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20 pages, 4614 KiB  
Article
Fuel Injection Optimization for Large-Bore Two-Stroke Natural-Gas Engines
by Titilope Ibukun Banji, Gregg Arney and Daniel B. Olsen
Energies 2025, 18(3), 624; https://doi.org/10.3390/en18030624 - 29 Jan 2025
Viewed by 519
Abstract
Recent methane emissions regulations present a challenge for the large-bore, natural-gas-fueled engines used at over 1700 compression stations across the US. Poor air–fuel mixing in the main combustion chamber of these engines results in low combustion efficiency and the resulting methane emissions. High-pressure [...] Read more.
Recent methane emissions regulations present a challenge for the large-bore, natural-gas-fueled engines used at over 1700 compression stations across the US. Poor air–fuel mixing in the main combustion chamber of these engines results in low combustion efficiency and the resulting methane emissions. High-pressure fuel injection is believed to be a significant development in improving air–fuel mixing in natural-gas engine combustion chambers. This study aims to determine the sensitivity of in-cylinder mixing to injection pressures using Computational Fluid Dynamics (CFD) simulations, determine the limits of high-pressure fuel injection, and explore high-momentum low-pressure fuel injection. The engine, modeled using Converge Studio for CFD, was a Cooper-Bessemer large-bore, four-cylinder, GMV-4TF spark-ignited natural-gas engine with direct injection. The model was simulated for four sets of configured cases—baseline; ideal mixing; injection pressure variation; and low-pressure, high-momentum injection. The results show that fuel injection at 700 psi and −115 degrees BTDC gives the best in-cylinder mixing and improved mixing, potentially reducing methane emissions by half. The optimal timing for the injection at different injection pressures was determined. The level of mixing in low-pressure fuel-injection systems was also improved by the high-momentum fuel injector design. It was concluded that mixing can be further improved in integral gas compressor engines through fuel injection optimization. Full article
(This article belongs to the Section I2: Energy and Combustion Science)
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<p>The GMVH engine at the engines and energy conversion laboratory at CSU. Source: Authors (2024) [<a href="#B18-energies-18-00624" class="html-bibr">18</a>].</p>
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<p>High-pressure fuel-injection set-up on the GMVH cylinder head. Source: Authors (2024) [<a href="#B18-energies-18-00624" class="html-bibr">18</a>].</p>
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<p>Scavenging cycle geometric model. This cycle spans from −254 to 0 degrees ATDC and accounts for the scavenging process. Source: Authors (2024) [<a href="#B18-energies-18-00624" class="html-bibr">18</a>].</p>
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<p>Boundaries and regions in the scavenging cycle model. Source: Authors (2024) [<a href="#B18-energies-18-00624" class="html-bibr">18</a>].</p>
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<p>Cross-section of the combustion cycle geometric model. This cycle is like the scavenging cycle geometric model but with only regions involved in combustion. The cycle spans from −10 to 110 degrees ATDC. Source: Authors (2024) [<a href="#B18-energies-18-00624" class="html-bibr">18</a>].</p>
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<p>Boundaries and regions in the combustion cycle model. Source: Authors (2024) [<a href="#B18-energies-18-00624" class="html-bibr">18</a>].</p>
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<p>Discretized model: Intake and exhaust ports. The intake ports are in pairs and the exhaust ports are identical. Source: Authors (2024) [<a href="#B18-energies-18-00624" class="html-bibr">18</a>].</p>
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<p>Cross-section of geometric model: (<b>a</b>) at bottom dead center (BDC) and (<b>b</b>) at (TDC). Source: Authors (2024) [<a href="#B18-energies-18-00624" class="html-bibr">18</a>].</p>
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<p>CFD geometric model (showing surface edges) of the engine cylinder, head, and fuel valve.</p>
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<p>Cylinder pressure trace for baseline.</p>
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<p>Ideal uniform mixing case. CFD case with equivalence ratio standard deviation of 0 (indicating perfect mixing) at the point of ignition (−1.5 degrees ATDC) in the combustion cycle.</p>
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<p>Methane in main cylinder—combustion cycle: (<b>a</b>) −250 to 110 degrees ATDC and (<b>b</b>) 92 to 110 degrees ATDC.</p>
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<p>Optimal injection-timing investigation.</p>
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<p>Visual renderings: (<b>a</b>) 1.6% slip of fuel injected at 150 psi and −145 degrees ATDC (early in the cycle) from −148 to −132 degrees; (<b>b</b>) 1.6% slip of fuel injected at 150 psi and −145 degrees ATDC (early in the cycle) from −128 to −108 degrees.</p>
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<p>Visual renderings: (<b>a</b>) 1.6% slip of fuel injected at 150 psi and −145 degrees ATDC (early in the cycle) from −148 to −132 degrees; (<b>b</b>) 1.6% slip of fuel injected at 150 psi and −145 degrees ATDC (early in the cycle) from −128 to −108 degrees.</p>
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<p>Baseline case with no slip from injected fuel, at 500 psi and −115 degrees ATDC.</p>
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<p>The 150 psi optimal mixing.</p>
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<p>The 300 psi optimal mixing.</p>
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<p>The 500 psi optimal mixing.</p>
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<p>The 600 psi optimal mixing.</p>
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<p>The 700 psi optimal mixing.</p>
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<p>The 800 psi optimal mixing.</p>
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<p>Optimal mixing points.</p>
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<p>Increased flow area for low-pressure–high-momentum case (increased seat flow area, shroud poppet annulus, and stem-port annulus). (<b>a</b>) original design model cross-section of fuel injection valve; (<b>b</b>) modified design model cross-section of fuel injection valve—increased flow areas.</p>
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<p>Low-pressure, high-momentum case: Mass of fuel delivered. (*—values shown were multiplied by – 1 to show direction of flow from injector to main cylinder as the results were initially in the reverse direction).</p>
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<p>Low-pressure, high-momentum case: In-cylinder mixing.</p>
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20 pages, 5610 KiB  
Article
Numerical Simulations of Thermodynamic Processes in the Chamber of a Liquid Piston Compressor for Hydrogen Applications
by Valerijs Bezrukovs, Vladislavs Bezrukovs, Marina Konuhova, Deniss Bezrukovs, Imants Kaldre and Anatoli I. Popov
Technologies 2024, 12(12), 266; https://doi.org/10.3390/technologies12120266 - 18 Dec 2024
Cited by 1 | Viewed by 1551
Abstract
This paper presents the results of numerical simulations examining the thermodynamic processes during hydraulic hydrogen compression, using COMSOL Multiphysics® 6.0. These simulations focus on the application of hydrogen compression systems, particularly in hydrogen refueling stations. The computational models employ the CFD and [...] Read more.
