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32 pages, 9192 KiB  
Article
Reactivation of Abandoned Oilfields for Cleaner Energy Generation: Three-Dimensional Modelling of Reservoir Heterogeneity and Geometry
by Benjamin Michael Storey, Richard H. Worden, David D. McNamara, John Wheeler, Julian Parker and Andre Kristen
Processes 2024, 12(12), 2883; https://doi.org/10.3390/pr12122883 - 17 Dec 2024
Viewed by 266
Abstract
With the changing picture of global energy supplies and the shift toward the energy transition, it has never been more important to look for alternative sources of energy. Globally there are tens of thousands of abandoned oil fields with considerable reserves left behind. [...] Read more.
With the changing picture of global energy supplies and the shift toward the energy transition, it has never been more important to look for alternative sources of energy. Globally there are tens of thousands of abandoned oil fields with considerable reserves left behind. These have the potential to be reactivated to become an energy supply that is cleaner than conventional oil and gas. This can be achieved by the use of in situ combustion and the subsequent exploitation of the inherent increase in temperature and pressure to produce geothermal energy, allied to sequestration of the mixture of produced fluids. In situ combustion (ISC) has conventionally been used as an enhanced oil recovery technique, with a high failure rate that has been recently attributed to poor reservoir selection and project design. We suggest that the failure of many earlier ISC projects is due to insufficient appreciation of how the subsurface geology affects the process. With the use of computer numerical modelling, we aim to ascertain how the geometry and heterogeneity of the reservoir control the success of the process. Here we employ simple three-dimensional sector models to assess a variety of different petrophysical heterogeneities, within a set of different reservoir geometries, on the temperature, velocity, propagation stability and enthalpy rate. These models illustrate that the biggest impact on success of the ISC process for geothermal energy generation, as a function of temperature and enthalpy, is the location of the wells relative to the heterogeneities and the scale of heterogeneities. Metre-scale heterogeneities do not have a significant effect on this. Instead, the biggest contributor to the propagation stability and direction of the fire front is the presence of a large-scale (10 s to 100 s of metres) heterogeneities, such as channels, or the geometry of a tilted fault block; both have a strong control over the direction of the propagation, and therefore are important factors with regards to well placement. Full article
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Figure 1

Figure 1
<p>Relative permeability curves used in all simulations: (<b>a</b>) oil–water relative permeability and (<b>b</b>) liquid–gas relative permeability curves with temperature dependence included [<a href="#B62-processes-12-02883" class="html-bibr">62</a>].</p>
Full article ">Figure 2
<p>Viscosity vs. temperature graphs to illustrate how the initial oil viscosity decreases with increasing temperature [<a href="#B64-processes-12-02883" class="html-bibr">64</a>,<a href="#B65-processes-12-02883" class="html-bibr">65</a>].</p>
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<p>Diagrams of each of the different geometries that is used for the model, with injection and production wells marked and depth scale. (<b>a</b>) Base–case cube model without any tectonic structure, (<b>b</b>) periclinal fold with four-way dip closure, (<b>c</b>) tilted fault block dipping at 45°.</p>
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<p>Porosity distribution of the three heterogeneous sub-models (note that the homogeneous model is not represented here). (<b>a</b>) Gaussian distribution of porosity with a mean porosity of 20% and standard deviation of 4; (<b>b</b>) facies-controlled heterogeneity of a single channel of defined orientation that, in this case, is not intersected by the injector or producer wells; (<b>c</b>) layered model with alternating 5% and 20 percent layers. All models’ permeabilities are derived from the Kozeny–Carman relationship (Equation (1)), each sub model is used with each geo-model.</p>
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<p>Oil saturation distribution plots with the fire front marked, for each of the different type A models, no heterogeneity. (<b>a</b>) Model 1-A, homogeneous cube geometry, revealing the development of a wedge-shaped fire front moving more at the top than the base of the structure. (<b>b</b>) Model 2-A, homogeneous periclinal fold, illustrating the development of a wedge-shaped fire front with the majority of the oil bank to the top of the reservoir. (<b>c</b>) Model 3-A, homogenous tilted fault block, revealing a strong preference for the migration of oil up-dip and to the left of the reservoir.</p>
