiency of DWTPs. For a sample of Chilean DWTPs, bias-corrected energy efficiency scores were computed with consideration of data variability, and the determinants of DWTP energy efficiency were explored. Most DWTPs in the sample had much room for the improvement of energy efficiency. In the second stage of analysis, facility age, the volume of water treated, and the technology used for treatment were found to influence DWTP energy efficiency. These findings demonstrate the importance of using a reliable and robust method to evaluate the energy efficiency of DWTPs, which is essential to support decision making and to benchmark these facilities’ energy performance. Full article
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<p>Original energy efficiency scores of drinking water treatment plants.</p>
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<p>Ranking of drinking water treatment plants based on original and bias-corrected energy efficiency scores.</p>
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<p>Lower and upper bounds of energy efficiency for each drinking water treatment plant.</p>
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23 pages, 3488 KiB  
Article
Driving Forces of Energy-Related CO2 Emissions Based on Expanded IPAT Decomposition Analysis: Evidence from ASEAN and Four Selected Countries
by Jaruwan Chontanawat
Energies 2019, 12(4), 764; https://doi.org/10.3390/en12040764 - 25 Feb 2019
Cited by 44 | Viewed by 7829
Abstract
ASEAN is a dynamic and diverse region which has experienced rapid urbanization and population growth. Their energy demand grew by 60% in the last 15 years. In 2013, about 3.6% of global greenhouse-gas emissions was emitted from this region and the share is [...] Read more.
ASEAN is a dynamic and diverse region which has experienced rapid urbanization and population growth. Their energy demand grew by 60% in the last 15 years. In 2013, about 3.6% of global greenhouse-gas emissions was emitted from this region and the share is expected to rise substantially. Hence, a better understanding of driving forces of the changes in CO2 emissions is important to tackle global climate change and develop appropriate policies. Using IPAT combined with variance analysis, this study aims to identify the main driving factors of CO2 emissions for ASEAN and four selected countries (Indonesia, Malaysia, Philippines and Thailand) during 1971–2013. The results show that population growth and economic growth were the main driving factors for increasing CO2 emissions for most of the countries. Fossil fuels play an important role in increasing CO2 emissions, however the growth in emissions was compensated by improved energy efficiency and carbon intensity of fossil energy. The results imply that to decouple energy use from high levels of emissions is important. Proper energy management through fuel substitution and decreasing emission intensity through technological upgrades have considerable potential to cut emissions. Full article
(This article belongs to the Special Issue Sustainable Energy Systems)
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<p>Chain decomposition methodology.</p>
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<p>Decomposition flow chart.</p>
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<p>CO<sub>2</sub> emissions in ASEAN countries (calculated from IEA database 2015).</p>
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<p>Total energy production in ASEAN by source (calculated from IEA database 2015).</p>
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<p>Relative contributions of nine ASEAN countries (except Laos PDR) to cumulative ASEAN emissions (1971–2013), current ASEAN emission flux (2013), ASEAN emission annual growth rate (2005–2013), and ASEAN population (2013), (calculated from IEA database 2015).</p>
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<p>CO<sub>2</sub> emissions contribution by source of energy in 2013 (calculated from IEA database 2015).</p>
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<p>Share of CO<sub>2</sub> emissions by sources of energy in 2013 (calculated from IEA database 2015).</p>
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<p>Trends of IPAT factors in ASEAN, Indonesia, Malaysia, Philippines and Thailand, 1971–2013.</p>
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<p>Decomposition results of CO<sub>2</sub> emissions in ASEAN.</p>
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<p>Decomposition results of CO<sub>2</sub> emissions in Indonesia.</p>
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<p>Decomposition results of CO<sub>2</sub> emissions in Malaysia.</p>
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<p>Decomposition results of CO<sub>2</sub> emissions in Philippines.</p>
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<p>Decomposition results of CO<sub>2</sub> emissions in Thailand</p>
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<p>Decomposition results of total CO<sub>2</sub> emissions in Indonesia, Malaysia, Philippines, Thailand, and ASEAN.</p>
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15 pages, 6405 KiB  
Article
Investigation of Elastomer Seal Energization: Implications for Conventional and Expandable Hanger Assembly
by Harshkumar Patel and Saeed Salehi
Energies 2019, 12(4), 763; https://doi.org/10.3390/en12040763 - 25 Feb 2019
Cited by 14 | Viewed by 6678
Abstract
Elastomer seals are extensively used in various wellhead and casing/liner hanger equipment as barriers for isolating fluids. Seal assemblies have been identified as one of the major cause of well control incidents. Majority of hangers utilize conventional weight- or mechanical-set slip-and-seal assembly. The [...] Read more.
Elastomer seals are extensively used in various wellhead and casing/liner hanger equipment as barriers for isolating fluids. Seal assemblies have been identified as one of the major cause of well control incidents. Majority of hangers utilize conventional weight- or mechanical-set slip-and-seal assembly. The objective of this paper is to conduct a detailed investigation of seal energization in conventional and relatively newer expandable type hanger seal assembly. To achieve the objective, the finite element modeling approach was employed. Three dimensional computer models consisting of concentric casings and annular elastomer seal element were constructed. Seal energization process was modelled by manipulating boundary conditions. Conventional seal energization was mimicked by applying rigid support at the bottom of elastomer element and compressing it from the top. Expandable hanger type seal energization was modelled by radially displacing the inner pipe to compress annular seal element. Seal quality was evaluated in terms of contact stress values and profile along the seal-pipe interface. Different amounts of seal energization were simulated. Both types of seal energization processes yielded different contact stress profiles. For the same amount of seal volumetric compression, contact stress profiles were compared. In case of conventional seal energization, contact stress profile decreases from the compression side towards support side. The seal in expandable hanger generates contact stress profile that peaks at the center of contact interface and reduces towards the ends. Convectional seal assembly has more moving parts, making it more prone to failure or under-energization. Finite Element Models were validated using analytical equations, and a good match was obtained. The majority of research related to elastomer seal is focused on material properties evaluation. Limited information is available in public domain on functional design and assessment of seal assembly. This paper adds novel information by providing detailed assessment of advantages and limitations of two different seal energization process. This opens doors for further research in functional failure modes in seal assembly. Full article
(This article belongs to the Special Issue Shale Oil and Shale Gas Resources)
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Figure 1
<p>Schematic of (<b>a</b>) typical conventional and (<b>b</b>) expandable type hanger seal assemblies.</p>
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<p>Causes of secondary barrier failure in 156 loss of well control events occurred during 2000–2015.</p>
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<p>Two dimensional schematic of the Finite Element Analysis (FEA) models of (<b>a</b>) conventional and (<b>b</b>) expandable type hanger seal assembly, and (<b>c</b>) the top view.</p>
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<p>Uniaxial, shear, and biaxial material behavior of Fluorocarbon (FKM).</p>
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<p>Volumetric compression in FEA model of conventional hanger seal.</p>
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<p>Comparison between contact stress simulated by FEA model and calculated using analytical equation.</p>
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<p>Contact stress profiles generated in conventional seal assembly at different volumetric compression.</p>
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<p>Contact stress profiles generate in expandable seal assembly at different volumetric compression.</p>
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<p>Contact pressure as a function of volumetric compression for conventional and expandable assembly (with and without elastomer containment).</p>
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<p>Elastomer seal containment in expandable liner hanger: (<b>a</b>) no containment, (<b>b</b>) 50% containment, and (<b>c</b>) 100% containment.</p>
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<p>Contact stress profiles generated in expandable seal assembly at different amounts of seal containment.</p>
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<p>Contact stress profiles generate in expandable seal assembly with 100% containment and different volumetric compression.</p>
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<p>Contact stress profiles in conventional seal assembly for hyper-elastic FKM.</p>
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<p>Contact stress profiles in expandable seal assembly for hyper-elastic FKM.</p>
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<p>Contact pressure as a function of volumetric compression for conventional and expandable assembly with linear- and hyper-elastic material behavior.</p>
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<p>Effect of friction on contact stress profile in conventional seal assembly.</p>
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<p>Effect of friction on contact stress profile in expandable seal assembly.</p>
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16 pages, 6478 KiB  
Article
Investigating Permeability of Coal Samples of Various Porosities under Stress Conditions
by Mateusz Kudasik
Energies 2019, 12(4), 762; https://doi.org/10.3390/en12040762 - 25 Feb 2019
Cited by 23 | Viewed by 3474
Abstract
Among the numerous factors that have an impact on coal permeability, coal porosity is one of the main parameters. A change in the mechanical stress applied to coal results in a change of porosity. The main objective of the conducted research was to [...] Read more.
Among the numerous factors that have an impact on coal permeability, coal porosity is one of the main parameters. A change in the mechanical stress applied to coal results in a change of porosity. The main objective of the conducted research was to answer the following question: is a decline in coal permeability a direct effect of a decrease in coal porosity, and does mechanical stress result solely in a porosity change? A study of coal porosity under mechanical stress conditions was conducted using a uniquely constructed measurement stand. The coal samples used were briquettes prepared from a granular coal material (middle-rank coal of type B—meta bituminous, upper carboniferous formation) from the “Zofiówka” coal mine, in Poland. In order to describe coal permeability, the Klinkenberg equation was used, as it takes into consideration the slippage effect, typical of porous media characterized by low permeability. On the basis of the obtained results, it was established that the values of the Klinkenberg permeability coefficient decrease as the mechanical stress and the corresponding reduction in porosity become greater. As the briquette porosity increased, the Klinkenberg slippage effect: (i) disappeared in the case of nitrogen, (ii) and was minor for methane. The briquettes used were characterized by various porosities and showed that mechanical stress results mainly in a change in coal porosity, which, in turn, reduces coal permeability. Full article
(This article belongs to the Section L: Energy Sources)
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Graphical abstract

Graphical abstract
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<p>Gas flow in the pore space according to Darcy (<b>a</b>) and taking into account the Klinkenberg slippage effect (<b>b</b>).</p>
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<p>An example of the dependence of the permeability coefficient <math display="inline"><semantics> <mrow> <msub> <mi>k</mi> <mi>g</mi> </msub> </mrow> </semantics></math> on the reciprocal average pressure <math display="inline"><semantics> <mrow> <mn>1</mn> <mo>/</mo> <msub> <mi>p</mi> <mrow> <mi>a</mi> <mi>v</mi> <mi>g</mi> </mrow> </msub> </mrow> </semantics></math>.</p>
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<p>A scheme of the measurement stands for investigating coal permeability under stress conditions, where <math display="inline"><semantics> <mrow> <msub> <mi>P</mi> <mrow> <mi>i</mi> <mi>n</mi> </mrow> </msub> <mo>,</mo> <mtext> </mtext> <msub> <mi>P</mi> <mrow> <mi>o</mi> <mi>u</mi> <mi>t</mi> </mrow> </msub> </mrow> </semantics></math>—are the gas inlet and outlet pressure transducers; <math display="inline"><semantics> <mrow> <msub> <mi>P</mi> <mrow> <mi>a</mi> <mi>t</mi> <mi>m</mi> </mrow> </msub> </mrow> </semantics></math>—is the barometer.</p>
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<p>A photograph (left) and 3D model (right) of a part of the measurement stand for investigating coal permeability under stress conditions.</p>
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<p>A sample course in the changes of the registered parameters for a single measurement procedure (with the sample porosity amounting to 18.87% and the stress value equaling 0 MPa—the graph to the left) and the permeability coefficients <math display="inline"><semantics> <mrow> <msub> <mi>k</mi> <mi>g</mi> </msub> </mrow> </semantics></math> obtained on that basis as a function of the reverse average pressure of gas in the sample (the graph to the right).</p>
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<p>The relationship between the permeability coefficients <math display="inline"><semantics> <mrow> <msub> <mi>k</mi> <mi>g</mi> </msub> </mrow> </semantics></math> of the sample N3 and nitrogen, as a function of the reverse nitrogen average pressure <math display="inline"><semantics> <mrow> <msub> <mi>p</mi> <mrow> <mi>a</mi> <mi>v</mi> <mi>g</mi> </mrow> </msub> </mrow> </semantics></math>, for various stress <math display="inline"><semantics> <mi>σ</mi> </semantics></math> values and the corresponding sample porosities <math display="inline"><semantics> <mi>ϕ</mi> </semantics></math>.</p>
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<p>The relationships between the values of the Klinkenberg permeability coefficient <math display="inline"><semantics> <mrow> <msub> <mi>k</mi> <mo>∞</mo> </msub> </mrow> </semantics></math>, and the slippage factor <math display="inline"><semantics> <mi>b</mi> </semantics></math>, as a function of the porosity, obtained from the tests on the coal samples N1–N4 using nitrogen, where: <math display="inline"><semantics> <mi>σ</mi> </semantics></math>—are the stress values; <math display="inline"><semantics> <mi>ϕ</mi> </semantics></math>—is the porosity.</p>
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<p>The relationships between the values of the Klinkenberg permeability coefficient <math display="inline"><semantics> <mrow> <msub> <mi>k</mi> <mo>∞</mo> </msub> </mrow> </semantics></math>, and the slippage factor <math display="inline"><semantics> <mi>b</mi> </semantics></math>, as a function of the porosity, obtained from the tests on the coal samples M1–M4 using methane, where: <math display="inline"><semantics> <mi>σ</mi> </semantics></math>—are the stress values; <math display="inline"><semantics> <mi>ϕ</mi> </semantics></math>—is the porosity.</p>
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<p>The relationship between the values of the Klinkenberg permeability coefficient <math display="inline"><semantics> <mrow> <msub> <mi>k</mi> <mo>∞</mo> </msub> </mrow> </semantics></math>, and the slippage factor <math display="inline"><semantics> <mi>b</mi> </semantics></math> of coal briquettes and nitrogen &amp; methane as a function of porosity.</p>
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19 pages, 4393 KiB  
Article
Experimental Study and Mechanism Analysis of the Effect of Oil Viscosity and Asphaltene on Foamy Oil
by Zhuangzhuang Wang, Zhaomin Li and Teng Lu
Energies 2019, 12(4), 761; https://doi.org/10.3390/en12040761 - 25 Feb 2019
Cited by 7 | Viewed by 4417
Abstract
Foamy oil is considered an important reason for the anomalous performance in depletion development for some heavy oil reservoirs, but its influence factors remain to be fully investigated. In order to determine the effect of oil viscosity and asphaltene on foamy oil, ten [...] Read more.