This paper presents the results of numerical simulations examining the thermodynamic processes during hydraulic hydrogen compression, using COMSOL Multiphysics® 6.0. These simulations focus on the application of hydrogen compression systems, particularly in hydrogen refueling stations. The computational models employ the CFD and heat transfer modules, along with deforming mesh technology, to simulate gas compression and heat transfer dynamics. The superposition method was applied to simplify the analysis of hydrogen and liquid piston interactions within a stainless-steel chamber, accounting for heat exchange between the hydrogen, the oil (working fluid), and the cylinder walls. The study investigates the effects of varying compression stroke durations and initial hydrogen pressures, providing detailed insights into temperature distributions and energy consumption under different conditions. The results reveal that the upper region of the chamber experiences significant heating, highlighting the need for efficient cooling systems. Additionally, the simulations show that longer compression strokes reduce the power requirement for the liquid pump, offering potential for optimizing system design and reducing equipment costs. This study offers crucial data for enhancing the efficiency of hydraulic hydrogen compression systems, paving the way for improved energy consumption and thermal management in high-pressure applications. Full article
(This article belongs to the Special Issue Technological Advances in Science, Medicine, and Engineering 2024)
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<p>Schematic diagram of the delivery, storage, and preparation of compressed high-pressure hydrogen for use at refueling stations.</p>
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<p>A model of a steel cylinder shaped chamber where hydrogen is compressed by the oil (working fluid) coming from the bottom in the direction of the arrow.</p>
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<p>Model of a stainless-steel cylinder chamber for hydrogen compression via fluid injection.</p>
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<p>Mesh cell distribution in the numerical model during the change in hydrogen volume within the compression chamber and the position of the liquid piston column as it moves upward at times 0, 10, and 20 s over a single stroke period.</p>
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<p>The structure of the mesh cells in the numerical model during hydrogen compression in the chamber to a compression ratio <span class="html-italic">K<sub>c</sub></span> = 5.0 for time intervals of (<b>a</b>) 0 s and (<b>b</b>) 20 s.</p>
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<p>Distribution of the temperature of hydrogen in the compression chamber during a single 20 s compression stroke: (<b>a</b>) the initial pressure 3.0 MPa, (<b>b</b>) the initial pressure 20.0 MPa.</p>
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<p>Temperature distribution in the compression chamber wall during a single 20 s compression stroke: (<b>a</b>) initial pressure of 3.0 MPa, and (<b>b</b>) initial pressure of 20.0 MPa.</p>
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<p>Average temperature increases in hydrogen ∆<span class="html-italic">T<sub>H</sub></span> for different durations of the compression stroke <span class="html-italic">t<sub>s</sub></span> at initial pressures <span class="html-italic">P</span><sub>1</sub> = 3.0, 10.0, 15.0, and 20.0 MPa and compression ratio <span class="html-italic">K<sub>c</sub></span> = 5.0.</p>
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<p>Average temperature increases in oil ∆<span class="html-italic">T<sub>F</sub></span> for different durations of the compression stroke <span class="html-italic">t<sub>s</sub></span> at initial pressures <span class="html-italic">P</span><sub>1</sub> = 3.0, 10.0, 15.0, and 20.0 MPa and compression ratio <span class="html-italic">K<sub>c</sub></span> = 5.0.</p>
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<p>Average temperature increases in the cylinder body ∆<span class="html-italic">T<sub>C</sub></span> for different durations of the compression stroke <span class="html-italic">t<sub>s</sub></span> at initial pressures <span class="html-italic">P</span><sub>1</sub> = 3.0, 10.0, 15.0, and 20.0 MPa and compression ratio <span class="html-italic">K<sub>c</sub></span> = 5.0.</p>
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<p>Diagrams of thermal energy distribution <span class="html-italic">Q<sub>T</sub></span> between energies accumulated in hydrogen <span class="html-italic">Q<sub>H</sub></span>, oil <span class="html-italic">Q<sub>F</sub></span>, and compression cylinder body <span class="html-italic">Q<sub>C</sub></span> for different durations of the compression stroke <span class="html-italic">t<sub>s</sub></span> at initial pressures <span class="html-italic">P</span><sub>1</sub> = 3.0 MPa and compression ratio <span class="html-italic">K<sub>c</sub></span> = 5.0.</p>
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<p>Diagrams of thermal energy distribution <span class="html-italic">Q<sub>T</sub></span> between energies accumulated in hydrogen <span class="html-italic">Q<sub>H</sub></span>, oil <span class="html-italic">Q<sub>F</sub></span>, and compression cylinder body <span class="html-italic">Q<sub>C</sub></span> for different durations of the compression stroke <span class="html-italic">t<sub>s</sub></span> at initial pressures <span class="html-italic">P</span><sub>1</sub> = 20.0 MPa and compression ratio <span class="html-italic">K<sub>c</sub></span> = 5.0.</p>
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<p>Increase in overall system temperature ∆<span class="html-italic">T<sub>O</sub></span> for different durations of the compression stroke <span class="html-italic">t<sub>s</sub></span>, at initial pressures <span class="html-italic">P</span><sub>1</sub> = 3.0, 10.0, 15.0, and 20.0 MPa and compression ratio <span class="html-italic">K<sub>c</sub></span> = 5.0.</p>
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<p>The power <span class="html-italic">W</span> required for hydrogen compression for different durations of the compression stroke <span class="html-italic">t<sub>s</sub></span> at initial pressures <span class="html-italic">P</span><sub>1</sub> = 3.0, 10.0, 15.0, and 20.0 MPa and compression ratio <span class="html-italic">K<sub>c</sub></span> = 5.0.</p>
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28 pages, 8666 KiB  
Article
Cooling of Air in Outdoor Areas of Human Habitation
by Ewelina Barnat, Robert Sekret and Bożena Babiarz
Energies 2024, 17(24), 6303; https://doi.org/10.3390/en17246303 - 13 Dec 2024
Viewed by 464
Abstract
This paper deals with the issue of air cooling in outdoor areas of human habitation. An analysis of air parameters during the summer season was carried out to determine the thermal comfort zone for a part of the northern platform of the local [...] Read more.
This paper deals with the issue of air cooling in outdoor areas of human habitation. An analysis of air parameters during the summer season was carried out to determine the thermal comfort zone for a part of the northern platform of the local station in Rzeszow (Poland). The cooling capacity required for thermal comfort was calculated using outdoor air parameters and heat gains in the vicinity of the research object. Ten potential air-cooling systems were proposed for the outdoor zones. The systems differed in terms of cooling equipment, primary energy source, cooling medium, and recipients. They were divided into three categories: compressor, adsorption, and evaporative cooling. The electricity yield of the existing photovoltaic installation at the research facility was evaluated to identify potential synergies between the cooling demand and solar energy. An analysis assessed the energy, economic, and environmental impact of each proposed option. The best option for cooling the outdoor areas was found to be an evaporative cooling system with a PV system. Solar radiation can be effectively used for cooling outdoor zones in Poland in the summer. The optimal solution for the research facility is an evaporative cooling system based on direct evaporation combined with a photovoltaic system. The subject matter covered can be used as an effective tool for the optimal selection of outdoor air-cooling systems to ensure the thermal comfort of the occupants. Full article
(This article belongs to the Special Issue Thermal Comfort, Environment Quality and Energy Consumption)
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<p>Site plan of the Rzeszow local bus station (<b>a</b>) and the top view and vertical cross-section of the research facility (<b>b</b>).</p>
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<p>Rzeszow local train station—north shelter.</p>
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<p>Diagram of the air-cooling system proposed in the AS-WL-AC, AS/PV-WL-AC variant.</p>
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<p>Diagram of the air-cooling system proposed in variants AA-PK-WL-AC, AA/PV-PK-WL-AC, AA-OZE-WL-AC, AA/PV-OZE-WL-AC.</p>
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<p>Diagram of the air-cooling plant proposed in the PKW-CP-KW, PKW/PV-CP-KW variant.</p>
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<p>Diagram of the air-cooling plant proposed for BKW-CP-KW, BKW/PV-CP-KW variant.</p>
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<p>Frequency of episodes when TE exceeded 22.9 °C by year [<a href="#B48-energies-17-06303" class="html-bibr">48</a>].</p>
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<p>Total cooling demand <span class="html-italic">Q<sub>CH</sub></span> for the reference area.</p>
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<p>Electricity yield from an existing photovoltaic installation.</p>
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<p>Degree of coverage of energy needs from PV.</p>
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<p>EP values for the different alternatives.</p>
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<p>EP, EK, and EU values for the different options.</p>
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<p>Comparison of the E-indicators of the different impact categories for the analyzed options.</p>
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<p>Comparison of the eco-indicators of the different damage categories for the analyzed options.</p>
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<p>The value of the LLC index for the different options.</p>
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25 pages, 5210 KiB  
Article
Application of SHAP and Multi-Agent Approach for Short-Term Forecast of Power Consumption of Gas Industry Enterprises
by Alina I. Stepanova, Alexandra I. Khalyasmaa, Pavel V. Matrenin and Stanislav A. Eroshenko
Algorithms 2024, 17(10), 447; https://doi.org/10.3390/a17100447 - 8 Oct 2024
Viewed by 1285
Abstract
Currently, machine learning methods are widely applied in the power industry to solve various tasks, including short-term power consumption forecasting. However, the lack of interpretability of machine learning methods can lead to their incorrect use, potentially resulting in electrical system instability or equipment [...] Read more.