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<p>Graphs of average properties by layer for each homogenous model. (<b>a</b>) Average temperature of six hottest points. (<b>b</b>) Average velocity of the six hottest points. (<b>c</b>) Average propagation angle with respect to the production and injection wells for the six hottest points.</p>
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<p>Oil saturation distribution plots with the fire front marked on for each of the different type B models, with heterogeneous distribution of petrophysical properties. (<b>a</b>) Model 1-B, randomly distributed heterogeneity cube geometry, revealing a distorted fire front moving predominantly to the left of the grid and beginning to split (<b>b</b>) Model 2-B, randomly distributed heterogeneity periclinal fold, revealing a distorted shape to the fire front but moving towards the apex of the structure. (<b>c</b>) Model 3-B, randomly distributed heterogeneity tilted fault block, showing that the fire front preferentially migrates up-dip as well as the formation of a small movement towards the production well.</p>
Full article ">Figure 8
<p>Graphs of average properties by layer for each randomly distributed heterogeneity model. (<b>a</b>) Average temperature of six hottest points. (<b>b</b>) Average velocity of the six hottest points. (<b>c</b>) Average propagation angle with respect to the production and injection wells for the six hottest points.</p>
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<p>Oil saturation distribution plots with the fire front marked on for each of the different type C models, facies-controlled (channel) petrophysical heterogeneity. (<b>a</b>) Model 1-C, facies-controlled heterogeneity cube geometry, revealing minor movement of oil to the right-hand side of the upper layers of the reservoir. (<b>b</b>) Model 2-C, facies-controlled periclinal fold, revealing a small displacement of oil around the injection well within the upper layers of the reservoir. (<b>c</b>) Model 3-C, facies-controlled tilted fault block, revealing extinction of the fire front before it could develop and no movement of oil.</p>
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<p>Graphs of average properties by layer for each facies-controlled heterogeneity model. (<b>a</b>) Average temperature of six hottest points. (<b>b</b>) Average velocity of the six hottest points. (<b>c</b>) Average propagation angle with respect to the production and injection wells for the six hottest points.</p>
Full article ">Figure 11
<p>Oil saturation distribution plots with the fire front marked on for each of the different type D models, with layered stratigraphic petrophysical heterogeneity. (<b>a</b>) Model 1-D, layered cube geometry, revealing the preferential movement of oil within the higher porosity and permeability layers. (<b>b</b>) Model 2-D, layered periclinal fold, showing the preferential movement of oil within the high-porosity and permeability layers and slight distortions of the fire front within the top layer. (<b>c</b>) Model 3-D, layered tilted fault block, illustrating the preferential movement of oil within the high-porosity and permeability layers and the preferential movement of the fire front up-dip.</p>
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<p>Graphs of average properties by layer for each layered model. (<b>a</b>) Average temperature of the six hottest points. (<b>b</b>) Average velocity of the six hottest points. (<b>c</b>) Average propagation angle with respect to the production and injection wells for the six hottest points.</p>
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<p>Graph to illustrate the cumulative enthalpy of each model when run for a duration of 5 years, not including models 2-A, 3-A, or 3-B, as these models did not run to completion. Given the selected orientation of the channel relative to the injector and producer wells, the facies-controlled heterogeneity models do not develop a significant fire front and do not generate any significant enthalpy after 5 years. The other models generate enthalpy after 5 years, with the cube models generating earlier than others.</p>
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<p>Graph of the temperature difference compared to the base–case cube model to determine the different effects on the peak average temperature when changing the geometry of the reservoir for each heterogeneity. (<b>a</b>) Homogeneous reservoir. (<b>b</b>) Randomly distributed heterogeneity. (<b>c</b>) Facies-controlled (channel) heterogeneity. (<b>d</b>) Layered reservoir.</p>
Full article ">Figure 15
<p>Graph of the velocity difference compared to the base–case cube model to ascertain the different effects on the velocity when changing the geometry of the reservoir for each heterogeneity. (<b>a</b>) Homogeneous reservoir. (<b>b</b>) Randomly distributed heterogeneity. (<b>c</b>) Facies-controlled (channel) heterogeneity. (<b>d</b>) Layered reservoir.</p>