Foamy oil is considered an important reason for the anomalous performance in depletion development for some heavy oil reservoirs, but its influence factors remain to be fully investigated. In order to determine the effect of oil viscosity and asphaltene on foamy oil, ten oil samples including two types (deasphalted oil and asphaltenic oil) and five viscosities were used in the work. On this basis, depletion experiments were conducted in a sandpack and microscopic visualization model. Then, viscoelastic moduli of the oil–gas interface were measured to analyze the mechanisms of viscosity and asphaltene of foamy oil from the perspective of interfacial viscoelasticity. Results show that, with the decrease of the oil viscosity, the foamy oil performance in depletion development worsened, including a rapider decline in average pressure, earlier appearance of gas channeling, shorter period of foamy oil, and lower contribution of foamy oil to recovery. Asphaltene had an influence on foamy oil only in the viscosity range between 870 mPa∙s and 2270 mPa∙s for this study. The effect of viscosity and asphaltene on foamy oil can be explained by the viscoelasticity of bubble film. With the increase of oil viscosity, the interfacial viscous modulus increases significantly, indicating the bubble film becomes stronger and more rigid. Asphaltene, like armor on the bubble film, can improve the viscoelastic modulus, especially at lower viscosity. This can inhibit the coalescence of micro-bubbles and increase the possibility of splitting. This work identifies the effects of oil viscosity and asphaltene on foamy oil systematically and provides theoretical support for foamy oil production. Full article
(This article belongs to the Special Issue Enhanced Oil Recovery 2019)
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<p>Schematic diagram of depletion experiment in the sandpack and micromodel.</p>
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<p>Schematic of the pendant drop tensiometer.</p>
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<p>Production behavior for the ten depletion experiments. (<b>a</b>) Change in average pressure with time. (<b>b</b>) Change in production gas–oil ratio with average pressure. (<b>c</b>) Change in oil recovery with average pressure.</p>
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<p>Production behavior for the ten depletion experiments. (<b>a</b>) Change in average pressure with time. (<b>b</b>) Change in production gas–oil ratio with average pressure. (<b>c</b>) Change in oil recovery with average pressure.</p>
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<p>Characteristics for foamy oil depletion development (taking test 1 as an example).</p>
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<p>Characteristics for weak foamy oil depletion development (taking test 7 as an example).</p>
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<p>Characteristics for conventional solution gas drive (taking test 8 as an example).</p>
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<p>Effect of oil viscosity and asphaltene on bubble pressure and pseudo-bubble pressure.</p>
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<p>Effect of oil viscosity and asphaltene on the total recovery and the recovery of each stage.</p>
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<p>Flow characteristic of each type of depletion development: (<b>a</b>) foamy oil depletion development; (<b>b</b>) weak foamy oil depletion development; (<b>c</b>) conventional solution gas drive.</p>
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<p>A continuous process whereby the bubble goes through a pore throat and then splits into small bubbles: (<b>a</b>) bubble deforms; (<b>b</b>) bubble is elongated; (<b>c</b>) bubble gets thinner; (<b>d</b>) bubble splits.</p>
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<p>A continuous process whereby bubbles coalesce: (<b>a</b>) bubbles come across; (<b>b</b>–<b>d</b>) bubbles coalesce.</p>
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<p>Changes in viscoelastic moduli with viscosity: (<b>a</b>) asphaltenic oil; (<b>b</b>) deasphalted oil.</p>
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<p>Effect of asphaltene on the elastic modulus and viscous modulus at different viscosities: (<b>a</b>) elastic modulus; (<b>b</b>) viscous modulus.</p>
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<p>Viscoelastic modulus and the performance of depletion experiments of the ten oil samples.</p>
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<p>Schematic showing how asphaltene plays a protective role akin to armor on the bubble film.</p>
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<p>Schematic showing how interactions between the asphaltene on the bubble film and on the surface of porous media promote the bubble to deform and stretch. (<b>a</b>) Interlacement between the asphaltenes on the bubble film and on the surface of porous media; (<b>b</b>) Bubble deformation and stretch happens due to the interlacement.</p>
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19 pages, 4430 KiB  
Article
Development of an Exergy-Rational Method and Optimum Control Algorithm for the Best Utilization of the Flue Gas Heat in Coal-Fired Power Plant Stacks
by Birol Kılkış
Energies 2019, 12(4), 760; https://doi.org/10.3390/en12040760 - 25 Feb 2019
Cited by 5 | Viewed by 3700
Abstract
Waste heat that is available in the flue gas of power plant stacks is a potential source of useful thermal power. In reclaiming and utilizing this waste heat without compromising plant efficiency, stacks usually need to be equipped with forced-draught fans in order [...] Read more.
Waste heat that is available in the flue gas of power plant stacks is a potential source of useful thermal power. In reclaiming and utilizing this waste heat without compromising plant efficiency, stacks usually need to be equipped with forced-draught fans in order to compensate for the decrease in natural draught while stack gas is cooled. In addition, pumps are used to circulate the heat transfer fluid. All of these parasitic operations require electrical power. Electrical power has unit exergy of almost 1 W/W. On the contrary, the thermal power exergy that is claimed from the low-enthalpy flue gas has much lower unit exergy. Therefore, from an exergetic point of view, the additional electrical exergy that is required to drive pumps and fans must not exceed the thermal exergy claimed. Based on the First-Law of Thermodynamics, the net energy that is saved may be positive with an apparently high coefficient of performance; however, the same generally does not hold true for the Second-Law. This is a matter of determining the optimum amount of heat to be claimed and the most rational method of utilizing this heat for maximum net exergy gain from the process, under variable outdoor conditions and the plant operations. The four main methods were compared. These are (a) electricity generation by thermoelectric generators, electricity generation with an Organic-Rankine Cycle with (b) or without (c) a heat pump, and (d) the direct use of the thermal exergy that is gained in a district energy system. The comparison of these methods shows that exergy-rationality is the best for method (b). A new analytical optimization algorithm and the exergy-based optimum control strategy were developed, which determine the optimum pump flow rate of the heat recovery system and then calculate how much forced-draft fan power is required in the stack at dynamic operating conditions. Robust design metrics were established to maximize the net exergy gain, including an exergy-based coefficient of performance. Parametric studies indicate that the exergetic approach provides a better insight by showing that the amount of heat that can be optimally recovered is much different than the values given by classical economic and energy efficiency considerations. A case study was performed for method (d), which shows that, without any exergy rationality-based control algorithm and design method, the flue gas heat recovery may not be feasible in district energy systems or any other methods of utilization of the heat recovered. The study has implications in the field, since most of the waste heat recovery units in industrial applications, which are designed based on the First-Law of Thermodynamics, result in exergy loss instead of exergy gain, and are therefore responsible for more carbon dioxide emissions. These applications must be retrofitted with new exergy-based controllers for variable speed pumps and fans with optimally selected capacities. Full article
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<p>Adaptation of a coal plant to a cogeneration system.</p>
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<p>Exergy claim with thermo-electric generator (TEG) arrays cooled with an external hydronic loop.</p>
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<p>Exergy claim by Organic-Rankine cycle (ORC) and its waste heat.</p>
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<p>Exergy claim by ORC and it’s waste heat where ORC power is then used in a Ground-source Heat Pump (GSHP).</p>
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<p>Thermal exergy recovery.</p>
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<p>Flue gas heat recovery and district energy system model.</p>
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<p>Exergy flow bar for the heat recovery of the flue gas in the stack.</p>
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<p>Variation of exergy-based coefficient of performance (<span class="html-italic">COPEX</span>) with a fluid flow rate with flue gas temperature 600 K. Note: Here Flue gas input exergy is ignored in calculating <span class="html-italic">COPEX</span>.</p>
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<p>Variation of <span class="html-italic">COPEX</span> with outdoor air temperature, <span class="html-italic">T<sub>o</sub></span>. Note: Here flue gas input exergy is included.</p>
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<p>Variation of COPEX with a fluid flow rate with flue gas temperature 500 K.</p>
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<p>Data processing and control of the pump speed.</p>
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13 pages, 2506 KiB  
Article
Characterization of Performance of Short Stroke Engines with Valve Timing for Blended Bioethanol Internal Combustion
by Kun-Ho Chen and Yei-Chin Chao
Energies 2019, 12(4), 759; https://doi.org/10.3390/en12040759 - 25 Feb 2019
Cited by 6 | Viewed by 6290
Abstract
The present study provides a feasible strategy for minimizing automotive CO2 emissions by coupling the principle of the Atkinson cycle with the use of bioethanol fuel. Motor cycles and scooters have a stroke to bore ratio of less than unity, which allows [...] Read more.
The present study provides a feasible strategy for minimizing automotive CO2 emissions by coupling the principle of the Atkinson cycle with the use of bioethanol fuel. Motor cycles and scooters have a stroke to bore ratio of less than unity, which allows higher speeds. The expansion to compression ratio (ECR) of these engines can be altered by tuning the opening time of the intake and exhaust valves. The effect of ECR on fuel consumption and the feasibility of ethanol fuels are still not clear, especially for short stroke engines. Hence, in this study, the valve timing of a short stroke engine was tuned in order to explore potential bioethanol applications. The effect of valve timing on engine performance was theoretically and experimentally investigated. In addition, the application of ethanol/gasoline blended fuels, E3, E20, E50, and E85, were examined. The results show that consumption, as well as engine performance of short stroke motorcycle engines, can be improved by correctly setting the valve controls. In addition, ethanol/gasoline blended fuel can be used up to a composition of 20% without engine modification. The ignition time needs to be adjusted in fuel with higher compositions of blended ethanol. The fuel economy of a short stroke engine cannot be sharply improved using an Atkinson cycle, but CO2 emissions can be reduced using ethanol/gasoline blended fuel. The present study demonstrates the effect of ECR on the performance of short stroke engines, and explores the feasibility of applying ethanol/gasoline blended fuel to it. Full article
(This article belongs to the Special Issue Cleaner Combustion)
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<p>p-v and T-s diagram of Otto cycle and Atkinson cycle.</p>
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<p>Single-cylinder engine mode.</p>
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<p>Single-cylinder engine model.</p>
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<p>Comparison of measured and theoretically estimated brake specific fuel consumption (BSFC) for different valve settings.</p>
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<p>(<b>a</b>) Heat release rate; (<b>b</b>) Total heat release for different valve settings.</p>
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<p>Power and torque output for different valve settings.</p>
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<p>Emissions of CO, HC, and NO for different valve settings.</p>
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<p>Estimated and measured BSFC for ethanol/gasoline blended fuel.</p>
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<p>Power (KW) / torque(N-m) t for ethanol/gasoline blended fuel.</p>
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<p>Emissions of CO, HC, and NO for ethanol/gasoline blended fuel.</p>
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12 pages, 12790 KiB  
Article
Study on the Cooling Effect of Attached Fins on PV Using CFD Simulation
by Jaemin Kim and Yujin Nam
Energies 2019, 12(4), 758; https://doi.org/10.3390/en12040758 - 25 Feb 2019
Cited by 39 | Viewed by 7628
Abstract
The issue of efficiency decrease according to temperature increase is a pending problem in the PV market. Several active and passive technologies have been suggested but few quantitative studies on the estimation of the cooling effect have been carried out. In this study, [...] Read more.