Currently, machine learning methods are widely applied in the power industry to solve various tasks, including short-term power consumption forecasting. However, the lack of interpretability of machine learning methods can lead to their incorrect use, potentially resulting in electrical system instability or equipment failures. This article addresses the task of short-term power consumption forecasting, one of the tasks of enhancing the energy efficiency of gas industry enterprises. In order to reduce the risks of making incorrect decisions based on the results of short-term power consumption forecasts made by machine learning methods, the SHapley Additive exPlanations method was proposed. Additionally, the application of a multi-agent approach for the decomposition of production processes using self-generation agents, energy storage agents, and consumption agents was demonstrated. It can enable the safe operation of critical infrastructure, for instance, adjusting the operation modes of self-generation units and energy-storage systems, optimizing the power consumption schedule, and reducing electricity and power costs. A comparative analysis of various algorithms for constructing decision tree ensembles was conducted to forecast power consumption by gas industry enterprises with different numbers of categorical features. The experiments demonstrated that using the developed method and production process factors reduced the MAE from 105.00 kWh (MAPE of 16.81%), obtained through expert forecasting, to 15.52 kWh (3.44%). Examples were provided of how the use of SHapley Additive exPlanation can increase the safety of the electrical system management of gas industry enterprises by improving experts’ confidence in the results of the information system. Full article
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<p>Pipeline of the proposed method.</p>
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<p>The main elements of typical compressor station.</p>
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<p>Actual power consumption of compressor station from December 2020 to January 2021.</p>
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<p>The first information model used to generate “Schedule of power consumption forecast”, “Schedule of controllable load consumers”, and “Operating schedule of energy storage systems”.</p>
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<p>The second information model used to generate “Operating schedule of self-generation”.</p>
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<p>The agent decomposition of elements of compressor station.</p>
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<p>Interaction of storage agent, generator agent, and consumer agent.</p>
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<p>The algorithm of data preprocessing.</p>
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<p>Spearman’s correlation coefficients.</p>
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<p>Actual and forecast power consumption from December 2020 to January 2021.</p>
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<p>Actual and forecast power consumption from September 2020 to October 2021.</p>
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<p>Influence of the features on the forecast of power consumption of 2nd hour on 6 February 2020 obtained by (<b>a</b>) LightGBM; (<b>b</b>) XGBoost.</p>
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<p>Influence of the features on the forecast of power consumption for midnight on 3 April 2020 obtained by (<b>a</b>) LightGBM; (<b>b</b>) XGBoost.</p>
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12 pages, 6000 KiB  
Article
Development and Design Validation of an Inflow-Settling Chamber for Turbomachinery Test-Benches
by Michael Henke, Stefan Gärling, Lena Junge, Lars Wein and Hans-Ulrich Fleige
Int. J. Turbomach. Propuls. Power 2024, 9(4), 31; https://doi.org/10.3390/ijtpp9040031 - 24 Sep 2024
Viewed by 978
Abstract
At Leibniz University of Hannover, Germany, a new turbomachinery test facility has been built over the last few years. A major part of this facility is a new 6 MW compressor station, which is connected to a large piping system, both designed and [...] Read more.
At Leibniz University of Hannover, Germany, a new turbomachinery test facility has been built over the last few years. A major part of this facility is a new 6 MW compressor station, which is connected to a large piping system, both designed and built by AERZEN. This system provides air supply to several wind tunnel and turbomachinery test rigs, e.g., axial turbines and axial compressors. These test rigs are designed to conduct high-quality aerodynamic, aeroelastic, and aeroacoustic measurements to increase physical understanding of steady and unsteady effects in turbomachines. One primary purpose of these investigations is the validation of aerodynamic and aeroacoustic numerical methods. To provide precise boundary conditions for the validation process, extremely high homogeneity of the inflow to the investigated experimental setup is imminent. Thus, customized settling chambers have been developed using analytical and numerical design methods. The authors have chosen to follow basic aerodynamic design steps, using analytical assumptions for the inlet section, the “mixing” area of a settling chamber, and the outlet nozzle in combination with state-of-the-art numerical investigations. In early 2020, the first settling chamber was brought into operation for the acceptance tests. In order to collect high-resolution flow field data during the tests, Leibniz University and AERZEN have designed a unique measurement device for robust and fast in-line flow field measurements. For this measurement device, total pressure and total-temperature rake probes, as well as traversing multi-hole probes, have been used in combination to receive high-resolution flow field data at the outlet section of the settling chamber. The paper provides information about the design process of the settling chamber, the developed measurement device, and measurement data gained from the acceptance tests. Full article
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<p>Schematic view of the main air supply system of the test facility adapted from [<a href="#B7-ijtpp-09-00031" class="html-bibr">7</a>].</p>
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<p>Three-dimensional model view of the standard test cell with a settling chamber installed upstream of the test rig.</p>
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<p>Three-dimensional visualization of the settling chamber design with optimized geometry and flow straighteners.</p>
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<p>Cross-sectional view of the final design for the settling chamber and optimized components (individually optimized geometry components marked in different colored).</p>
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<p>Numerical domain and model details for the post-test analysis.</p>
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<p>Measurement device mounted downstream of the settling chamber (<b>left</b>) and a schematic view of the internal probe design (<b>right</b>).</p>
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<p>Comparison of normalized circumferential velocity at the settling chamber outlet between an empty settling chamber and a settling chamber fully equipped with internal aerodynamic structures.</p>
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<p>Deviation from the mean value of the relative total pressure distribution at the settling chamber outlet cross-section for OP5; measurement uncertainty in experiment ±50 Pa.</p>
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<p>Deviation from the mean value of the absolute total temperature distribution at the settling chamber outlet cross-section for OP5; measurement uncertainty in experiment ±0.4 K.</p>
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<p>Deviation from the mean value of the relative total pressure distribution at the settling chamber outlet cross-section for OP19; measurement uncertainty in experiment ±50 Pa.</p>
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<p>Deviation from the mean value of the absolute total temperature distribution at the settling chamber outlet cross-section for OP19; measurement uncertainty in experiment ±0.4 K.</p>
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<p>Comparison between measurement results and simulation of the absolute total temperature distribution in the core flow section downstream of the settling chamber.</p>
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18 pages, 2830 KiB  
Article
Obsolete Mining Buildings and the Circular Economy on the Example of a Coal Mine from Poland—Adaptation or Demolition and Building Anew?
by Anna Ostręga, Anna Szewczyk-Świątek, Marek Cała and Piotr Dybeł
Sustainability 2024, 16(17), 7493; https://doi.org/10.3390/su16177493 - 29 Aug 2024
Viewed by 1273
Abstract
During the energy transition period and the increased supply of developed land, an analysis was conducted on the economic viability of transforming post-mining buildings. This study sought to answer the following questions: Does the circular economy create new conditions for adapting these specific [...] Read more.