Full article ">Figure 16
<p>Graph of the propagation angle difference compared to the base–case cube model to ascertain the different effects on the propagation angle when changing the geometry of the reservoir for each heterogeneity. (<b>a</b>) Homogeneous reservoir. (<b>b</b>) Randomly distributed heterogeneity. (<b>c</b>) Facies-controlled (channel) heterogeneity. (<b>d</b>) Layered reservoir.</p>
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<p>Graphs of the temperature difference compared to the base–case homogeneous model to illustrate the different effects of the changing petrophysical heterogeneity for each reservoir geometry. (<b>a</b>) Cube model. (<b>b</b>) Periclinal fold model. (<b>c</b>) Tilted fault block model.</p>
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<p>Graphs of the velocity difference compared to the base–case homogeneous model to illustrate the different effects of the changing petrophysical heterogeneity for each reservoir geometry. (<b>a</b>) Cube model. (<b>b</b>) Periclinal fold model. (<b>c</b>) Tilted fault block model.</p>
Full article ">Figure 19
<p>Graphs of the propagation angle difference compared to the base–case homogeneous model to illustrate the different effects of the changing petrophysical heterogeneity for each reservoir geometry. (<b>a</b>) Cube model. (<b>b</b>) Periclinal fold model. (<b>c</b>) Tilted fault block model.</p>
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<p>Box and whisker pots of the difference between the cube and the other geometries, and between the homogeneous reservoir with the heterogeneous reservoirs, showing the interquartile ranges, median average and outliers. (<b>a</b>) Overall effects of temperature. (<b>b</b>) Overall effects on velocity. (<b>c</b>) Overall effects on propagation angle.</p>
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23 pages, 8695 KiB  
Article
Corrosion Inhibition of Carbon Steel Immersed in Standardized Reconstituted Geothermal Water and Individually Treated with Four New Biosourced Oxazoline Molecules
by Chahinez Helali, Stephanie Betelu, Romain Valentin, Sophie Thiebaud-Roux and Ioannis Ignatiadis
Metals 2024, 14(12), 1439; https://doi.org/10.3390/met14121439 - 16 Dec 2024
Viewed by 326
Abstract
The current demand for heat production via geothermal energy is increasingly rising amid concerns surrounding non-renewable forms of energy. The Dogger aquifer in the Paris Basin (DAPB) in France produces saline geothermal waters (GWs), which are as hot as 70–85 °C, anaerobic, slightly [...] Read more.
The current demand for heat production via geothermal energy is increasingly rising amid concerns surrounding non-renewable forms of energy. The Dogger aquifer in the Paris Basin (DAPB) in France produces saline geothermal waters (GWs), which are as hot as 70–85 °C, anaerobic, slightly acidic (pH 6.1–6.4), and characterized mainly by the presence of Cl, SO42−, CO2/HCO3, and H2S/HS. These GWs are corrosive, and the casings of all geothermal wells are carbon steel. Since 1989, these GWs have been progressively treated using petrosourced organic corrosion inhibitors (PS–OCI) at the bottom of the production wells. Currently, there is a great need to test not only new PS–OCIs but also, and above all, biosourced organic corrosion inhibitors (BS–OCIs) to improve the efficiency and environmental friendliness of this carbon-free geothermal energy source. The main objective of this study is to evaluate the potential performance of biosourced corrosion inhibitor candidates (BS–CICs) in terms of their inhibition efficiency (IE) for carbon steel corrosion. This was achieved using a previously established geochemical and electrochemical method to study the mechanisms and kinetics of the corrosion/scaling of carbon steel and optimize short-term corrosion inhibition in standardized reconstituted geothermal water (SRGW) representative of the DAPB’s waters. Four new molecules from the 2-oxazoline family were evaluated individually and compared based on their behavior and inhibition efficiency. These molecules exhibited a mixed nature (i.e., anodic and cathodic inhibitors), with a slight anodic predominance, and showed a significant IE at a concentration of at 10 mg/L during the first hours of immersion of CS-XC38 in SRGW. The average IEs, obtained via the three electrochemical techniques used for the determination of corrosion current densities, i.e., Jcorr(Rp), Jcorr(Tafel), and Jcorr(Rw), are 51%, 79%, 96%, and 93% for Decenox (C10:1), Decanox (C10:0), Undecanox (C11:0), and Tridecanox (C13:0), respectively. Full article
(This article belongs to the Special Issue Recent Advances in Corrosion and Protection of Metallic Materials)
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Figure 1