The issue of efficiency decrease according to temperature increase is a pending problem in the PV market. Several active and passive technologies have been suggested but few quantitative studies on the estimation of the cooling effect have been carried out. In this study, a CFD (computational fluid dynamics) simulation model was developed to analyze a passive cooling technology using fins attached to the back of the PV module. Furthermore, a method to improve airflow at the back of the PV module by forming slits in the frame was analyzed. The simulation model reproduced the indoor test that uses a solar simulator and the cooling performance was analyzed according to the shape of the fins and the presence of slits. In the simulation results, the surface temperature and expected electrical efficiency without cooling were 62.78 °C and 13.24% respectively under nominal operating cell temperature conditions. Moreover, the temperature reduced by approximately 15.13 °C because the fins attached at the bottom of the PV module increased the heat transfer area with airflow. Thus, the electrical efficiency according to the PV module temperature was predicted as 14.39%. Furthermore, when slits were installed between the fins, they increased the airflow velocity and accelerated the formation of turbulence, thereby improving the cooling performance of the fins. The simulation results showed that the temperature could be further reduced by approximately 8.62 °C at a lower air velocity. As the fins and slits can also reduce the non-uniformity of the temperature, they are expected to supplement the efficiency and durability reduction of the PV modules caused by the hot spot phenomenon. In addition, it was shown that slits in the frame could further improve the cooling performance of the fins at a low-velocity airflow. Full article
(This article belongs to the Special Issue Photovoltaic Modules)
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Graphical abstract

Graphical abstract
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<p>Global annual and total solar PV installed capacity (2007–2017) [<a href="#B4-energies-12-00758" class="html-bibr">4</a>].</p>
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<p>The effect of cell temperature on PV module performance [<a href="#B8-energies-12-00758" class="html-bibr">8</a>].</p>
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<p>Solar simulator for indoor test (International Eletrotechnical Commission standard).</p>
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<p>Schematic diagram of the simulation model.</p>
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<p>The configuration of fins and slits.</p>
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<p>Temperature distribution of the case without cooling.</p>
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<p>Velocity distribution of module bottom (the case without cooling).</p>
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<p>Velocity distribution of the cases with cooling.</p>
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<p>Temperature distribution of the cases with cooling.</p>
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<p>Variation of PV temperature as a function of fins.</p>
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<p>Variation of PV temperature as a function of slits (Length: 30 mm, Number: 10EA).</p>
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<p>Schematic view of airflow around a diffuser [<a href="#B20-energies-12-00758" class="html-bibr">20</a>].</p>
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<p>Vector of velocity with and without the slits.</p>
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<p>Variation of the cell temperature as a function of air velocity.</p>
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<p>Variation of electrical efficiency as a function of PV temperature.</p>
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15 pages, 3418 KiB  
Article
Accurate and Efficient Estimation of Lithium-Ion Battery State of Charge with Alternate Adaptive Extended Kalman Filter and Ampere-Hour Counting Methods
by Zhongxiao Liu, Zhe Li, Jianbo Zhang, Laisuo Su and Hao Ge
Energies 2019, 12(4), 757; https://doi.org/10.3390/en12040757 - 25 Feb 2019
Cited by 62 | Viewed by 4933
Abstract
State of charge (SOC) estimation is a key issue in battery management systems. The challenge lies in balancing the trade-off between accuracy and computation cost. To this end, we propose an alternate method by combining the ampere-hour integral (AHI) method which has low [...] Read more.
State of charge (SOC) estimation is a key issue in battery management systems. The challenge lies in balancing the trade-off between accuracy and computation cost. To this end, we propose an alternate method by combining the ampere-hour integral (AHI) method which has low computation cost, and the adaptive extended Kalman filter (AEKF) method, which has high accuracy. The technical viability of this alternate method is verified on a LiMnO2-LiNiO2 battery module with a nominal capacity of 130 Ah under the New European Driving Cycle (NEDC) condition. Drifts in current and voltage measurement are considered. The experimental results show that the absolute SOC error using the AHI method monotonously increases from 0% to 7.2% with the computation time of 10 s while the calculation time is obtained on a ThinkPad E450 PC with an Intel Core i7-5500U CPU @2.40 GHz and 16.0 GB RAM. The absolute SOC error of the AEKF method maintains within 3.5% with the computation time of 49 s. Therefore, the alternate method almost maintains the same SOC accuracy compared to the AEKF method which reduces the maximum absolute SOC error by 50% compared to the AHI method. Therefore, the alternate method almost has the same computation time compared with the AHI method which reduces the computation time by nearly 75% compared to the AEKF method. Full article
(This article belongs to the Special Issue Progresses in Advanced Research on Intelligent Electric Vehicles)
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<p>The Thevenin model for a lithium-ion cell.</p>
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<p>OCV-SOC relationship.</p>
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<p>Current step method for model parameterization.</p>
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<p>Model parameters of the battery module as a function of SOC.</p>
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<p>State flow of the AEKF method for SOC estimation.</p>
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<p>Flowchart of the proposed approach for SOC estimation.</p>
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<p>SOC estimation error and <span class="html-italic">L</span><sub>ks</sub><span class="html-italic">(k)</span> in the process of SOC estimation by AEKF: the red line represents the SOC estimation error and the blue line represents the SOC correction parameter <span class="html-italic">L</span><sub>ks</sub>.</p>
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<p>SOC estimation process and errors using alternate method with ASCL and ADSCL of different values.</p>
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<p>SOC estimation with voltage drift of +6 mV and current drift of −8% under different transition conditions.</p>
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<p>MAE and the upper and down limitation as a function of switching number: n.</p>
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<p>NEDC profiles.</p>
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<p>SOC estimation error with voltage and current drifts.</p>
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<p>SOC estimation results obtained using three methods.</p>
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<p>SOC estimation results obtained using three methods.</p>
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28 pages, 10502 KiB  
Article
Optimal Planning of Integrated Energy Systems for Offshore Oil Extraction and Processing Platforms
by Anan Zhang, Hong Zhang, Meysam Qadrdan, Wei Yang, Xiaolong Jin and Jianzhong Wu
Energies 2019, 12(4), 756; https://doi.org/10.3390/en12040756 - 24 Feb 2019
Cited by 26 | Viewed by 6355
Abstract
With the introduction of new technologies, such as waste heat recovery units (WHRU), associated gas utilization, the energy flow coupling relationship is further deepened within the energy system of the offshore oil and gas production platform. Besides, the energy system is closely linked [...] Read more.
With the introduction of new technologies, such as waste heat recovery units (WHRU), associated gas utilization, the energy flow coupling relationship is further deepened within the energy system of the offshore oil and gas production platform. Besides, the energy system is closely linked with the oil and gas production system, and a closed-loop relationship between energy flow and material flow can be revealed. Uncertainties of energy supply and production process may lead to system-wide fluctuations, which threaten the stable operation of the platform. Therefore, an optimal planning model of integrated energy system for offshore oil and gas production platform is proposed in this paper. Firstly, a generalized energy and material flow model is proposed, three matrixes are defined based on laws of thermodynamics, including energy matrix, process matrix and feedback matrix. Secondly, the energy-material conversion relationship between the energy system and production system of a typical offshore oil and gas platform is quantitatively described, together with the coupling between the input and output of the two systems. Thirdly, considering the energy-material balance constraints and the uncertainties of production system, a multi-objective stochastic planning model for the offshore integrated energy system is established, which takes economics and environmental protection into consideration. A Monte Carlo simulation-based NSGA-II algorithm is proposed to solve the model. Finally, the validity and feasibility of the proposed methodology are demonstrated through an offshore oil and gas platform in Bohai, China. Compared with the traditional planning method, the total cost and CO2 emissions of the proposed method are reduced by 18.9% and 17.3%, respectively. Full article
(This article belongs to the Section B: Energy and Environment)
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<p>The structure of the proposed IESs for offshore oil platforms.</p>
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<p>Illustration of Generalized Energy and Material Flow Model.</p>
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<p>A generalised framework of an EMCE.</p>
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<p>Energy and Emission Flow Mapping of IESs.</p>
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<p>Schematic diagram of OEPS.</p>
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<p>The flow chart of multi-objective stochastic optimization.</p>
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<p>Estimated curve of an oil platform in the Bohai Sea in the coming 20 years (<b>a</b>) electric and thermal load demands; (<b>b</b>) associated gas production.</p>
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<p>Analysis of IESs sensitivity under maximum reference load in 2026 (<b>a</b>) annual total cost; (<b>b</b>) annual carbon dioxide emissions.</p>
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<p>Data samples of correlation between random variables at maximum reference load in 2026: (<b>a</b>) associated gas production and electric load; (<b>b</b>) associated gas production and heat load; (<b>c</b>) heat load and electric load.</p>
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<p>Comparison of results from the three methods.</p>
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<p>Results from Method 3 under maximum reference load.</p>
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<p>Dispatch of associated gas in the three methods.</p>
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<p>Process flowsheets of <span class="html-italic">DM</span>.</p>
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<p>Process flowsheets of <span class="html-italic">CR-sep</span>.</p>
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<p>Process flowsheets of <span class="html-italic">CR-oil</span>.</p>
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<p>Process flowsheets of <span class="html-italic">NG-tr</span>.</p>
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<p>Process flowsheets of <span class="html-italic">NG-co</span>.</p>
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<p>Process flowsheets of <span class="html-italic">WT</span>.</p>
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<p>Process flowsheets of <span class="html-italic">LQ</span>.</p>
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21 pages, 11304 KiB  
Article
Techno-Economic Assessment of Turboexpander Application at Natural Gas Regulation Stations
by Szymon Kuczyński, Mariusz Łaciak, Andrzej Olijnyk, Adam Szurlej and Tomasz Włodek
Energies 2019, 12(4), 755; https://doi.org/10.3390/en12040755 - 24 Feb 2019
Cited by 14 | Viewed by 6586
Abstract
During the natural gas pipeline transportation process, gas stream pressure is reduced at natural gas regulation stations (GRS). Natural gas pressure reduction is accompanied by energy dissipation which results in irreversible exergy losses in the gas stream. Energy loss depends on the thermodynamic [...] Read more.
During the natural gas pipeline transportation process, gas stream pressure is reduced at natural gas regulation stations (GRS). Natural gas pressure reduction is accompanied by energy dissipation which results in irreversible exergy losses in the gas stream. Energy loss depends on the thermodynamic parameters of the natural gas stream on inlet and outlet gas pressure regulation and metering stations. Recovered energy can be used for electricity generation when the pressure regulator is replaced with an expander to drive electric energy generation. To ensure the correct operation of the system, the natural gas stream should be heated, on inlet to expander. This temperature should be higher than the gas stream during choking in the pressure regulator. The purpose of this research was to investigate GRS operational parameters which influence the efficiency of the gas expansion process and to determine selection criteria for a cost-effective application of turboexpanders at selected GRS, instead of pressure regulators. The main novelty presented in this paper shows investigation on discounted payback period (DPP) equation which depends on the annual average natural gas flow rate through the analyzed GRS, average annual level of gas expansion, average annual natural gas purchase price, average annual produced electrical energy sale price and CAPEX. Full article
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<p>Scheme of the natural gas Reducing and Metering Station (without turboexpander). 1—Valve; 2—Filter; 3—Turbine gas meter; 4—Ultrasound gas meter; 5—Heat exchanger; 6—Shut down valve; 7—Pressure regulator; 8—Pressure drop valve; 9—Regulation valve; 10—Ventilation valve; 11—Gas odorizer.</p>
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<p>Schemes of Reducing and Metering Station (with turboexpander)<b>.</b> 1—Valve; 2—Filter; 3—Turbine gas meter; 4—Ultrasound gas meter; 5—Heat exchanger; 6—Shut down valve; 7—Pressure regulator; 8—Pressure drop valve; 9—Regulation valve; 10—Ventilation valve; 11—Gas odorizer; 12—Turboexpander; 13—Generator.</p>
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<p>Relationship between the ratio of real and minimal efficiency vs. the ratio of real and nominal gas flow.</p>
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<p>Natural gas flow and pressure at regulation stations GRS #1 (before expansion) over a period of one year.</p>
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<p>Natural gas flow and pressure at gas regulation stations (GRS) #2 (before expansion) over a period of one year.</p>
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<p>Natural gas flow and pressure at regulation stations GRS #3 (before expansion) over a period of one year.</p>
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<p>Natural gas flow and at pressure regulation stations GRS #5 (before expansion) over a period of one year.</p>
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<p>Generated electrical energy and heat demand at GRS #1 over a period of one year.</p>
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<p>Expander efficiency for GRS #1 over a period of one year.</p>
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<p>Generated electrical energy and heat demand at GRS #2 over a period of one year.</p>
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<p>Expander efficiency for GRS #2 over a period of one year.</p>
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<p>Generated electrical energy and heat demand at GRS #3 over a period of one year.</p>
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<p>Expander efficiency for GRS #3 over a period of one year.</p>
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<p>Generated electrical energy and heat demand at GRS #5 over a period of one year.</p>
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<p>Expander efficiency for GRS #5 over a period of one year.</p>
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<p>Discounted Payback Period (<span class="html-italic">Y<sub>j</sub></span>) vs. individual independent parameter (<span class="html-italic">X<sub>i</sub></span>).</p>
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20 pages, 5274 KiB  
Article
Power Flow Analysis of the Advanced Co-Phase Traction Power Supply System
by Xiaoqiong He, Haijun Ren, Jingying Lin, Pengcheng Han, Yi Wang, Xu Peng and Zeliang Shu
Energies 2019, 12(4), 754; https://doi.org/10.3390/en12040754 - 24 Feb 2019
Cited by 9 | Viewed by 4988
Abstract
The development of the traction power supply system (TPSS) is limited by the existence of the neutral section in the present system. The advanced co-phase traction power supply system (ACTPSS) can reduce the neutral section completely and becomes an important research and development [...] Read more.