During the energy transition period and the increased supply of developed land, an analysis was conducted on the economic viability of transforming post-mining buildings. This study sought to answer the following questions: Does the circular economy create new conditions for adapting these specific industrial facilities? Should mining buildings be adapted or should they be demolished and built anew? The objectives of the article were to perform a comparative analysis (financial, environmental, and social) of these alternatives and to develop a decision-making model for managing obsolete mining facilities using circular economy principles. Decision-making regarding mining buildings should occur as part of revitalising post-mining areas. Consequently, the method used was research through design followed by comparative analyses: financial, environmental, and social. As a result, the study demonstrated the potential for adapting buildings on a defunct mining site, mainly compressor and fan station. The financial, environmental, and social profitability of investing in the adaptive reuse of historic buildings was established. The entire process was encapsulated in a universal decision-making model. The analytical results presented in the article indicate that mining buildings represent a significant resource in a circular economy and their adaptation should be prioritised. Full article
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<p>Impact of the construction sector on the environment: (<b>a</b>) annual use of construction materials for buildings in the EU 27, an average of 2006–2010 (source: [<a href="#B4-sustainability-16-07493" class="html-bibr">4</a>] after CRI calculations); (<b>b</b>) waste generation by economic activities and households, EU, 2020 (source: [<a href="#B5-sustainability-16-07493" class="html-bibr">5</a>]).</p>
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<p>Examples of adapting post-mining buildings for service functions: (<b>a</b>) public—Silesian Museum (photo: A. Ostręga); (<b>b</b>) commercial—restaurant Casino at Zeche Zollverein (photo: A. Ostręga).</p>
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<p>Inventory of buildings and technical structures of the inactive Brzeszcze-East Hard Coal Mine. (<b>a</b>) Partially preserved wagon scale building at the powder store from 1974; (<b>b</b>) pithead waiting room with bath, administration, and lamp rooms from 1936, 1949, and 1963 (adapted by an entrepreneur); (<b>c</b>) boiler house from 1935; (<b>d</b>) gatehouse from 1974; (<b>e</b>) Andrzej III shaft headhouse with headframe and lacing from 1932 to 1934, on the left part of circulation wagons from 1975; (<b>f</b>) Andrzej III shaft drawing machine from 1945; (<b>g</b>) Andrzej III shaft hoist house, converter, and switching station from 1932, 1941, and 1968; (<b>h</b>) transformer station; (<b>i</b>) Andrzej IV shaft headhouse from 1954 to 1955; (<b>j</b>) Andrzej IV shaft hoist house from 1945 and (<b>k</b>) drawing machine from 1959; (<b>l</b>) compressor and fan station from 1949, 1958, 1963, 1966, and 1986; (<b>n</b>) Fan cooler from 1986, and (<b>m</b>) water cooling pool from 1947. (photos: by A. Ostręga: (<b>a</b>–<b>f</b>,<b>j</b>–<b>n</b>); M. Kramarczyk: (<b>h</b>,<b>i</b>); S. Berrut: (<b>g</b>)).</p>
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<p>Examples of equipment in the compressor and fan station: (<b>a</b>) ventilation stack and compressor, (<b>b</b>) compressor (photo by A. Ostręga).</p>
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<p>(<b>a</b>) Adaptive reuse plan for the compressor and fan station, indicating possible divisions of rooms (yellow) and open, functional spaces (grey and green) between elements of equipment remaining from the mine (red); (<b>b</b>) Visualisation of the open functional space in the compressor building (Author: 55Architekci, 2021, we have drawing permission from 55Architekci).</p>
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<p>Decision-making model for dealing with buildings in post-mining areas (own study).</p>
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15 pages, 6439 KiB  
Article
Influence of High-Temperature Aggressive Environments on the Durability of Composites Reinforced with Refractory Particles
by Peter Rusinov, George Kurapov, Anastasia Rusinova, Maxim Semadeni and Polina Sereda
Metals 2024, 14(8), 939; https://doi.org/10.3390/met14080939 - 16 Aug 2024
Viewed by 1268
Abstract
The problem of increasing heat resistance and corrosion and erosion resistance of gas turbine units in compressor stations was solved through the development of new layered materials containing nanostructured grains. The authors carried out a destruction analysis of gas turbine units in compressor [...] Read more.
The problem of increasing heat resistance and corrosion and erosion resistance of gas turbine units in compressor stations was solved through the development of new layered materials containing nanostructured grains. The authors carried out a destruction analysis of gas turbine units in compressor stations. It was shown that after 10–30,000 h of operation, the greatest damage occurred when the gas turbine operated in dusty environments at high temperatures (or in air environments with a high salt content). The developed layered composites include the thermal barrier and functional reinforced nanostructured layers consisting of refractory carbides and oxides. This paper describes the destruction mechanism of gas turbine units under the influence of high-temperature aggressive environments. As a result, a new formation technology for reinforced nanostructured layered composites has been developed. The developed composition makes it possible to increase the heat resistance of materials by approximately 10 times. This significantly increases the reliability and durability of gas turbine units in compressor stations. The structural and mechanical parameters of the layered nanostructured heat-resistant composites have been studied. Full article
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<p>The general view of the gas turbine unit—(<b>a</b>); the general view of the turbine blades, after 30,000 h of operation—(<b>b</b>); the destruction scheme of gas turbine blades from exposure to high-temperature aggressive media—(<b>c</b>).</p>
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<p>The corrosion stages of nozzle blades (the GTD111 alloy): the second (15,000 h)—(<b>a</b>); the third (19,000 h)—(<b>b</b>); the shoulder blades’ destruction—(<b>c</b>).</p>
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<p>The microstructure of the GTD111 material—(<b>a</b>); the corrosion of the blade (the GTD 111 alloy)—(<b>b</b>,<b>c</b>); the corrosive destruction of the surface layer (Alloy 1)—(<b>d</b>).</p>
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<p>The microstructure of the layered composite: GTD111 (1)—TBL (2)—Alloy 1 (3)—(<b>a</b>); TBL (2) structure—(<b>b</b>); Alloy 1 structure—(<b>c</b>,<b>d</b>); Alloy 2 structure—(<b>e</b>,<b>f</b>); the microelectron diffraction patterns of composite layers: Alloy 1—(<b>g</b>) and Alloy 2—(<b>h</b>).</p>
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<p>The microstructure of the layered composite: GTD111 (1)—TBL (2)—Alloy 1 (3)—(<b>a</b>); TBL (2) structure—(<b>b</b>); Alloy 1 structure—(<b>c</b>,<b>d</b>); Alloy 2 structure—(<b>e</b>,<b>f</b>); the microelectron diffraction patterns of composite layers: Alloy 1—(<b>g</b>) and Alloy 2—(<b>h</b>).</p>
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<p>The quantitative analysis of grain size in the structure of the composite materials: (<b>a</b>) Alloy 1; (<b>b</b>) Alloy 2.</p>
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<p>The X-ray diffraction patterns of composite materials: (<b>a</b>) TBL; (<b>b</b>) Alloy 1; (<b>c</b>) Alloy 2.</p>
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<p>The X-ray diffraction patterns of composite materials: (<b>a</b>) TBL; (<b>b</b>) Alloy 1; (<b>c</b>) Alloy 2.</p>
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<p>The dependence of the specific change in the mass of the GTU materials on the exposure times to an aggressive environment: Inconel 738LC (1); GTD 111 (2); Rene N6 (3); Alloy 1 (4); Alloy 2 (5).</p>
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23 pages, 4332 KiB  
Article
Transitioning to a Hydrogen Economy: Exploring the Viability of Adapting Natural Gas Pipelines for Hydrogen Transport through a Case Study on Compression vs. Looping
by Abubakar Jibrin Abbas, Salisu Kwalami Haruna, Martin Burby, Idoko Job John and Kabir Hassan Yar’Adua
Gases 2024, 4(2), 74-96; https://doi.org/10.3390/gases4020005 - 30 Apr 2024
Viewed by 2118
Abstract
The growing importance of hydrogen as an energy carrier in a future decarbonised energy system has led to a surge in its production plans. However, the development of infrastructure for hydrogen delivery, particularly in the hard-to-abate sectors, remains a significant challenge. While constructing [...] Read more.