<p>Synthesis of decenoxHAm and Decenox (C10:1).</p>
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<p>Temporal evolution of the CS-XC38 electrode’s corrosion potential (E<sub>corr</sub> in mV/SCE) when immersed in SRGW in the presence of each of the four tested oxazolines at 10 mg/L compared to immersion without inhibitor.</p>
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<p>Temporal evolution of IE, obtained via J<sub>corr</sub> (R<sub>p</sub>) deduced from R<sub>p</sub> on new CS-X38 electrodes immersed in SRGW in the presence of each of the four oxazolines, tested at 10 mg/L.</p>
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<p>Temporal evolution of corrosion current density, J<sub>corr</sub>, deduced from R<sub>p</sub> on new CS-XC38 electrodes immersed in SRGW in the absence (without an inhibitor) and in the presence of each of the four oxazolines, tested at 10 mg/L.</p>
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<p>Evolution of Tafel curves of the CS-XC38 electrode immersed in SRGW in the presence of Decenox (C10:1) at concentrations of 5, 10, 20, 40, 80, and 160 mg/L, compared to immersion without inhibitors at immersion times between 43 and 57 min.</p>
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<p>Evolution of Tafel curves of the CS-XC38 electrode immersed in SRGW in the presence of each of the four oxazolines at 10 mg/L compared to immersion without inhibitors at immersion times between 43 and 57 min.</p>
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<p>Polarization curves of CS-XC38 electrode immersed in SRGW in the presence of Decenox (C10:1) (in green) or Decanox (C10:0) (in blue), both at 10 mg/L.</p>
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<p>Polarization curves of CS-XC38 electrode immersed in SRGW in the presence of (<b>A</b>) Decenox (C10:1) on the left and (<b>B</b>) Decanox (C10:0) on the right, both at 10 mg/L, as a function of immersion time.</p>
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<p>Evolution of IE (%) determined from J<sub>corr</sub> based on Tafel curves for CS-XC38 electrode immersed in SRGW in the presence of the four oxazolines at 10 mg/L at immersion times from 0 to 17 h.</p>
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<p>Evolution of electrochemical impedances, both in the Nyquist and in the Bode planes, measured on new CS-XC38 electrodes in the presence of each of the four oxazolines at 10 mg/L compared to without inhibitors as a function of immersion time in SRGW.</p>
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<p>Evolution of electrochemical impedances, in the Nyquist plane, measured on new CS-XC38 electrodes in the presence of Decanox (C10:0) at 10 mg/L compared to without inhibitors as a function of immersion time in SRGW.</p>
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<p>Evolutions of electrochemical impedance, in the Nyquist plane, measured on new CS-XC38 electrodes in the presence of Undecanox (C11:0) at 10 mg/L compared to without inhibitors as a function of immersion time in SRGW.</p>
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<p>Evolution of Tafel curves of new CS-XC38 electrodes in the presence of Undecanox (C11:0) at 10 mg/L as a function of immersion time in SRGW.</p>
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<p>Langmuir, Temkin, Freundlich, Frumkin, and El-Awady adsorption isotherms plotted from the polarization resistance (1st R<sub>p</sub>) of the CS-XC38 electrode in SRGW in the presence of Decenox (C10:1) at 70 °C.</p>
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<p>Langmuir adsorption isotherm, plotted from the average of 5 electrochemical polarization resistances (Rp average) of the CS-XC38 electrode in SRGW in the presence of Decenox (C10:1) at 70 °C.</p>
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<p>SEM photograph of the CS-XC38 electrode’s surface in the presence of Decenox (C10:1), showing that the CS-XC38 sample was electrochemically disturbed at 70 °C.</p>
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<p>Variation in coverage rate θ and corrosion current density J<sub>corr</sub> of CS-XC38 electrode in SRGW at 70 °C as a function of log (concentration) of Decenox (C10:1).</p>
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16 pages, 3984 KiB  
Article
Comparative Exergy Analysis of Series and Parallel Dual-Pressure Auto-Cascade Organic Rankine Cycles
by Yongsheng Li, Zhiyu Li, Haigang Zhang, Jieyu Zhang, Xiaohong He, Yanjin Qiao and Zeting Yu
Processes 2024, 12(12), 2872; https://doi.org/10.3390/pr12122872 - 16 Dec 2024
Viewed by 267
Abstract
The organic Rankine cycle (ORC) is a valuable method for harnessing low-temperature waste heat to generate electricity. In this study, two dual-pressure auto-cascade ORC systems driven by low-grade geothermal water are proposed in series and parallel configurations to ensure high thermal efficiency and [...] Read more.