The development of the traction power supply system (TPSS) is limited by the existence of the neutral section in the present system. The advanced co-phase traction power supply system (ACTPSS) can reduce the neutral section completely and becomes an important research and development direction of the railway. To ensure the stable operation of ACTPSS, it is necessary to carry out an appropriate power analysis. In this paper, the topology of advanced co-phase traction substation is mainly composed by the three-phase to single-phase cascaded converter. Then, the improved PQ decomposition algorithm is proposed to analyze the power flow. The impedance model of the traction network is calculated and established. The power flow analysis and calculation of the ACTPSS with different locations of locomotive are carried out, which theoretically illustrates that the system can maintain stable operation under various working conditions. The feasibility and operation stability of the ACTPSS are verified by the simulations and low power experiments. Full article
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<p>Traction power supply system. (<b>left</b>) The existing power supply substation, (<b>right</b>) the co-phase power supply substation based on active power compensators (APC).</p>
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<p>The structure of the advanced co-phase traction power supply system (ACTPSS).</p>
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<p>The control strategy and modulation strategy of the three-phase three-level neutral point clamped (3L-NPC) rectifier.</p>
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<p>The control strategy and modulation strategy of single-phase 3L-NPC cascaded inverter.</p>
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<p>The original circuit model of the traction network.</p>
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<p>The simplified impedance model of the traction network.</p>
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<p>The models of the traction network. (<b>a</b>) The impedance model of the traction network; (<b>b</b>) the parallel equivalent impedance model of the traction network; (<b>c</b>) the simplified equivalent impedance model of the traction network.</p>
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<p>The equivalent mathematic model of ACTPSS.</p>
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<p>The equivalent model of ACTPSS.</p>
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<p>The model of ACTPSS with two traction substation.</p>
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<p>The relationship between the location of the locomotive and the output power ratio of the traction substation.</p>
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<p>The output voltage waves of three three-phase rectifiers.</p>
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<p>The output voltage and current waves of 3L-NPC cascaded inverter. (<b>a</b>) The output voltage and current wave of the three-model 3L-NPC cascaded inverter after filter; (<b>b</b>) the output voltage waves of the three single-phase 3L-NPC inverter and the output voltage of 3L-NPC cascaded inverter.</p>
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<p>The current waves of the traction substations and locomotives in 0–3.5 s.</p>
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<p>The voltage waves of the traction substations and the locomotives in 0–3.5 s.</p>
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<p>The current waves of the traction substations and locomotives in 3.5–7 s.</p>
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<p>The voltage waves of the traction substations and locomotives in 3.5–7 s.</p>
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<p>The output active and reactive power of three traction substations.</p>
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<p>The output voltage waves of the three-model 3L-NPC cascaded converter. (<b>a</b>) The relationship of the output voltage waves; (<b>b</b>) the output voltage waves in about one period (CH1: the output voltage of cascaded converter; CH2: the voltage of the inverter 1; CH3: the voltage of the inverter 2; CH4: the voltage of the inverter 3).</p>
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<p>The output current waves of the three parallel traction substations and the load voltage wave. (<b>a</b>) The waves under the adjusting state and stable state; (<b>b</b>) the relationship between the current waves and the load voltage wave under the stable state (CH1: the output current of the SS1; CH2: the output current of the SS2; CH3: the output current of the SS3; CH4: the voltage of load.).</p>
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20 pages, 4816 KiB  
Article
Adaptive Gains Control Scheme for PMSG-Based Wind Power Plant to Provide Voltage Regulation Service
by Jianfeng Dai, Yi Tang and Jun Yi
Energies 2019, 12(4), 753; https://doi.org/10.3390/en12040753 - 24 Feb 2019
Cited by 8 | Viewed by 3339
Abstract
High-penetration wind power will count towards a significant portion of future power grid. This significant role requires wind turbine generators (WTGs) to contribute to voltage and reactive power support. The maximum reactive power capacity (MRPC) of a WTG depends on its current input [...] Read more.
High-penetration wind power will count towards a significant portion of future power grid. This significant role requires wind turbine generators (WTGs) to contribute to voltage and reactive power support. The maximum reactive power capacity (MRPC) of a WTG depends on its current input wind speed, so that the reactive power regulating ability of the WTG itself and adjacent WTGs are not necessarily identical due to the variable wind speed and the wake effect. This paper proposes an adaptive gains control scheme (AGCS) for a permanent magnet synchronous generator (PMSG)-based wind power plant (WPP) to provide a voltage regulation service that can enhance the voltage-support capability under load disturbance and various wind conditions. The droop gains of the voltage controller for PMSGs are spatially and temporally dependent variables and adjusted adaptively depending on the MRPC which are a function of the current variable wind speed. Thus, WTGs with lower input wind speed can provide greater reactive power capability. The proposed AGCS is demonstrated by using a PSCAD/EMTDC simulator. It can be concluded that, compared with the conventional fixed-gains control scheme (FGCS), the proposed method can effectively improve the voltage-support capacity while ensuring stable operation of all PMSGs in WPP, especially under high wind speed conditions. Full article
(This article belongs to the Section F: Electrical Engineering)
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<p>A typical configuration of the permanent magnet synchronous generator (PMSG) model.</p>
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<p>Control strategy of grid-side converter.</p>
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<p>Active and reactive power range of the PMSG.</p>
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<p>Conventional fixed-gain voltage control scheme of a PMSG.</p>
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<p>Proposed adaptive-gain voltage control scheme of a PMSG.</p>
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<p>Test system used in this paper.</p>
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<p>IEEE alternator supplied rectifier excitation system model.</p>
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<p>Maximum reactive power capacity (MRPC) of the all PMSGs in case 1.</p>
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<p>Results of Case 1. (<b>a</b>) Voltage at PCC, (<b>b</b>) reactive power of PMSGs under the conventional FGCS, (<b>c</b>) reactive power of PMSGs under the proposed AGCS.</p>
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<p>MRPC of the all PMSGs in case 2.</p>
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<p>Results of Case 2. (<b>a</b>) Voltage at PCC, (<b>b</b>) reactive power of PMSGs under the conventional FGCS, (<b>c</b>) reactive power of PMSGs under the proposed AGCS.</p>
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<p>Results of Case 3. (<b>a</b>) Wind speed, (<b>b</b>) voltage at PCC, (<b>c</b>) reactive power of PMSGs under the conventional FGCS, (<b>d</b>) adaptive gain of PMSGs, (<b>e</b>) reactive power of PMSGs under the proposed AGCS.</p>
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<p>Results of Case 3. (<b>a</b>) Wind speed, (<b>b</b>) voltage at PCC, (<b>c</b>) reactive power of PMSGs under the conventional FGCS, (<b>d</b>) adaptive gain of PMSGs, (<b>e</b>) reactive power of PMSGs under the proposed AGCS.</p>
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<p>Results of Case 4. (<b>a</b>) Wind speed, (<b>b</b>) voltage at PCC, (<b>c</b>) reactive power of PMSGs under the conventional FGCS, (<b>d</b>) adaptive gain of PMSGs, (<b>e</b>) reactive power of PMSGs under the proposed AGCS.</p>
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<p>Results of Case 4. (<b>a</b>) Wind speed, (<b>b</b>) voltage at PCC, (<b>c</b>) reactive power of PMSGs under the conventional FGCS, (<b>d</b>) adaptive gain of PMSGs, (<b>e</b>) reactive power of PMSGs under the proposed AGCS.</p>
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<p>Results of Case 5. (<b>a</b>) Real pattern of wind speed, (<b>b</b>) voltage at PCC, (<b>c</b>) adaptive gain of PMSGs, (<b>d</b>) reactive power of PMSGs under the proposed AGCS.</p>
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<p>Results of Case 5. (<b>a</b>) Real pattern of wind speed, (<b>b</b>) voltage at PCC, (<b>c</b>) adaptive gain of PMSGs, (<b>d</b>) reactive power of PMSGs under the proposed AGCS.</p>
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15 pages, 2703 KiB  
Article
Determining Soil-Water Characteristic Curves from Mercury Intrusion Porosimeter Test Data Using Fractal Theory
by Gaoliang Tao, Yin Chen, Henglin Xiao, Qingsheng Chen and Juan Wan
Energies 2019, 12(4), 752; https://doi.org/10.3390/en12040752 - 24 Feb 2019
Cited by 20 | Viewed by 3816
Abstract
Accurate determination of soil-water characteristic curve (SWCC) is of immense importance for understanding the mechanical behavior of unsaturated soils. Due to the difficulty and long duration of experimental procedures, it is of great significance to estimate the SWCC by indirect methods. To address [...] Read more.
Accurate determination of soil-water characteristic curve (SWCC) is of immense importance for understanding the mechanical behavior of unsaturated soils. Due to the difficulty and long duration of experimental procedures, it is of great significance to estimate the SWCC by indirect methods. To address this issue, in this article an effective fractal method is proposed for predicting the SWCC based on mercury intrusion porosimeter (MIP) data. Only two characteristic parameters, namely the fractal dimension and air-entry value, are needed in the presented approach. Detailed procedures for determining the parameters are clearly elaborated. Due to the influence of sample size difference on the equivalent connected pore size, a sample scale effect coefficient is proposed to predict air-entry values. The concept of “critical pore size” is introduced to obtain the optimal fractal dimension, which can accurately reflect the fractal behaviour of SWCC samples. By comparisons between predicted and experimental SWCCs, the validation of the proposed method is verified. The comparisons reveal the good agreement between the proposed approach and laboratory experiments. Full article
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<p>Schematic diagram of an air-water interface and a mercury-air interface. (<b>a</b>) air-water interface; (<b>b</b>) mercury-air interface.</p>
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<p>The influence of parameters on SWCC: (<b>a</b>) fractal dimension, (<b>b</b>) air-entry value.</p>
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<p>Diagram of the sample scale effect for the equivalent connected pore size. (<b>a</b>) ichnography for two layers; (<b>b</b>) ichnography for three layers; (<b>c</b>) cross section for two layers and (<b>d</b>) cross section for three layers.</p>
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<p>Diagram of the sample scale effect for the equivalent connected pore size. (<b>a</b>) ichnography for two layers; (<b>b</b>) ichnography for three layers; (<b>c</b>) cross section for two layers and (<b>d</b>) cross section for three layers.</p>
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<p>The experimental data of MIP tests.</p>
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<p>The cumulative pore volume curves of different dry densities.</p>
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<p>Determination of fractal dimension <span class="html-italic">D.</span> (<b>a</b>) neglecting “critical pore size”; (<b>b</b>) considering “critical pore size”.</p>
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<p>Comparison between experimental results and predicted SWCCs from Equation (15) and Equation (10).</p>
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<p>Comparison between experimental results and predicted SWCCs from Equation (15) and Equation (10).</p>
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<p>Comparison between experimental results and predicted SWCCs from Equation (15) and Equation (10).</p>
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20 pages, 8617 KiB  
Article
Design and Control of Coupled Inductor DC–DC Converters for MVDC Ship Power Systems
by Flavio Balsamo, Davide Lauria and Fabio Mottola
Energies 2019, 12(4), 751; https://doi.org/10.3390/en12040751 - 24 Feb 2019
Cited by 6 | Viewed by 4022
Abstract
This paper deals with the design and control aspects of modern ship power systems within the paradigm of an all-electric ship. The widespread use of power electronic converters is central in this context due to the technological advances in automation systems and the [...] Read more.