The growing importance of hydrogen as an energy carrier in a future decarbonised energy system has led to a surge in its production plans. However, the development of infrastructure for hydrogen delivery, particularly in the hard-to-abate sectors, remains a significant challenge. While constructing new pipelines entails substantial investment, repurposing existing pipelines offers a cost-effective approach to jump-starting hydrogen networks. Many European countries and, more recently, other regions are exploring the possibility of utilising their current pipeline infrastructure for hydrogen transport. Despite the recent efforts to enhance the understanding of pipeline compatibility and integrity for hydrogen transportation, including issues such as embrittlement, blend ratios, safety concerns, compressor optimisation, and corrosion in distribution networks, there has been limited or no focus on pipeline expansion options to address the low-energy density of hydrogen blends and associated costs. This study, therefore, aims to explore expansion options for existing natural gas high-pressure pipelines through additional compression or looping. It seeks to analyse the corresponding cost implications to achieve an affordable and sustainable hydrogen economy by investigating the utilisation of existing natural gas pipeline infrastructure for hydrogen transportation as a cost-saving measure. It explores two expansion strategies, namely pipeline looping (also known as pipeline reinforcement) and compression, for repurposing a segment of a 342 km × 36 inch existing pipeline, from the Escravos–Lagos gas pipeline system (ELPS) in Nigeria, for hydrogen transport. Employing the Promax® process simulator tool, the study assesses compliance with the API RP 14E and ASME B31.12 standards for hydrogen and hydrogen–methane blends. Both expansion strategies demonstrate acceptable velocity and pressure drop characteristics for hydrogen blends of up to 40%. Additionally, the increase in hydrogen content leads to heightened compression power requirements until approximately 80% hydrogen in the blends for compression and a corresponding extension in looping length until around 80% hydrogen in the blend for looping. Moreover, the compression option is more economically viable for all investigated proportions of hydrogen blends for the PS1–PS5 segment of the Escravos–Lagos gas pipeline case study. The percentage price differentials between the two expansion strategies reach as high as 495% for a 20% hydrogen proportion in the blend. This study offers valuable insights into the technical and economic implications of repurposing existing natural gas infrastructure for hydrogen transportation. Full article
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<p>Pipeline expansion through inlet pressure increase [<a href="#B12-gases-04-00005" class="html-bibr">12</a>].</p>
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<p>An illustration of compressor spacings in pipeline capacity increment (maximum operating pressure—MOP) [<a href="#B12-gases-04-00005" class="html-bibr">12</a>].</p>
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<p>Pipeline looping schematic for flow increase.</p>
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<p>Escravos–Lagos pipeline network route on Southwestern Nigerian map.</p>
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<p>Existing pipeline single-pipe model diagram (* denoting a feed stream).</p>
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<p>Experimental workflow.</p>
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<p>Process diagram of pipeline expansion with looping/pipe reinforcement (* denoting a feed stream).</p>
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<p>Process diagram for gas network expansion through compression (* denoting a feed stream and -3- refers to the stream after heat exchanger XCHG-100).</p>
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<p>Pressure profile of the reinforced pipeline.</p>
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<p>Velocity behaviour in the reinforced and non-reinforced section.</p>
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<p>Required reinforcement length for equivalent and desired pressure drop.</p>
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<p>Compression option pressure profile.</p>
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<p>Gas velocities for compression option.</p>
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<p>Number of compressor stations required for equivalent and desired pressure drop.</p>
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<p>Comparison of pipeline expansion costs by looping versus compression.</p>
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25 pages, 20399 KiB  
Article
Management of Hybrid Wind and Photovoltaic System Electrolyzer for Green Hydrogen Production and Storage in the Presence of a Small Fleet of Hydrogen Vehicles—An Economic Assessment
by Anestis G. Anastasiadis, Panagiotis Papadimitriou, Paraskevi Vlachou and Georgios A. Vokas
Energies 2023, 16(24), 7990; https://doi.org/10.3390/en16247990 - 10 Dec 2023
Cited by 8 | Viewed by 2026
Abstract
Nowadays, with the need for clean and sustainable energy at its historical peak, new equipment, strategies, and methods have to be developed to reduce environmental pollution. Drastic steps and measures have already been taken on a global scale. Renewable energy sources (RESs) are [...] Read more.