The organic Rankine cycle (ORC) is a valuable method for harnessing low-temperature waste heat to generate electricity. In this study, two dual-pressure auto-cascade ORC systems driven by low-grade geothermal water are proposed in series and parallel configurations to ensure high thermal efficiency and power output. The energy and exergy analysis models for two systems are developed for comparative and parametric analysis, which uses a zeotropic refrigerant mixture of R134a and R245fa. The findings indicate that, with a heat source temperature of 393.15 K, the thermal efficiency and exergy efficiency of the series auto-cascade ORC reach 10.12% and 42.07%, respectively, which are 27% and 21.9% higher than those of the parallel auto-cascade ORC. However, the parallel cycle exhibits a higher net power output, indicating a better heat source utilization. The exergy analysis shows that evaporator 1 and the condenser possess the highest exergy destruction in both cycles. Finally, the parameter analysis reveals that the system performance is affected significantly by the heat source and heat sink temperature, the pinch temperature difference, and the refrigerant mixture concentration. These findings could provide valuable insights for improving the overall performance of ORCs driven by low-grade energy when using zeotropic refrigerant mixtures. Full article
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Figure 1
<p>Schematic diagram of the series auto-cascade organic Rankine cycle system (SAORC). (<b>a</b>) Schematic diagram of the SAORC. (<b>b</b>) <span class="html-italic">T</span>-<span class="html-italic">s</span> diagram of the SAORC.</p>
Full article ">Figure 1 Cont.
<p>Schematic diagram of the series auto-cascade organic Rankine cycle system (SAORC). (<b>a</b>) Schematic diagram of the SAORC. (<b>b</b>) <span class="html-italic">T</span>-<span class="html-italic">s</span> diagram of the SAORC.</p>
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<p>Schematic diagram of the parallel auto-cascade organic Rankine cycle system (PAORC). (<b>a</b>) Schematic diagram of the PAORC. (<b>b</b>) <span class="html-italic">T</span>-<span class="html-italic">s</span> diagram of the PAORC.</p>
Full article ">Figure 2 Cont.
<p>Schematic diagram of the parallel auto-cascade organic Rankine cycle system (PAORC). (<b>a</b>) Schematic diagram of the PAORC. (<b>b</b>) <span class="html-italic">T</span>-<span class="html-italic">s</span> diagram of the PAORC.</p>
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<p>Phase diagram of the zeotropic mixture of R134a and R245fa.</p>
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<p>Exergy destruction and exergy efficiency of components of the SAORC.</p>
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<p>Exergy destruction and exergy efficiency of components of the PAORC.</p>
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<p>The impacts of heat source temperature (<span class="html-italic">T<sub>source</sub></span>) on system performance. (<b>a</b>) Thermal efficiency and exergy efficiency. (<b>b</b>) Evaporation heat and net power output.</p>
Full article ">Figure 6 Cont.
<p>The impacts of heat source temperature (<span class="html-italic">T<sub>source</sub></span>) on system performance. (<b>a</b>) Thermal efficiency and exergy efficiency. (<b>b</b>) Evaporation heat and net power output.</p>
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<p>The impact of heat sink temperature (<span class="html-italic">T<sub>sink</sub></span>) on system performance. (<b>a</b>) Thermal efficiency and exergy efficiency. (<b>b</b>) Evaporation heat and net power output.</p>
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<p>The impact of heat sink temperature (<span class="html-italic">T<sub>sink</sub></span>) on system performance. (<b>a</b>) Thermal efficiency and exergy efficiency. (<b>b</b>) Evaporation heat and net power output.</p>
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<p>The effects of pinch temperature difference (<span class="html-italic">T<sub>pinch</sub></span>) on system performance. (<b>a</b>) Thermal efficiency and exergy efficiency. (<b>b</b>) Evaporation heat and net power output.</p>
Full article ">Figure 8 Cont.