This paper deals with the design and control aspects of modern ship power systems within the paradigm of an all-electric ship. The widespread use of power electronic converters is central in this context due to the technological advances in automation systems and the integration of the electrical propulsion systems and other components, such as electrical energy storage systems and renewable energy sources. The issue to address in this scenario is related to the request of increased performances in dynamic operation while pursuing advantages in terms of energy savings and overall system security. In addition, the presence of large load changes requires providing robustness of the control in terms of system stability. This paper is focused on medium voltage direct current (MVDC) ship power systems and the design and control of coupled inductor DC–DC converters. The load is handled in terms of a constant power model, which generally is considered the most critical case for testing the stability of the system. The robustness of the design procedure, which is verified numerically against large and rapid load variations, allowed us to confirm the feasibility and the attractiveness of the design and the control proposal. Full article
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<p>DC ship power system (DG: diesel generator, RES: renewable energy source, BESS: battery energy storage system, LVAC: low voltage alternating current).</p>
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<p>Full-bridge bidirectional converter.</p>
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<p>Coupled inductor DC–DC converter.</p>
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<p><span class="html-italic">N<sub>opt</sub></span> and <span class="html-italic">D<sub>ref</sub></span> vs. <span class="html-italic">k</span> over the interval <span class="html-italic">k</span> ∈ [2÷10].</p>
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<p>Coupled inductor DC–DC converter in boost mode during (<b>a</b>) <span class="html-italic">T<sub>on</sub></span> and (<b>b</b>) <span class="html-italic">T<sub>off</sub></span>.</p>
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<p>Coupled inductor DC–DC converter in boost mode: voltages and currents.</p>
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<p>Qualitative time evolution of the function <span class="html-italic">S</span>(<b>x</b>,<b>z</b>).</p>
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<p>Architecture of the control strategy.</p>
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<p>The medium voltage direct current (MVDC) ship electrical system under study.</p>
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<p>Output voltage dynamic behavior (case A).</p>
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<p>Magnetizing current (case A).</p>
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<p>Current in inductor <span class="html-italic">L</span><sub>1</sub> (case A).</p>
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<p>Current in inductor <span class="html-italic">L</span><sub>2</sub> (case A).</p>
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<p>Error between the actual magnetizing current and the estimated current (case A).</p>
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<p>Dynamic behavior of the output voltage (case B).</p>
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<p>Magnetizing current dynamic behavior (case B).</p>
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<p>Dynamic behavior of the <span class="html-italic">L</span><sub>1</sub> current (case B).</p>
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<p>Dynamic behavior of the <span class="html-italic">L</span><sub>2</sub> current (case B).</p>
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<p>Error between the actual magnetizing current and the estimated current (case B).</p>
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17 pages, 4957 KiB  
Article
Dynamic Emulation of a PEM Electrolyzer by Time Constant Based Exponential Model
by Damien Guilbert and Gianpaolo Vitale
Energies 2019, 12(4), 750; https://doi.org/10.3390/en12040750 - 24 Feb 2019
Cited by 81 | Viewed by 10159
Abstract
The main objective of this paper is to develop a dynamic emulator of a proton exchange membrane (PEM) electrolyzer (EL) through an equivalent electrical model. Experimental investigations have highlighted the capacitive effect of EL when subjecting to dynamic current profiles, which so far [...] Read more.
The main objective of this paper is to develop a dynamic emulator of a proton exchange membrane (PEM) electrolyzer (EL) through an equivalent electrical model. Experimental investigations have highlighted the capacitive effect of EL when subjecting to dynamic current profiles, which so far has not been reported in the literature. Thanks to a thorough experimental study, the electrical domain of a PEM EL composed of 3 cells has been modeled under dynamic operating conditions. The dynamic emulator is based on an equivalent electrical scheme that takes into consideration the dynamic behavior of the EL in cases of sudden variation in the supply current. The model parameters were identified for a suitable current interval to consider them as constant and then tested with experimental data. The obtained results through the developed dynamic emulator have demonstrated its ability to accurately replicate the dynamic behavior of a PEM EL. Full article
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<p>Proton exchange membrane (PEM) water electrolysis reactions. In the anode, the water is divided into protons and oxygen providing electrons; in the cathode, the protons combine with electrons coming from the terminal at negative potential, obtaining hydrogen.</p>
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<p>Equivalent electric scheme of the PEM electrolyzer (EL).</p>
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<p>Developed experimental set up with the PEM EL: (1) DC power supply, (2) digital oscilloscope, (3) current clamp, (4) PEM EL stack, (5) digital multimeter, (6) dSPACE board, (7) pressurized pure water tank.</p>
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<p>Demonstration of the capacitive effect of the EL. Channel 1: EL voltage (2 V.div<sup>−1</sup>), channel 2: EL current (2 A.div<sup>−1</sup>), time: 10 s.div<sup>−1</sup>.</p>
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<p>Operating limits of the PEM EL. Channel 1: EL voltage (2 V.div<sup>−1</sup>), channel 2: EL current (2 A.div<sup>−1</sup>), time: 10 s.div<sup>−1</sup>.</p>
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<p>Example of voltage transient.</p>
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<p>Static characteristic obtained by linear regression and experimental measurements.</p>
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<p>Input power vs. the current density supplied to the PEM EL.</p>
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<p>Zoom of the transient with exponential curves.</p>
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<p>Upper limit of the efficiency for the PEM EL.</p>
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<p>Upper limit of the of hydrogen production vs. current density.</p>
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<p>Experimental and estimated temperature of the PEM EL.</p>
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<p>Comparison among the PEM EL voltage: experimental, obtained by dynamic model and by static model.</p>
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<p>Error percentage obtained comparing the experimental data with the dynamic model (<b>top</b>) and the static model (<b>bottom</b>).</p>
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<p>Voltage drop into the cathode, into the anode and into the membrane together with the supply current.</p>
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<p>Power balance of the PEM EL.</p>
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29 pages, 1796 KiB  
Article
Inter-Criteria Dependencies-Based Decision Support in the Sustainable wind Energy Management
by Paweł Ziemba
Energies 2019, 12(4), 749; https://doi.org/10.3390/en12040749 - 24 Feb 2019
Cited by 44 | Viewed by 4764
Abstract
Decision problems related to the wind energy require considering many, often interrelated and dependent on each other, criteria. To solve such problems, decision systems based on Multi-Criteria Decision Analysis (MCDA) methods are usually used. Unfortunately, most methods assume independence between the criteria, therefore, [...] Read more.
Decision problems related to the wind energy require considering many, often interrelated and dependent on each other, criteria. To solve such problems, decision systems based on Multi-Criteria Decision Analysis (MCDA) methods are usually used. Unfortunately, most methods assume independence between the criteria, therefore, their application in decision problems related to the wind energy is debatable. This paper presents the use of the Analytic Network Process (ANP) method to solve a decision problem consisting in selecting the location and design of a wind farm. The use of the ANP method allows capturing the complexity of the decision problem by taking into consideration dependencies between criteria. As part of the verification of the solution, the results of the ANP method were compared with those of the Analytic Hierarchy Process (AHP) method, which uses only hierarchical dependencies between criteria. The conducted verification showed that the inter-criteria dependencies may have a significant influence on the obtained solution. On the basis of the conducted sensitivity analysis and the research into robustness of the rankings to the rank reversal phenomenon, it has been found out that the ranking obtained with the use of the ANP is characterized by a higher quality than by means of the AHP. Full article
(This article belongs to the Special Issue Assessment of Energy–Environment–Economy Interrelations)
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<p>Network structure in the ANP method.</p>
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<p>Research procedure</p>
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<p>Decision model with alternatives and dependencies between sub-criteria</p>
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<p>Utility of alternatives determined by means of: (<b>a</b>) the AHP method; (<b>b</b>) the ANP method; depending on the weight of the criterion C1 and sub-criterion C1.1.</p>
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<p>The number of changed rankings for the alternative A5 generated: (<b>a</b>) without considering dependencies between sub-criteria; (<b>b</b>) when taking into account dependencies between sub-criteria</p>
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17 pages, 2834 KiB  
Article
Effect of Salts on Interfacial Tension and CO2 Mass Transfer in Carbonated Water Injection
by Aly A Hamouda and Nikhil Bagalkot
Energies 2019, 12(4), 748; https://doi.org/10.3390/en12040748 - 24 Feb 2019
Cited by 13 | Viewed by 6321
Abstract
Carbonated water injection (CWI) is a promising enhanced oil recovery (EOR) and CO2 sequestration method, which overcomes the problems associated with CO2 EOR. CO2 mass transfer and interfacial tension (IFT) are important parameters that influence oil recovery efficiency. This study [...] Read more.
Carbonated water injection (CWI) is a promising enhanced oil recovery (EOR) and CO2 sequestration method, which overcomes the problems associated with CO2 EOR. CO2 mass transfer and interfacial tension (IFT) are important parameters that influence oil recovery efficiency. This study addresses the impact of MgCl2 and Na2SO4 in carbonated water (CW) on CW/hydrocarbon IFT and CO2 mass transfer. An axisymmetric drop shape analysis was used to estimate the IFT and the CO2 diffusion coefficient. It was found that CW+MgCl2 reduced both the CW/n-decane IFT (36.5%) and CO2 mass transfer, while CW+Na2SO4 increased both the IFT and CO2 mass transfer (57%). It is suggested that reduction in IFT for CW+MgCl2 brine is mainly due to the higher hydration energy of Mg2+. The Mg2+ ion forms a tight bond to the first hydration shell [Mg(H2O)6]2+, this increases the effective size at the interface, hence reduce IFT. Meanwhile, the SO42− outer hydration shell has free OH groups, which may locally promote CO2 mass transfer. The study illustrates the potential of combining salts and CW in enhancing CO2 mass transfer that can be the base for further investigations. Furthermore, the contribution and proposed mechanisms of the different ions (SO42− and Mg2+) to the physical process in carbonated water/hydrocarbon have been addressed, which forms one of primary bases of EOR. Full article
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<p>Pictorial representation of sweep front for the case of (<b>a</b>) CO<sub>2</sub> flooding and (<b>b</b>) Carbonated water injection.</p>
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<p>(<b>a</b>) Cross-section view of the PVT cell; (<b>b</b>) Schematics of the experimental setup.</p>
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<p>Mass of CO<sub>2</sub> transferred into the n-decane drop (mole/ml) from the start of the experiment till equilibrium for 50 bar (<b>a</b>), 70 bar (<b>b</b>), 80 bar (<b>c</b>), and 100 bar (<b>d</b>).</p>
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<p>Swelling (ratio of final to initial volume) of the n-decane pendant for different carbonated brines for the pressure range of 50–100 bar at 45 °C.</p>
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<p>Effective diffusion coefficient of CO<sub>2</sub> into n-C10 from different CB and CW for pressures; 50, 70, 80, and 100 bar at 45 °C.</p>
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<p>Dynamic changes in the CB/n-decane IFT for different brine compositions at 50 bar (<b>a</b>), 70 bar (<b>b</b>), 80 bar (<b>c</b>), and 100 bar (<b>d</b>) at 45 °C.</p>
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<p>IFT as a function of CO<sub>2</sub> concentration in the n-decane.</p>
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18 pages, 9075 KiB  
Article
Experimental Study of Particle Deposition on Surface at Different Mainstream Velocity and Temperature
by Fei Zhang, Zhenxia Liu, Zhengang Liu and Yanan Liu
Energies 2019, 12(4), 747; https://doi.org/10.3390/en12040747 - 24 Feb 2019
Cited by 5 | Viewed by 3891
Abstract
The effect of mainstream velocity and mainstream temperature on the behavior of deposition on a flat plate surface has been investigated experimentally. Molten wax particles were injected to generate particle deposition in a two-phase flow wind tunnel. Tests indicated that deposition occurs mainly [...] Read more.