Nowadays, with the need for clean and sustainable energy at its historical peak, new equipment, strategies, and methods have to be developed to reduce environmental pollution. Drastic steps and measures have already been taken on a global scale. Renewable energy sources (RESs) are being installed with a growing rhythm in the power grids. Such installations and operations in power systems must also be economically viable over time to attract more investors, thus creating a cycle where green energy, e.g., green hydrogen production will be both environmentally friendly and economically beneficial. This work presents a management method for assessing wind–solar–hydrogen (H2) energy systems. To optimize component sizing and calculate the cost of the produced H2, the basic procedure of the whole management method includes chronological simulations and economic calculations. The proposed system consists of a wind turbine (WT), a photovoltaic (PV) unit, an electrolyzer, a compressor, a storage tank, a fuel cell (FC), and various power converters. The paper presents a case study of green hydrogen production on Sifnos Island in Greece through RES, together with a scenario where hydrogen vehicle consumption and RES production are higher during the summer months. Hydrogen stations represent H2 demand. The proposed system is connected to the main power grid of the island to cover the load demand if the RES cannot do this. This study also includes a cost analysis due to the high investment costs. The levelized cost of energy (LCOE) and the cost of the produced H2 are calculated, and some future simulations correlated with the main costs of the components of the proposed system are pointed out. The MATLAB language is used for all simulations. Full article
(This article belongs to the Special Issue Techno-Economic Analysis and Optimization for Energy Systems)
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Graphical abstract

Graphical abstract
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<p>The island of Sifnos on a map of Greek islands (Aegean Sea—Cyclades).</p>
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<p>Road map of Sifnos (Triangles – Peaks, Dotted – Ship routes, Purple line - Borders).</p>
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<p>The proposed HyPS.</p>
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<p>Simplified flow chart of the implemented algorithm.</p>
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<p>Hourly wind speed curve per month (2020 year).</p>
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<p>Characteristic wind speed–power curve for WT (VESTAS 200 kW).</p>
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<p>Power curve production for VESTAS200 WT for the whole year (per hour)—estimated capacity factor of WT, CF = 37%.</p>
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<p>Data for PV system (PVGIS 2020) [<a href="#B33-energies-16-07990" class="html-bibr">33</a>].</p>
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<p>Power production curve for PV system for the whole year (per hour).</p>
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<p>H<sub>2</sub> consumption curve for vehicles for the whole year (per hour).</p>
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<p>Load demand curve for the whole year (per hour).</p>
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<p>Total power from the RES (WT + PV) for one year (per hour).</p>
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<p>H<sub>2</sub> production from the RES (WT + PV) for one year (per hour).</p>
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<p>Total power from the grid for one year (per hour).</p>
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<p>Total power to the grid for one year (per hour).</p>
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<p>Real hourly H<sub>2</sub> consumption curve for one year.</p>
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<p>Hourly H<sub>2</sub> storage curve for one year.</p>
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<p>Hourly H<sub>2</sub> deficit curve for one year.</p>
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<p>Hourly production curve of fuel cell for one year.</p>
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<p>Estimated reduction in the LCOE and price of green hydrogen produced for the proposed hybrid power system with a time horizon of 2050 assuming a uniform reduction in the installation cost (CAPEX) of its components by 2% annually.</p>
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<p>Estimated reduction in the LCOE and price of green hydrogen produced for the proposed hybrid power system through better capacity factor values for both WT (areas with better wind potential) and PV (more southerly areas).</p>
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<p>Effect of percentage reduction in electrolyzer cost on the LCOE value for the hybrid case study system.</p>
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18 pages, 3508 KiB  
Article
Mobile Laboratory Investigations of Industrial Point Source Emissions during the MOOSE Field Campaign
by Tara I. Yacovitch, Brian M. Lerner, Manjula R. Canagaratna, Conner Daube, Robert M. Healy, Jonathan M. Wang, Edward C. Fortner, Francesca Majluf, Megan S. Claflin, Joseph R. Roscioli, Elizabeth M. Lunny and Scott C. Herndon
Atmosphere 2023, 14(11), 1632; https://doi.org/10.3390/atmos14111632 - 30 Oct 2023
Cited by 5 | Viewed by 1656
Abstract
Industrial emissions of trace gases and VOCs can be an important contributor to air quality in cities. Disentangling different point sources from each other and characterizing their emissions can be particularly challenging in dense industrial areas, such as Detroit, Dearborn and surrounding areas [...] Read more.
Industrial emissions of trace gases and VOCs can be an important contributor to air quality in cities. Disentangling different point sources from each other and characterizing their emissions can be particularly challenging in dense industrial areas, such as Detroit, Dearborn and surrounding areas in Southeast Michigan (SEMI). Here, we leverage mobile measurements of trace gases and speciated volatile organic compounds (VOCs) to identify emitting sites. We characterize their complicated emissions fingerprints based on a core set of chemical ratios. We report chemical ratios for 7 source types including automakers, steel manufacturers, chemical refineries, industrial chemical use (cleaning; coatings; etc.), chemical waste sites, compressor stations, and more. The source dataset includes visits to over 85 distinct point sources. As expected, we find similarities between the different types of facilities, but observe variability between them and even at individual facilities day-to-day. Certain larger sites are better thought of as a collection of individual point sources. These results demonstrate the power of mobile laboratories over stationary sampling in dense industrial areas. Full article
(This article belongs to the Special Issue The Michigan-Ontario Ozone Source Experiment (MOOSE))
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<p>Aerodyne Mobile Laboratory Instrument Manifest for MOOSE-2021.</p>
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<p>Time traces (<b>A</b>) and correlation plot (<b>B</b>) of toluene versus the sum of C6–C9 aromatics. The molar ratio is taken from the slope of the correlation plot, m = 0.440.</p>
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<p>Overview map of study area showing Michigan and Ontario boundaries. Select cities (blue) and Michigan counties (grey) are labeled. Visited/measured sources are shown as pink dots, with those sources characterized here shown in darker pink and labeled with their site ID. Shorelines: NOAA [<a href="#B22-atmosphere-14-01632" class="html-bibr">22</a>], county lines: State of Michigan [<a href="#B23-atmosphere-14-01632" class="html-bibr">23</a>].</p>
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<p>Example chemical fingerprint for Facility MA130. Ratios of VOCs to the sum of aromatics and R<sup>2</sup> of the linear fit are listed beside their trace name (<b>top</b>). Additional ratios for other gas phase tracers are noted versus their denominator. Time traces for selected traces are shown (<b>middle</b>). A map (<b>bottom</b>) shows concentration over the driven path.</p>
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<p>Representative transects downwind of the chemical waste facility WA236 and the automaker assembly plant WA137. The map (<b>left</b>) shows the AML path colored by acetone concentration. The time traces (<b>right</b>) show a subset of measured species, with traces colored to match the axis labels. For legend of aromatic traces, see <a href="#atmosphere-14-01632-f004" class="html-fig">Figure 4</a>. A primary VOC plume (@ symbol) is shown, along with a lower intensity and broader plume (* symbol). These plumes correspond to the circled and labeled areas on the map.</p>
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<p>Sum of C6–C9 aromatics during Dearborn Loops under SW winds. (<b>A</b>) shows average concentrations. EGLE monitoring stations (purple triangles), inventory sources (white squares) and the outlines of 3 major facilities (WA87—automaker; WA0—steel; WA22—refinery) are also drawn. (<b>B</b>) shows a histogram of the measured concentrations in each map pixel, on a log scale. (<b>C</b>) shows the number of measurements in each map pixel, as well as roads driven over the course of the campaign.</p>
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<p>AML and MECP TAGA coordinated transects in Port Huron/Sarnia, from South to North, showing three distinct HCHO plumes, and two broad C8 aromatic plumes. Concentration as a function of kilometers north (<b>top</b>) and maps (<b>bottom</b>) are shown. The drive paths are colored by concentration, with the HCHO trace offset for clarity. The C8-aromatic axes are clipped at 3 ppb to emphasize the broad enhancements over other short-duration events. The petrochemical and refinery sources on the Canadian side of the river are labeled as Clusters 1 through 3. Wind barbs (white) point into the wind. Satellite image source: Google Maps. Imagery ©2023 TerraMetrics.</p>
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13 pages, 1526 KiB  
Article
Technological Aspects of Methane–Hydrogen Mixture Transportation through Operating Gas Pipelines Considering Industrial and Fire Safety
by Vadim Fetisov, Hadi Davardoost and Veronika Mogylevets
Fire 2023, 6(10), 409; https://doi.org/10.3390/fire6100409 - 23 Oct 2023
Cited by 27 | Viewed by 3872
Abstract
Pipeline transportation is widely regarded as the most cost-effective method for conveying substantial volumes of hydrogen across extensive distances. However, before hydrogen can be widely used, a new pipeline network must be built to reliably supply industrial users. An alternative way to rather [...] Read more.