<p>The effects of pinch temperature difference (<span class="html-italic">T<sub>pinch</sub></span>) on system performance. (<b>a</b>) Thermal efficiency and exergy efficiency. (<b>b</b>) Evaporation heat and net power output.</p>
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<p>The effects of mass fraction of zeotropic mixture (<span class="html-italic">x<sub>mass</sub></span>) on system performance. (<b>a</b>) Thermal efficiency and exergy efficiency. (<b>b</b>) Evaporation heat and net power output.</p>
Full article ">Figure 9 Cont.
<p>The effects of mass fraction of zeotropic mixture (<span class="html-italic">x<sub>mass</sub></span>) on system performance. (<b>a</b>) Thermal efficiency and exergy efficiency. (<b>b</b>) Evaporation heat and net power output.</p>
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18 pages, 2675 KiB  
Article
Analysis and Recommendations on the Current State of Renewable Energy Development in Tibet
by Yue Meng, Boyang Gao, Yuwen Duan, Yiyuan Wang and Huanyu Li
Sustainability 2024, 16(24), 10974; https://doi.org/10.3390/su162410974 - 14 Dec 2024
Viewed by 430
Abstract
Tibet, with its abundant hydraulic, solar, and wind resources, stands at the forefront of China’s renewable energy development. This paper provides a comprehensive analysis of the current state of clean energy development in Tibet, highlighting the region’s vast potential and the challenges it [...] Read more.
Tibet, with its abundant hydraulic, solar, and wind resources, stands at the forefront of China’s renewable energy development. This paper provides a comprehensive analysis of the current state of clean energy development in Tibet, highlighting the region’s vast potential and the challenges it faces. We find that, while Tibet has made significant strides in harnessing its natural endowments, infrastructural limitations, seasonal fluctuations, and technological hurdles constrain the development of clean energy. This paper offers a multifaceted set of recommendations aimed at accelerating clean energy development in Tibet, including policy reforms, infrastructure enhancements, and technological innovations. Our study’s unique contributions lie in its holistic approach to clean energy development, its detailed analysis of the regional energy policies, and its forward-looking recommendations that balance ecological protection with energy security. By adhering to the principle of ecological priority and conducting innovative research in clean energy development, Tibet can leverage its carbon sequestration capabilities for environmental protection while promoting sustainable economic and social development. This paper provides valuable insights for policymakers and scholars, offering a roadmap for the sustainable development of Tibet’s economy and a reference for similar regions embarking on clean energy transitions. Full article
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<p>Installed capacity of various types of electric power in Tibet from 2017–2021. Source: China Electric Power Statistical Yearbook 2022.</p>
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<p>Total water resources of various provinces in China in 2021. Source: National Bureau of Statistics of China.</p>
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<p>Installed capacity and power generation of hydropower in Tibet from 2016 to 2021. Source: China Electric Power Statistical Yearbook 2021.</p>
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<p>Wind power installed capacity and power generation in Tibet from 2016 to 2021. Source: China Electric Power Statistical Yearbook 2022.</p>
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<p>Installed capacity and power generation in Tibet from 2016 to 2021. Source: China Electric Power Statistical Yearbook 2022.</p>
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<p>Total installed capacity and growth rate of power in Tibet from 2016 to 2022. Source: Tibet Statistical Yearbook.</p>
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<p>Tibetan clean energy related policies. Source: Tibet Autonomous Region People’s Government.</p>
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22 pages, 848 KiB  
Article
Effects of Primary Energy Consumption and Alternative Energy Patents on CO2 Emissions in China
by Lina Lai and Yongzhong Qiao
Sustainability 2024, 16(24), 10963; https://doi.org/10.3390/su162410963 - 13 Dec 2024
Viewed by 374
Abstract
China’s significant carbon emissions have attracted global attention, and the country has committed to reaching a peak in carbon emissions before 2030 and achieving carbon neutrality by 2060. It is crucial to achieve this goal by effectively controlling the combustion of primary fuels [...] Read more.