The effect of mainstream velocity and mainstream temperature on the behavior of deposition on a flat plate surface has been investigated experimentally. Molten wax particles were injected to generate particle deposition in a two-phase flow wind tunnel. Tests indicated that deposition occurs mainly at the leading edge and the middle and backward portions of the windward side. The mass of deposition at the leading edge was far more than that on the windward and lee sides. For the windward and lee sides, deposition mass increased as the mainstream velocity was increased for a given particle concentration. Capture efficiency was found to increase initially until the mainstream velocity reaches a certain value, where it begins to drop with mainstream velocity increasing. For the leading edge, capture efficiency followed a similar trend due to deposition spallation and detachment induced by aerodynamic shear at high velocity. Deposition formation was also strongly affected by the mainstream temperature due to its control of particle phase (solid or liquid). Capture efficiency initially increased with increasing mainstream temperature until a certain threshold temperature (near the wax melting point). Subsequently, it began to decrease, for wax detaches from the model surface when subjected to the aerodynamic force at the surface temperature above the wax melting point. Full article
(This article belongs to the Special Issue Fluid Flow and Heat Transfer)
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<p>Experimental system schematic.</p>
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<p>Photograph of the test section.</p>
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<p>Schematic of the wax spray system.</p>
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<p>Picture of the wax sprayer and turbulence generating.</p>
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<p>Three-dimensional maps of the test model and its fixing holder.</p>
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<p>Schematic of multiphase flow and angle of attack.</p>
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<p>Wax particle size distribution.</p>
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<p>Photographs of wax deposition on leading edge with different mainstream velocities.</p>
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<p>Photographs of wax deposition on windward surface with different mainstream velocities.</p>
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<p>Photographs of wax deposition on lee surface with different mainstream velocities.</p>
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<p>Deposition mass with different mainstream velocities.</p>
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<p>Capture efficiency at different mainstream velocities.</p>
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<p>Total capture efficiency in this study compared with data from Taltavull [<a href="#B31-energies-12-00747" class="html-bibr">31</a>] and Bowen [<a href="#B32-energies-12-00747" class="html-bibr">32</a>].</p>
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<p>Photographs of wax deposition on leading edge with different mainstream temperature.</p>
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<p>Photographs of wax deposition on windward surface with different mainstream temperatures.</p>
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<p>Photographs of wax deposition on lee surface with different mainstream temperatures.</p>
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<p>Deposition mass with different mainstream temperature.</p>
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<p>Capture efficiency with different mainstream temperature.</p>
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<p>Total capture efficiency herein compared to data from Crosby [<a href="#B11-energies-12-00747" class="html-bibr">11</a>] and Laycock [<a href="#B17-energies-12-00747" class="html-bibr">17</a>].</p>
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17 pages, 8513 KiB  
Article
Evaluation Model for the Scope of DC Interference Generated by Stray Currents in Light Rail Systems
by Chengtao Wang, Wei Li, Yuqiao Wang, Shaoyi Xu and Kunpeng Li
Energies 2019, 12(4), 746; https://doi.org/10.3390/en12040746 - 23 Feb 2019
Cited by 18 | Viewed by 4408
Abstract
Electrochemical corrosion caused by stray currents reduces the lifespan of buried gas pipelines and the safety of light rail systems. Determining the scope of stray current corrosion will help prevent the corrosion of existing buried pipelines and provide an effective reference for new [...] Read more.
Electrochemical corrosion caused by stray currents reduces the lifespan of buried gas pipelines and the safety of light rail systems. Determining the scope of stray current corrosion will help prevent the corrosion of existing buried pipelines and provide an effective reference for new pipeline siting. In response to this problem, in this paper the surface potential gradient was used to evaluate the scope of stray current corrosion. First, an analytical model for the scope of the stray current corrosion combined with distributed parameters and the electric field generated by a point current source was put forward. Second, exemplary calculations were conducted based on the proposed model. Sensitivity of the potential gradient was analyzed with an example of the transition resistance, and the dynamic distribution of surface potential gradient under different locomotive operation modes was also analyzed in time-domain. Finally, the scope was evaluated at four different intervals with the parameters from the field test to judge whether the protective measures need to be taken in areas with buried pipelines and light rail systems nearby or not. Full article
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Graphical abstract

Graphical abstract
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<p>Stray current in the light rail system.</p>
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<p>N-layer stratification of a geological structure.</p>
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<p>Effect of the stray current leakage on the potential near the running rail.</p>
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<p>Powered equivalent model.</p>
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<p>Calculation flow of time-domain evaluation model of DC interference generated by stray current.</p>
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<p>Surface potential gradient near the running rail under the bilateral power supply: (<b>a</b>) Along the locomotive running direction; (<b>b</b>) Vertical to the locomotive running direction.</p>
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<p>Surface potential gradient under the bilateral power supply: (<b>a</b>) Along the locomotive running direction; (<b>b</b>) Vertical to the locomotive running direction.</p>
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<p>Surface potential gradient simulated by COMSOL 5.2.</p>
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<p>Effect of transition resistance on the surface potential gradient: (<b>a</b>) Along the locomotive running direction (100 m); (<b>b</b>) Along the locomotive running direction (200 m); (<b>c</b>) Vertical to the locomotive running direction (600 m); (<b>d</b>) Position instructions.</p>
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<p>Locomotive dynamic characteristics: (<b>a</b>) Traction current; (<b>b</b>) Locomotive position.</p>
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<p>Dynamic surface potential gradient: (<b>a</b>) Acceleration mode; (<b>b</b>) Deceleration mode; (<b>c</b>) Surface potential gradient during the entire locomotive operation; (<b>d</b>) Position instructions.</p>
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<p>Sensitivity analysis considering operation modes: (<b>a</b>) Acceleration mode; (<b>b</b>) Deceleration mode; (<b>c</b>) Entire operation time; (<b>d</b>) Acceleration mode (25 s); (<b>e</b>) Deceleration mode (160 s); (<b>f</b>) Entire operation time; (<b>g</b>) Position instructions.</p>
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<p>Field test on the transition resistance and rail longitudinal resistance. (<b>Left</b>) Parameters test; (<b>Right</b>) Test box.</p>
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<p>Stray current corrosion scope: (<b>a</b>) Interval I; (<b>b</b>) Interval II; (<b>c</b>) Interval III; (<b>d</b>) Interval IV.</p>
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<p>Stray current corrosion scope simulated by COMSOL 5.2.</p>
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17 pages, 2180 KiB  
Article
Synthesis and Optimal Operation of Smart Microgrids Serving a Cluster of Buildings on a Campus with Centralized and Distributed Hybrid Renewable Energy Units
by Daniele Testi, Paolo Conti, Eva Schito, Luca Urbanucci and Francesco D’Ettorre
Energies 2019, 12(4), 745; https://doi.org/10.3390/en12040745 - 23 Feb 2019
Cited by 17 | Viewed by 4945
Abstract
Micro-district heating networks based on cogeneration plants and renewable energy technologies are considered efficient, viable and environmentally-friendly solutions to realizing smart multi-energy microgrids. Nonetheless, the energy production from renewable sources is intermittent and stochastic, and cogeneration units are characterized by fixed power-to-heat ratios, [...] Read more.
Micro-district heating networks based on cogeneration plants and renewable energy technologies are considered efficient, viable and environmentally-friendly solutions to realizing smart multi-energy microgrids. Nonetheless, the energy production from renewable sources is intermittent and stochastic, and cogeneration units are characterized by fixed power-to-heat ratios, which are incompatible with fluctuating thermal and electric demands. These drawbacks can be partially overcome by smart operational controls that are capable of maximizing the energy system performance. Moreover, electrically driven heat pumps may add flexibility to the system, by shifting thermal loads into electric loads. In this paper, a novel configuration for smart multi-energy microgrids, which combines centralized and distributed energy units is proposed. A centralized cogeneration system, consisting of an internal combustion engine is connected to a micro-district heating network. Distributed electric heat pumps assist the thermal production at the building level, giving operational flexibility to the system and supporting the integration of renewable energy technologies, i.e., wind turbines, photovoltaic panels, and solar thermal collectors. The proposed configuration was tested in a hypothetical case study, namely, a University Campus located in Trieste, Italy. The system operation is based on a cost-optimal control strategy and the effect of the size of the cogeneration unit and heat pumps was investigated. A comparison with a conventional configuration, without distributed heat pumps, was also performed. The results show that the proposed configuration outperformed the conventional one, leading to a total-cost saving of around 8%, a carbon emission reduction of 11%, and a primary energy saving of 8%. Full article
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<p>Schematic of the energy system.</p>
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<p>Average monthly temperature and daily irradiance on horizontal plane.</p>
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<p>Scale representation of the campus: buildings, district heating, and generation systems.</p>
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<p>Analyzed configuration for the reference multi-energy microgrid: (<b>a</b>) centralized, (<b>b</b>) distributed.</p>
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<p>Installation, energy, and maintenance annual costs using the optimal control strategy.</p>
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<p>Heat and power profiles in 3 weeks of the year (areas are for consumption, lines for production).</p>
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<p>Heat and power profiles in 3 weeks of the year (areas are for consumption, lines for production).</p>
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<p>Thermal energy balance (MWh/yr).</p>
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<p>Electrical energy balance (MWh/yr).</p>
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13 pages, 4192 KiB  
Article
Assessment and Possible Solution to Increase Resilience: Flooding Threats in Terni Distribution Grid
by Tommaso Bragatto, Massimo Cresta, Fabrizio Cortesi, Fabio Massimo Gatta, Alberto Geri, Marco Maccioni and Marco Paulucci
Energies 2019, 12(4), 744; https://doi.org/10.3390/en12040744 - 23 Feb 2019
Cited by 15 | Viewed by 3461
Abstract
In recent years, because of increasing frequency and magnitude of extreme weather events, the main stakeholders of electric power systems are emphasizing issues about resilience. Whenever networks are designed and development plans are drawn, this new feature must be assessed and implemented. In [...] Read more.
In recent years, because of increasing frequency and magnitude of extreme weather events, the main stakeholders of electric power systems are emphasizing issues about resilience. Whenever networks are designed and development plans are drawn, this new feature must be assessed and implemented. In this paper, a procedure to evaluate the resilience of a distribution network against flooding threats is presented. Starting from a detailed analysis about the resilience of each asset of the grid, the procedure implements the exploration of the network in order to evaluate the impact of interruptions (e.g., in terms of number of disconnected users) produced by the specific threat; then, it calculates the resilience indices of the whole system. The procedure is applied with respect to the flooding threats, on a real distribution network in the center of Italy (i.e., the distribution network of Terni). Referring to this case study, the proposed method suggests countermeasures able to reduce the impact of flooding events and evaluates their benefits. Results indicate that, at the present time, the network is adequately resilient with respect to flooding events, as demonstrated by the index values. However, the remedial actions identified by the procedure are also able to improve the resilience of the network and, in addition, they are in agreement with the development plan already established by the distribution system operator (DSO). Full article
(This article belongs to the Section F: Electrical Engineering)
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<p>Representation of simulation model.</p>
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<p>Fictitious branches representation.</p>
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<p>Flooding risk zones with respect to Terni municipality (red: Zone A; green: Zone B; yellow: Zone C).</p>
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<p>Flooding risk areas with respect to electric substations in Terni municipality.</p>
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<p>Flooding events on substation represented as NUD and equivalent return time.</p>
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<p>Statistical distribution of flooding events in terms of NUD.</p>
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<p>Flooding events on substations represented in terms of NUD and equivalent return time (ex-post evaluation).</p>
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<p>Comparison between ex-ante and ex-post impact for the first ten substations listed in <a href="#energies-12-00744-t001" class="html-table">Table 1</a>.</p>
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26 pages, 6573 KiB  
Article
Narrow Band State of Charge (SOC) Control Strategy for Hybrid Container Cranes
by Sheron Ruchiranga Anton Bolonne and Dedduwa Pathiranage Chandima
Energies 2019, 12(4), 743; https://doi.org/10.3390/en12040743 - 23 Feb 2019
Cited by 12 | Viewed by 5512
Abstract
This paper evaluates possibility of using a new hybrid system based on variable speed diesel generator (VSDG), Li-ion battery bank and supercapacitor bank (SC) for a rubber tire gantry crane (RTGC) used in container terminals. Existing commercial hybrid systems face difficulties producing high [...] Read more.