Pipeline transportation is widely regarded as the most cost-effective method for conveying substantial volumes of hydrogen across extensive distances. However, before hydrogen can be widely used, a new pipeline network must be built to reliably supply industrial users. An alternative way to rather expensive investments in new infrastructure could be to use the existing pipeline network to add pure hydrogen to natural gas and further transport the gas mixture in an industrially safe way. The new solution necessities will be examined for compression, transportation, and fire hazard accidents, which have not been scrutinized by other scholars. This study presents the results of a comprehensive analysis of the methane–hydrogen mixture compression process and a mathematical description of the main pipeline operation during gas mixture transportation, considering industrial fire safety issues. By examining a case study involving a main gas pipeline and its associated mathematical model for hydrogen transportation, it becomes feasible to assess the potential hazards associated with various leakage areas and the subsequent occurrence of fires. The findings of this investigation demonstrate that the spontaneous combustion of hydrogen due to leakage from a natural gas pipeline is directly influenced by the proportion of hydrogen present in the gas mixture. If the hydrogen percentage reaches a balanced ratio of 50–50%, it is plausible that the equipment at the compressor station could be subject to detrimental consequences, potentially leading to accidents and fires. Furthermore, the obtained results from modeling in ANSYS Fluent software propose two practical scenarios, which demonstrate that despite the limited research conducted on the safety aspects and the occurrence of fires during the operation of hydrogen gas pipelines, industrial and fire safety necessitate the inclusion of hydrogen transport infrastructure as a pivotal element within the broader framework of hydrogen infrastructure development. Full article
(This article belongs to the Special Issue Hydrogen Safety: Challenges and Opportunities)
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<p>Cross-section of an underground pipeline.</p>
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<p>The algorithm for performing calculations.</p>
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<p>Range of heat flow and velocity vectors.</p>
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<p>Temperature distribution contours resulting from a pipeline rupture.</p>
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<p>Explosion propagation area in the event of a pipeline rupture due to pressure drops and gas mixture velocity.</p>
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14 pages, 2941 KiB  
Article
Experimental Comparison of Hydrogen Refueling with Directly Pressurized vs. Cascade Method
by Matteo Genovese, David Blekhman, Michael Dray, Francesco Piraino and Petronilla Fragiacomo
Energies 2023, 16(15), 5749; https://doi.org/10.3390/en16155749 - 1 Aug 2023
Cited by 12 | Viewed by 2662
Abstract
This paper presents a comparative analysis of two hydrogen station configurations during the refueling process: the conventional “directly pressurized refueling process” and the innovative “cascade refueling process.” The objective of the cascade process is to refuel vehicles without the need for booster compressors. [...] Read more.
This paper presents a comparative analysis of two hydrogen station configurations during the refueling process: the conventional “directly pressurized refueling process” and the innovative “cascade refueling process.” The objective of the cascade process is to refuel vehicles without the need for booster compressors. The experiments were conducted at the Hydrogen Research and Fueling Facility located at California State University, Los Angeles. In the cascade refueling process, the facility buffer tanks were utilized as high-pressure storage, enabling the refueling operation. Three different scenarios were tested: one involving the cascade refueling process and two involving compressor-driven refueling processes. On average, each refueling event delivered 1.6 kg of hydrogen. Although the cascade refueling process using the high-pressure buffer tanks did not achieve the pressure target, it resulted in a notable improvement in the nozzle outlet temperature trend, reducing it by approximately 8 °C. Moreover, the overall hydrogen chiller load for the two directly pressurized refuelings was 66 Wh/kg and 62 Wh/kg, respectively, whereas the cascading process only required 55 Wh/kg. This represents a 20% and 12% reduction in energy consumption compared to the scenarios involving booster compressors during fueling. The observed refueling range of 150–350 bar showed that the cascade process consistently required 12–20% less energy for hydrogen chilling. Additionally, the nozzle outlet temperature demonstrated an approximate 8 °C improvement within this pressure range. These findings indicate that further improvements can be expected in the high-pressure region, specifically above 350 bar. This research suggests the potential for significant improvements in the high-pressure range, emphasizing the viability of the cascade refueling process as a promising alternative to the direct compression approach. Full article
(This article belongs to the Section A5: Hydrogen Energy)
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<p>Hydrogen Refueling Process Methods.</p>
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<p>Blueprint zoom on the circuit for high-pressure buffer tanks.</p>
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<p>Pressure (<b>a</b>) and Mass Flow Rate (<b>b</b>) Trends for the Investigated refueling processes.</p>
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<p>Temperature Trends for Vehicle Tank (<b>a</b>), Chiller Coil (<b>b</b>), and 70 MPa nozzle outlet (<b>c</b>).</p>
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<p>Timeshift and Trend Comparisons for Vehicle Pressure (<b>a</b>), 70 MPa nozzle outlet temperature (<b>b</b>), and Hydrogen Mass Flow Rate (<b>c</b>).</p>
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<p>Power Trends for Booster Compressors (<b>a</b>) and Hydrogen Chiller (<b>b</b>).</p>
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<p>Specific Energy Consumption and Energy Improvements for the Hydrogen Chiller.</p>
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16 pages, 4628 KiB  
Article
Study of Estimated Ultimate Recovery Prediction and Multi-Stage Supercharging Technology for Shale Gas Wells
by Yanli Luo, Jianying Yang, Man Chen, Liu Yang, Hao Peng, Jinyuan Liang and Liming Zhang
Separations 2023, 10(8), 432; https://doi.org/10.3390/separations10080432 - 29 Jul 2023
Viewed by 1548
Abstract
The development of shale gas reservoirs often involves the utilization of horizontal well segmental multi-stage fracturing techniques. However, these reservoirs face challenges, such as rapid initial wellhead pressure and production decline, leading to extended periods of low-pressure production. To address these issues and [...] Read more.