This paper evaluates possibility of using a new hybrid system based on variable speed diesel generator (VSDG), Li-ion battery bank and supercapacitor bank (SC) for a rubber tire gantry crane (RTGC) used in container terminals. Existing commercial hybrid systems face difficulties producing high efficiencies, higher life span, and lower initial investment cost due to inheriting characteristics of batteries and supercapacitors. In the proposed power system, a variable speed diesel generator act as the principal energy source, while a Li-ion battery bank and SC bank act as an energy storage system. The battery supports the diesel generator during steady demand and further, it absorbs a part of energy during regeneration. The energy management strategy, control the power flow from different sources while maintaining battery state of charge (SOC) level within a narrow band. Unlike most battery systems, this narrow band operation of battery system increases its life span while reducing capacity fade. The originality of this study can be emphasized from this narrow band SOC control technique. Simulation results for real operational load cycles are presented showing a stable system operating under defined current limits which can enhance lifetime of battery system and increase fuel saving by downsizing 400 kW constant speed diesel generator to 200 kW VSDG. Full article
(This article belongs to the Section F: Electrical Engineering)
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<p>Directions of motions of rubber tire gantry crane (RTGC) (<b>1</b>-Trolley, <b>2</b>-Hoist, <b>3</b>-Gantry).</p>
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<p>(<b>a</b>) Quite power profile; (<b>b</b>) Busy power profile.</p>
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<p>(<b>a</b>) Quite power profile; (<b>b</b>) Busy power profile.</p>
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<p>Configuration of proposed hybrid RTGC model. DG: diesel generator; SC: supercapacitor bank.</p>
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<p>Discharge characteristics of LIM40-7D cell ( Reproduced courtesy of the GS Yuasa) [<a href="#B11-energies-12-00743" class="html-bibr">11</a>].</p>
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<p>Discharge characteristics of proposed cell model.</p>
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<p>Charging characteristics of 3.0 V/3000 F SC cell of the proposed model [<a href="#B17-energies-12-00743" class="html-bibr">17</a>].</p>
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<p>Specific fuel consumption of proposed VSDG.</p>
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<p>Average-value model of DC/DC converter.</p>
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<p>VSDG architecture.</p>
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<p>State Machine Controller.</p>
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<p>SC Charge controller.</p>
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<p>SOC and current variations of Case 1.</p>
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<p>SOC and current variations of Case 2.</p>
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<p>SOC and current variations of Case 3.</p>
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<p>SOC and current variations of Case 4.</p>
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17 pages, 3779 KiB  
Article
Control Strategies of Full-Voltage to Half-Voltage Operation for LCC and Hybrid LCC/MMC based UHVDC Systems
by Gen Li, Wei Liu, Tibin Joseph, Jun Liang, Ting An, Jingjing Lu, Marcio Szechtman, Bjarne Andersen and Qikai Zhuang
Energies 2019, 12(4), 742; https://doi.org/10.3390/en12040742 - 23 Feb 2019
Cited by 4 | Viewed by 4120
Abstract
With the increasing demand of transmitting bulk-power over long-distance, the ultra high-voltage direct-current (UHVDC) transmission systems become an attractive option. Nowadays, not only the line commutated converter (LCC) based systems, but also the modular multilevel converter (MMC) based systems have reached UHVDC levels. [...] Read more.
With the increasing demand of transmitting bulk-power over long-distance, the ultra high-voltage direct-current (UHVDC) transmission systems become an attractive option. Nowadays, not only the line commutated converter (LCC) based systems, but also the modular multilevel converter (MMC) based systems have reached UHVDC levels. The converter stations of UHVDC systems normally utilize two series-connected valve-groups to reduce the difficulties of device manufacturing and transportation. This high-voltage and low-voltage valve-group configuration allows the UHVDC systems to achieve a full-voltage to half-voltage operation which increases the flexibility of the systems. However, the existing research only focuses on the full-voltage to half-voltage control of LCC-UHVDC systems. The control strategies for hybrid LCC/MMC UHVDC systems are underresearched. Moreover, the approaches to reduce the load-shedding caused by the full-voltage to half-voltage control for both LCC and hybrid LCC/MMC based UHVDC systems have not been investigated. In this paper, full-voltage to half-voltage control strategies for both LCC and hybrid LCC/MMC based UHVDC systems have been proposed. Moreover, to avoid load-shedding caused by the half-voltage operation, a power rescheduling method that re-sets the power references of the half-voltage operating and full-voltage operating poles has been proposed. The proposed full-voltage to half-voltage control strategies and power rescheduling method can achieve a stable and fast control process with a minimum power loss. The proposed methods have been verified through the time-domain simulations conducted in PSCAD/EMTDC. Full article
(This article belongs to the Special Issue Control and Protection of HVDC-Connected Offshore Wind Power Plants)
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<p>A typical line commuted converter (LCC) ultra high-voltage direct-current (UHVDC) system.</p>
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<p>A hybrid LCC/modular multilevel converter (MMC) UHVDC system.</p>
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<p>The bypass switches and isolators equipped with the valve-groups.</p>
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<p>Possible operation modes of the positive pole of an LCC-UHVDC system. (<b>a</b>) Normal operation; (<b>b</b>) High-voltage (HV) valve-groups operation; (<b>c</b>) Low-voltage (LV) valve-groups operation; (<b>d</b>) Mixed valve-groups operation.</p>
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<p>The sequence of bypassing the HV valve-group. (<b>a</b>) Normal operation; (<b>b</b>) BPS closed; (<b>c</b>) Valve blocked, isolator closed; (<b>d</b>) Half-voltage operation.</p>
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<p>The valve-group bypassing control logic.</p>
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<p>The positive pole of an LCC/half-bridge (HB)-MMC UHVDC system.</p>
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<p>DC voltage outer loop controller of the full-bridge (FB)-MMC.</p>
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<p>System dynamics during the full-voltage to half-voltage operation of the LCC-UHVDC link. (<b>a</b>) DC terminal voltage and current of the sending end; (<b>b</b>) Firing angles of the LV and HV valve-groups of the sending end; (<b>c</b>) Extinction angles of the LV and HV valve-groups of the receiving end.</p>
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<p>System dynamics of the negative pole. (<b>a</b>) DC terminal voltage and current of the sending end; (<b>b</b>) Firing angle of the sending end.</p>
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<p>System dynamics during the full-voltage to half-voltage operation of the Hybrid LCC/HB-MMC UHVDC link. (<b>a</b>) DC terminal voltage and current of the sending end; (<b>b</b>) Firing angles of the LV and HV valve-groups of the sending end.</p>
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<p>System dynamics during the full-voltage to half-voltage operation of the Hybrid LCC/FB-MMC UHVDC link. (<b>a</b>) DC terminal voltage and current of the sending end; (<b>b</b>) Firing angles of the LV and HV valve-groups of the sending end.</p>
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<p>The sending end LCC PSCAD model.</p>
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<p>The receiving end LCC PSCAD model.</p>
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<p>The dimensions and parameters of the ± 800 kV overhead line model in PSCAD.</p>
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24 pages, 5101 KiB  
Article
Low-Cost Position Sensorless Speed Control of PMSM Drive Using Four-Switch Inverter
by Omer Cihan Kivanc and Salih Baris Ozturk
Energies 2019, 12(4), 741; https://doi.org/10.3390/en12040741 - 23 Feb 2019
Cited by 10 | Viewed by 5126
Abstract
A low-cost position sensorless speed control method for permanent magnet synchronous motors (PMSMs) is proposed using a space vector PWM based four-switch three-phase (FSTP) inverter. The stator feedforward d q -axes voltages are obtained for the position sensorless PMSM drive. The q-axis [...] Read more.
A low-cost position sensorless speed control method for permanent magnet synchronous motors (PMSMs) is proposed using a space vector PWM based four-switch three-phase (FSTP) inverter. The stator feedforward d q -axes voltages are obtained for the position sensorless PMSM drive. The q-axis current controller output with a first order low-pass filter formulates the rotor speed estimation algorithm in a closed-loop fashion similar to PLL (Phase Lock Loop) and the output of the d-axis current controller acts as the derivative representation in the stator feedforward voltage equation. The proposed method is quite insensitive to multiple simultaneous parameter variations such as rotor flux linkage and stator resistance due to the dynamic effects of the PI current regulator outputs that are used in the stator feedforward voltages with a proper value of K gain in the q-axis stator voltage equation. The feasibility and effectiveness of the proposed position sensorless speed control scheme for the PMSM drive using an FSTP inverter are verified by simulation and experimental studies. Full article
(This article belongs to the Section F: Electrical Engineering)
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<p>Classification of the sensorless control methods for a PMSM drive [<a href="#B1-energies-12-00741" class="html-bibr">1</a>,<a href="#B2-energies-12-00741" class="html-bibr">2</a>,<a href="#B3-energies-12-00741" class="html-bibr">3</a>,<a href="#B4-energies-12-00741" class="html-bibr">4</a>,<a href="#B5-energies-12-00741" class="html-bibr">5</a>,<a href="#B6-energies-12-00741" class="html-bibr">6</a>,<a href="#B7-energies-12-00741" class="html-bibr">7</a>].</p>
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<p>Four-switch three-phase (FSTP) voltage source inverter (VSI) (phase-<span class="html-italic">a</span> is connected to the center tap of the split capacitors).</p>
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<p>Equivalent electrical circuit diagram of the permanent magnet synchronous machine (PMSM) in <math display="inline"><semantics> <mrow> <mi>d</mi> <mi>q</mi> </mrow> </semantics></math>-axes synchronous reference frame [<a href="#B70-energies-12-00741" class="html-bibr">70</a>,<a href="#B71-energies-12-00741" class="html-bibr">71</a>,<a href="#B72-energies-12-00741" class="html-bibr">72</a>].</p>
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<p>Space vector representations for an FSTP inverter [<a href="#B49-energies-12-00741" class="html-bibr">49</a>].</p>
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<p>The proposed position sensorless PMSM drive scheme using an FSTP inverter.</p>
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<p>Experimental test-platform.</p>
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<p>Experimental no-load ramp speed response (referenced 0 to 360 r/min in 2 s) without parameter detuning when <math display="inline"><semantics> <mrow> <mi>K</mi> <mo>=</mo> <mn>1</mn> </mrow> </semantics></math> (low).</p>
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<p>Experimental speed response when full load (2 N·m) rejection and injection are applied respectively under 360 r/min steady-state speed with <math display="inline"><semantics> <mrow> <mi>K</mi> <mo>=</mo> <mn>1</mn> </mrow> </semantics></math> (low).</p>
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<p>Experimental steady-state (360 r/min) phase-<span class="html-italic">a</span> and -<span class="html-italic">b</span> current waveforms under full load (2 N·m) without parameter detuning when <math display="inline"><semantics> <mrow> <mi>K</mi> <mo>=</mo> <mn>1</mn> </mrow> </semantics></math> (low).</p>
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<p>Experimental steady-state (360 r/min) phase-<span class="html-italic">a</span> and –<span class="html-italic">b</span> current waveforms under full load (2 N·m) while <math display="inline"><semantics> <msub> <mi>R</mi> <mi>s</mi> </msub> </semantics></math> increased by 82.35% and <math display="inline"><semantics> <msub> <mi>λ</mi> <mi>f</mi> </msub> </semantics></math> is decreased by 40% with <math display="inline"><semantics> <mrow> <mi>K</mi> <mo>=</mo> <mn>5</mn> </mrow> </semantics></math> (high).</p>
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<p>Experimental speed response under full load (2 N·m) with the steady-state 360 r/min speed reference when <math display="inline"><semantics> <msub> <mi>R</mi> <mi>s</mi> </msub> </semantics></math> is increased stepwise by 82.35% at <math display="inline"><semantics> <mrow> <mi>t</mi> <mo>=</mo> <mn>28</mn> </mrow> </semantics></math> s with <math display="inline"><semantics> <mrow> <mi>K</mi> <mo>=</mo> <mn>1</mn> </mrow> </semantics></math> (low).</p>
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<p>Experimental steady-state nominal speed (900 r/min) response under full load (2 N·m) with <math display="inline"><semantics> <mrow> <mi>K</mi> <mo>=</mo> <mn>5</mn> </mrow> </semantics></math> (high) while <math display="inline"><semantics> <msub> <mi>R</mi> <mi>s</mi> </msub> </semantics></math> is increased by 82.35% and <math display="inline"><semantics> <msub> <mi>λ</mi> <mi>f</mi> </msub> </semantics></math> is decreased by 40%.</p>
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<p>(<b>a</b>) Experimental transient and steady-state low speed (90 r/min); (<b>b</b>) phase currents’ response when full load (2 N·m) rejection and injection are performed at <math display="inline"><semantics> <mrow> <mi>t</mi> <mo>=</mo> <mn>7.87</mn> </mrow> </semantics></math> s and <math display="inline"><semantics> <mrow> <mi>t</mi> <mo>=</mo> <mn>23</mn> </mrow> </semantics></math> s respectively with <math display="inline"><semantics> <mrow> <mi>K</mi> <mo>=</mo> <mn>5</mn> </mrow> </semantics></math> (high) while <math display="inline"><semantics> <msub> <mi>R</mi> <mi>s</mi> </msub> </semantics></math> is increased by 82.35% and <math display="inline"><semantics> <msub> <mi>λ</mi> <mi>f</mi> </msub> </semantics></math> is decreased by 40%.</p>
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<p>Experimental transient speed test (120 r/min to 90 r/min) under full load (2 N·m) with <math display="inline"><semantics> <mrow> <mi>K</mi> <mo>=</mo> <mn>5</mn> </mrow> </semantics></math> (high) while <math display="inline"><semantics> <msub> <mi>R</mi> <mi>s</mi> </msub> </semantics></math> is increased by 82.35% and <math display="inline"><semantics> <msub> <mi>λ</mi> <mi>f</mi> </msub> </semantics></math> is decreased by 40%.</p>
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<p>Experimental lowest steady-state speed (78 r/min) response test under full load (2 N·m) injection and rejection with <math display="inline"><semantics> <mrow> <mi>K</mi> <mo>=</mo> <mn>5</mn> </mrow> </semantics></math> (high) while <math display="inline"><semantics> <msub> <mi>R</mi> <mi>s</mi> </msub> </semantics></math> is increased by 82.35% and <math display="inline"><semantics> <msub> <mi>λ</mi> <mi>f</mi> </msub> </semantics></math> is decreased by 40%.</p>
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<p>Experimental transient speed reversal test (±90 r/min) under full load (2 N·m) with <math display="inline"><semantics> <mrow> <mi>K</mi> <mo>=</mo> <mn>5</mn> </mrow> </semantics></math> (high) while <math display="inline"><semantics> <msub> <mi>R</mi> <mi>s</mi> </msub> </semantics></math> is increased by 82.35% and <math display="inline"><semantics> <msub> <mi>λ</mi> <mi>f</mi> </msub> </semantics></math> is decreased by 40% of its original value.</p>
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<p>Experimental steady-state (90 r/min) measured and estimated rotor position waveforms under full load (2 N·m) with <math display="inline"><semantics> <mrow> <mi>K</mi> <mo>=</mo> <mn>5</mn> </mrow> </semantics></math> (high) while <math display="inline"><semantics> <msub> <mi>R</mi> <mi>s</mi> </msub> </semantics></math> is increased by 82.35% and <math display="inline"><semantics> <msub> <mi>λ</mi> <mi>f</mi> </msub> </semantics></math> is decreased by 40% of its original value.</p>
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<p>Experimental rotor speed waveform in a steady-state (120 r/min) and when the speed is stepped down to 90 r/min at <math display="inline"><semantics> <mrow> <mi>t</mi> <mo>=</mo> <mn>24.32</mn> </mrow> </semantics></math> s during 82.35% higher stator resistance than the actual value and <math display="inline"><semantics> <msub> <mi>λ</mi> <mi>f</mi> </msub> </semantics></math> is decreased by 40% of its original value using classical SMO.</p>
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<p>Timing diagrams for (<b>a</b>) Feedforward Voltage Control (FFVC) and (<b>b</b>) Sliding Mode Control (SMO).</p>
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12 pages, 914 KiB  
Article
Production of Oxygenated Fuel Additives from Residual Glycerine Using Biocatalysts Obtained from Heavy-Metal-Contaminated Jatropha curcas L. Roots
by Juan Francisco García-Martín, Francisco Javier Alés-Álvarez, Miguel Torres-García, Chao-Hui Feng and Paloma Álvarez-Mateos
Energies 2019, 12(4), 740; https://doi.org/10.3390/en12040740 - 23 Feb 2019
Cited by 18 | Viewed by 4427
Abstract
This work aims to shed light on the use of two biochars, obtained from the pyrolysis at 550 °C of heavy-metal-contaminated Jatropha curcas L. roots, as heterogeneous catalysts for glycerol esterification using residual glycerine. To do this, glycerine from biodiesel production was purified. [...] Read more.
This work aims to shed light on the use of two biochars, obtained from the pyrolysis at 550 °C of heavy-metal-contaminated Jatropha curcas L. roots, as heterogeneous catalysts for glycerol esterification using residual glycerine. To do this, glycerine from biodiesel production was purified. In a first step, H3PO4 or H2SO4 was used to remove non-glycerol organic matter. The glycerol-rich phase was then extracted with ethanol or propanol, which increased the glycerol content from 43.2% to up to 100%. Subsequently, the esterification of both purified glycerine and commercial USP glycerine was assayed with acetic acid (AA) or with acetic anhydride (AH) at 9:1 molar ratio to glycerol using Amberlyst-15 as catalyst. Different reaction times (from 1.5 to 3 h) and temperatures (100–115 °C when using AA and 80–135 °C when using AH) were assessed. Results revealed that the most suitable conditions were 80 °C and 1.5 h reaction time using AH, achieving 100% yield and selectivity towards triacetylglycerol (TAG) almost with both glycerines. Finally, the performance and reuse of the two heterogeneous biocatalysts was assessed. Under these conditions, one of the biocatalysts also achieved 100% TAG yield. Full article
(This article belongs to the Section A4: Bio-Energy)
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<p>Mass balance of the crude glycerol purification under the most suitable conditions.</p>
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<p>GC-MS chromatograms obtained during Biocatalyst 2 reuse trials.</p>
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<p>GC-MS chromatograms obtained during Biocatalyst 2 reuse trials.</p>
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14 pages, 3797 KiB  
Article
Electric Energy Consumption Prediction by Deep Learning with State Explainable Autoencoder
by Jin-Young Kim and Sung-Bae Cho
Energies 2019, 12(4), 739; https://doi.org/10.3390/en12040739 - 22 Feb 2019
Cited by 114 | Viewed by 8802
Abstract
As energy demand grows globally, the energy management system (EMS) is becoming increasingly important. Energy prediction is an essential component in the first step to create a management plan in EMS. Conventional energy prediction models focus on prediction performance, but in order to [...] Read more.
As energy demand grows globally, the energy management system (EMS) is becoming increasingly important. Energy prediction is an essential component in the first step to create a management plan in EMS. Conventional energy prediction models focus on prediction performance, but in order to build an efficient system, it is necessary to predict energy demand according to various conditions. In this paper, we propose a method to predict energy demand in various situations using a deep learning model based on an autoencoder. This model consists of a projector that defines an appropriate state for a given situation and a predictor that forecasts energy demand from the defined state. The proposed model produces consumption predictions for 15, 30, 45, and 60 min with 60-min demand to date. In the experiments with household electric power consumption data for five years, this model not only has a better performance with a mean squared error of 0.384 than the conventional models, but also improves the capacity to explain the results of prediction by visualizing the state with t-SNE algorithm. Despite unsupervised representation learning, we confirm that the proposed model defines the state well and predicts the energy demand accordingly. Full article
(This article belongs to the Section A1: Smart Grids and Microgrids)
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<p>Plan, do, check, and act (PDCA) cycle for EMS. We focus on “plan” phase in this paper.</p>
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<p>(<b>a</b>) The electric energy demand for each date, and (<b>b</b>) the result of Fourier transform.</p>
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<p>The overall scheme of the proposed method.</p>
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<p>The predicted electric energy consumption and the actual demand. We show the prediction results for (<b>a</b>) 15, (<b>b</b>) 30, (<b>c</b>) 45, and (<b>d</b>) 60 min.</p>
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<p>The training and test loss values for each epoch. We show the mean squared error of the model that predicts electric energy demand for (<b>a</b>) 15, (<b>b</b>) 30, (<b>c</b>) 45, and (<b>d</b>) 60 min.</p>
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<p>The results of MSE of models. We show the MSE results for (<b>a</b>) 15, (<b>b</b>) 30, (<b>c</b>) 45, and (<b>d</b>) 60 min.</p>
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<p>Visualization of states for monthly electricity demands. We describe the cluster of states as red circles on a monthly basis.</p>
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<p>Examples of state transition from state in APR to state in AUG or OCT.</p>
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12 pages, 1844 KiB  
Article
Application of the Impedance Spectroscopy as a New Tool for Studying Biodiesel Fuel Aging Processes
by Krzysztof Biernat, Piotr Bocian, Paweł Bukrejewski and Krzysztof R. Noworyta
Energies 2019, 12(4), 738; https://doi.org/10.3390/en12040738 - 22 Feb 2019
Cited by 8 | Viewed by 4048
Abstract
Fatty acid methyl esters (FAME), which are presently the main component of biodiesel fuels, undergo relatively fast oxidation processes. This behavior prevents long term storage of this fuel. From laboratory practices, it transpires that even after a very short period of storage, the [...] Read more.
Fatty acid methyl esters (FAME), which are presently the main component of biodiesel fuels, undergo relatively fast oxidation processes. This behavior prevents long term storage of this fuel. From laboratory practices, it transpires that even after a very short period of storage, the oxidative stability of the biodiesel exceeds the values required by European regulations. Therefore, the goal of this work was to devise a parameter (marker) allowing for fast and convenient identification of the chemical stability of biodiesel. Moreover, we were aiming to devise a marker which can also be used for the evaluation of the chemical stability of other hydrocarbon fuels containing biocomponents. To this end, in the presented study, selected biodiesel samples were subjected to controlled aging processes in laboratory conditions at 95 °C and oxygen flow according to the norm. Then, physico-chemical parameters were selected that are critical from the point of view of the fuel practical application. Those included density, refractive index, oxidative stability and resistance to oxidation. The appropriate physico-chemical properties were measured before and after an aging process conducted for various times. Simultaneously, electrochemical impedance spectroscopy (EIS) studies were performed for all the studied samples yielding the electrical parameters of the sample, including resistance, relaxation time and capacitance. Subsequently, a correlation between the results of the EIS studies and the selected critical parameters has been established. The obtained results indicate that the resistance, relaxation time and capacitance of the studied biodiesel fuel increase with aging time. This indicates the formation of long chain compounds with increased polarity. Interestingly, the electrical parameter changes are faster at the early stages of the aging process. This suggests a change of the oxidation mechanism during prolonged aging. The devised methodology of impedimetric biodiesel testing can be proposed as a fast and inexpensive method of fuel chemical stability evaluation, allowing for estimating the useful storage time of biodiesel in real conditions. Full article
(This article belongs to the Special Issue Biodiesel Production)
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<p>Glass cell used for oxidation of diesel fuels containing fatty acid methyl esters (FAME).</p>
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<p>Schematic view of the measurement setup that has been used for electrochemical impedance spectroscopy studies of biodiesel fuel.</p>
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<p>Impedance spectra of the biodiesel samples aged according to norms recorded at 0 V voltage modified with sinusoidal alternate voltage with amplitude 0.4 V in the frequency range from 10 mHz to 3 MHz. <span class="html-italic">Z</span><sub>im</sub> = imaginary part of the impedance; <span class="html-italic">Z</span><sub>re</sub> = real part of the impedance.</p>
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<p>Curves of (<b>a</b>) imaginary, <span class="html-italic">Z</span><sub>im</sub> and (<b>b</b>) real, <span class="html-italic">Z</span><sub>re</sub> part of the impedance versus frequency of the applied alternating voltage recorded for the samples of biodiesel fuel ST ON 7 containing FAME recorded after different aging times.</p>
Full article ">Figure 5
<p>Dependence of (<b>a</b>) sample resistance, <span class="html-italic">R</span>, the real part of the impedance, <span class="html-italic">Z</span><sub>re</sub>, at 30 mHz and the imaginary part of the impedance, <span class="html-italic">Z</span><sub>im</sub>, at 15 mHz, as well as (<b>b</b>) sample capacitance, <span class="html-italic">C</span>, and relaxation time, <span class="html-italic">τ</span>, on the aging time of the studied biodiesel ST ON 7.</p>
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<p>Dependence of the (<b>a</b>) oxidative stability (“PetroOXY”) and oxidation resistance (“Rancimat”), as well as (<b>b</b>) density at 15 °C and refractive index at 20 °C on the aging time of the studied biodiesel ST ON 7.</p>
Full article ">Figure 7
<p>Correlation of the electrical parameters <span class="html-italic">R</span>, <span class="html-italic">Z</span><sub>re</sub> and <span class="html-italic">Z</span><sub>im</sub> obtained from the impedance measurements of the physico-chemical parameters of the diesel fuels routinely used for evaluation of the fuel quality. (<b>a</b>) Oxidative stability (“PetroOXY”), (<b>b</b>) oxidation resistance (“Rancimat”), (<b>c</b>) density at 15 °C, and (<b>d</b>) refractive index at 20 °C.</p>
Full article ">Figure 8
<p>Correlation of the relaxation time, <span class="html-italic">τ</span>, and capacitance, <span class="html-italic">C</span>, obtained from the impedance measurements with physico-chemical parameters of the diesel fuels routinely used for evaluation of the fuel quality. (<b>a</b>) Oxidative stability (“PetroOXY”), (<b>b</b>) oxidation resistance (“Rancimat”), (<b>c</b>) density at 15 °C, and (<b>d</b>) refractive index at 20 °C.</p>
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