The development of shale gas reservoirs often involves the utilization of horizontal well segmental multi-stage fracturing techniques. However, these reservoirs face challenges, such as rapid initial wellhead pressure and production decline, leading to extended periods of low-pressure production. To address these issues and enhance the production during the low-pressure stage, pressurized mining is considered as an effective measure. Determining the appropriate pressurization target and method for the shale gas wells is of great practical significance for ensuring stable production in shale gas fields. This study takes into account the current development status of shale gas fields and proposes a three-stage pressurization process. The process involves primary supercharging at the center station of the block, secondary supercharging at the gas collecting station, and the introduction of a small booster device located behind the platform separator and in front of the outbound valve group. By incorporating a compressor, the wellhead pressure can be reduced to 0.4 MPa, resulting in a daily output of 12,000 to 14,000 cubic meters from the platform. Using a critical liquid-carrying model for shale gas horizontal wells, this study demonstrates that reducing the wellhead pressure decreases the critical flow of liquid, thereby facilitating the discharge of the accumulated fluid from the gas well. Additionally, the formation pressure of shale gas wells is estimated using the mass balance method. This study calculates the cumulative production of different IPR curves based on the formation pressure. It develops a dynamic production decline model for gas outlet wells and establishes a relationship between the pressure depletion of gas reservoirs and the cumulative gas production before and after pressurization of H10 −2 and H10 −3 wells. The final estimated ultimate recovery of two wells is calculated. In conclusion, the implementation of multi-stage pressurization, as proposed in this study, effectively enhances the production of, and holds practical significance for, stable development of shale gas fields. Full article
(This article belongs to the Topic Oil, Gas and Water Separation Research)
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<p>(<b>a</b>) Xx H10 platform gas delivery process flow diagram; (<b>b</b>) Xx station gas transmission process flow diagram.</p>
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<p>(<b>a</b>) Graphs of different formation pressures and compression factors; (<b>b</b>) graphs of different formation pressures and viscosities; (<b>c</b>) product plot of different formation pressures with compression factors and viscosity.</p>
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<p>Relationship between Y/M and F/M.</p>
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<p>Comparison between predicted and measured data of the decay process of the average formation pressure under different cumulative production cases.</p>
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<p>Effect of wellhead pressure on fluid-carrying critical flow rate.</p>
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<p>Effect of wellhead pressure on fluid-carrying critical flow rate (black line meas IPR (Bottom pressure 4.1 MPa)).</p>
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<p>Effect of wellhead pressure on fluid-carrying critical flow rate.</p>
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<p>Change in oil pressure and gas production before and after pressurization of Xx H10 −3 well.</p>
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17 pages, 5207 KiB  
Article
Analysis of Heat Transfer of the Gas Head Cover of Diaphragm Compressors for Hydrogen Refueling Stations
by Shengdong Ren, Xiaohan Jia, Jiatong Zhang, Dianbo Xin and Xueyuan Peng
Processes 2023, 11(8), 2274; https://doi.org/10.3390/pr11082274 - 28 Jul 2023
Cited by 3 | Viewed by 1859
Abstract
The inadequate ability to dissipate heat of the gas head cover of the diaphragm compressor will result in its excessive temperature, which will put the operation of the hydrogen filling station at risk for safety issues and raise operating costs. This paper analyzed [...] Read more.
The inadequate ability to dissipate heat of the gas head cover of the diaphragm compressor will result in its excessive temperature, which will put the operation of the hydrogen filling station at risk for safety issues and raise operating costs. This paper analyzed the structure and the heat transfer characteristics of the gas head cover, along with the relevant heat transfer boundaries, based on which a finite element simulation model of the temperature distribution was established. A test rig for the temperature test of a 22 MPa diaphragm compressor was built to validate this simulation model. The results indicated that the simulated temperatures agree well with the measured values, and the deviation is within 9.1%. Further, this paper proposed two head cover structures for enhancing the heat transfer according to the temperature field distribution characteristics, and the simulation and experimental verification were carried out, respectively. The findings demonstrate that the method of enhancing heat transfer around the centre area is more effective, reducing the highest temperature by 14.1 °C, because it greatly lowers thermal conduction resistance, which is the principal impediment to the heat dissipation of the gas head cover. Full article
(This article belongs to the Special Issue Process Design and Modeling of Low-Carbon Energy Systems)
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<p>Structure of the diaphragm compressor.</p>
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<p>Heat transfer processes of the gas head cover.</p>
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<p>Heat transfers between the gas and the surfaces of the holes. (<b>a</b>) Discharge holes. (<b>b</b>) Suction holes.</p>
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<p>Heat transfers between the surfaces of nozzles and the gas head cover.</p>
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<p>Model of the gas head cover assembly.</p>
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<p>Mesh around the discharge holes.</p>
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<p>Positions of feature points.</p>
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<p>Results of mesh independence verification.</p>
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<p>Temperature test rig.</p>
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<p>Positions of the temperature measurement points.</p>
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<p>Temperature distribution of the gas head cover.</p>
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<p>Temperature with different natural convection heat transfer coefficients.</p>
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<p>Structure of augmented heat transfer of the outer surface.</p>
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<p>Structure of augmented heat transfer of the core high-temperature zone.</p>
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<p>Temperature distribution with augmented heat transfer of outer surface.</p>
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<p>Temperature distribution with augmented heat transfer of the core high-temperature zone.</p>
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10 pages, 3135 KiB  
Article
Electron Energy Spectrometer for MIR-THz FEL Light Source at Chiang Mai University
by Kittipong Techakaew, Kanlayaporn Kongmali and Sakhorn Rimjaem
Particles 2023, 6(3), 703-712; https://doi.org/10.3390/particles6030043 - 7 Jul 2023
Cited by 1 | Viewed by 1564
Abstract
The linear accelerator system of the PBP-CMU Electron Linac Laboratory has been designed with the aim of generating free-electron lasers (FELs) in the mid-infrared (MIR) and terahertz (THz) regions. The quality of the radiation is strongly dependent on the properties of the electron [...] Read more.
The linear accelerator system of the PBP-CMU Electron Linac Laboratory has been designed with the aim of generating free-electron lasers (FELs) in the mid-infrared (MIR) and terahertz (THz) regions. The quality of the radiation is strongly dependent on the properties of the electron beam. Among the important beam parameters, the electron beam energy and energy spread are particularly important. To accurately measure the electron beam energy, the first dipole magnet in the bunch compressor system and the downstream screen station are employed as an energy spectrometer. The A Space Charge Tracking Algorithm (ASTRA) software is used for the design and optimization of this system. Simulation results demonstrate that the developed spectrometer is capable of accurately measuring the energy within the 5–25 MeV range. The screen station system is designed and constructed to have the ability to capture a beam size with a resolution of 0.1 mm per pixel. This resolution is achieved with a screen-to-camera distance of 1.2 m, which proves sufficient for precise energy measurement. The systematic error in energy measurement is found to be less than 10%, with a minimum energy spread of 0.4% achievable when the horizontal beam size remains below 3 mm. Full article
(This article belongs to the Special Issue Generation and Application of High-Power Radiation Sources)
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<p>A schematic layout of the injector system, including the first two dipole magnets and other associated components. The location of the screen and the CCD camera is illustrated in the dashed orange rectangular box.</p>
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<p>A schematic layout of the electron energy spectrometer consisting of a 45° dipole magnet and a screen station.</p>
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<p>Schematic layout presenting the top view (<b>a</b>) and side view (<b>b</b>) of the transverse beam measurement setup. This setup comprises a phosphor screen, a CCD camera, and a computer for data acquisition and analysis.</p>
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<p>Systematic error of average energy measurement for electron bunch with average energy 5 MeV (<b>a</b>) and 25 MeV (<b>b</b>), considering values of initial energy spread and transverse beam size.</p>
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<p>Systematic error of energy spread measurement for electron bunch with average energy 5 MeV (<b>a</b>) and 25 MeV (<b>b</b>), considering values of initial energy spread and transverse beam size.</p>
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<p>Systematic errors of energy measurement for an electron bunch with an average energy of 5 MeV, considering various initial transverse emittance values.</p>
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<p>Longitudinal phase space distribution (<math display="inline"><semantics> <mrow> <mi>E</mi> <mi>k</mi> </mrow> </semantics></math>-<span class="html-italic">t</span>) with histogram, and scatter plots of transverse beam distribution (<span class="html-italic">x</span>,<span class="html-italic">y</span>) and transverse phase space distribution (<span class="html-italic">x</span>-<math display="inline"><semantics> <msup> <mi>x</mi> <mo>′</mo> </msup> </semantics></math> and <span class="html-italic">y</span>-<math display="inline"><semantics> <msup> <mi>y</mi> <mo>′</mo> </msup> </semantics></math>) at the transition radiation experimental station.</p>
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<p>The complete energy spectrum of an example beam with a bunch charge of 117.5 pC and a kinetic energy of 20.06 MeV.</p>
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