China’s significant carbon emissions have attracted global attention, and the country has committed to reaching a peak in carbon emissions before 2030 and achieving carbon neutrality by 2060. It is crucial to achieve this goal by effectively controlling the combustion of primary fuels and developing alternative energy technologies. The existing literature has studied the effects of primary energy consumption on CO2 emissions, alternative energy technology on CO2 emissions, and energy patents on CO2 emissions. However, there are few studies on the effects of the relationship between primary energy consumption and alternative energy technology patents. This study analyzes the effects of primary energy consumption and alternative energy patents on CO2 emission intensity and CO2 emissions per capita, and their relationship using canonical correlation analysis. Our results are as follows. First, CO2 emissions from natural gas and liquefied petroleum gas have positive effects (correlation coefficients of 0.102 and 0.275, respectively), while CO2 emissions from gasoline, fuel oil, diesel, and kerosene have negative effects on CO2 emission intensity (correlation coefficients of −0.767, −0.420, −0.138, and −0.035, respectively). Second, patents for devices for producing mechanical power from muscle energy have large positive effects on total CO2 emissions (correlation coefficient of 0.533). Finally, the more the patents utilize waste heat, geothermal energy, hydro energy, and wind energy, the higher the CO2 emissions from liquefied petroleum gas, gasoline, and crude oil, and the lower the CO2 emissions from diesel, which are conducive to controlling CO2 emissions. Therefore, energy policies will be more effective, improve the living environment, and promote sustainable development based on the CO2 emissions level from primary energy consumption and the control degree of CO2 emissions by alternative energy. Full article
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Figure 1
<p>Comparison of CO<sub>2</sub> emission intensity among major developed countries or regions during 1960–2014.</p>
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<p>Comparison of CO<sub>2</sub> emissions per capita in major developed countries or regions during 1960–2016.</p>
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30 pages, 18891 KiB  
Article
Geothermal Condition Investigation and Resource Potential Evaluation of Shallow Geothermal Energy in the Yinchuan Area, Ningxia, China
by Wengang Qu, Chao Yang, Hui Qian, Panpan Xu, Yanyan Gao, Leiqiang Wei and Qi Long
Sustainability 2024, 16(24), 10962; https://doi.org/10.3390/su162410962 - 13 Dec 2024
Viewed by 362
Abstract
Shallow geothermal energy (SGE) is a promising green and sustainable energy source, gaining prominence in light of the dual-carbon target. This study investigated the SGE resources in the Yinchuan area. Suitability zones and the potential of SGE resources were determined based on the [...] Read more.
Shallow geothermal energy (SGE) is a promising green and sustainable energy source, gaining prominence in light of the dual-carbon target. This study investigated the SGE resources in the Yinchuan area. Suitability zones and the potential of SGE resources were determined based on the comprehensive analysis about thermophysical parameters, hydrogeological conditions, and geological environment. Our findings revealed that the effective thermal conductivity in the Yinchuan area surpasses those of other cities, indicating significant potential for SGE. The thermostat layer depth ranges from 40 to 60 m, with a geothermal gradient between 0.81 and 6.19 °C/100 m. Regions with poor adaptability for a borehole heat exchanger (BHE) are mainly distributed in the western and southern parts of the Yinchuan area, whereas moderately and highly adaptable areas are primarily located in the central and eastern areas, respectively. The total geothermal resource of the BHE in the Yinchuan area amounts to 1.07 × 108 GJ/a, generating significant economic benefits of 1.07 × 109 CNY/a and saving 1.09 × 106 t/a of standard coal annually. This initiative leads to significant reductions in CO2, SO2, and NOx emissions by 2.61 × 106 t/a, 1.86 × 104 t/a, and 6.57 × 103 t/a, respectively. Additionally, it results in potential savings of 0.309 × 109 CNY/a in environmental treatment costs. The methods and models used in this study have potential for similar geothermal surveys in arid and cold regions. The results also contribute essential insights for policy formulation and sustainable development strategies related to shallow geothermal resources in the Yinchuan area. Full article
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<p>Maps showing the location (<b>a</b>), geomorphology (<b>b</b>), hydrogeology (<b>c</b>), and DEM (<b>d</b>) of the study area.</p>
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<p>Hydrogeological profile of the study area (<b>A</b>,<b>A′</b>), modified from [<a href="#B66-sustainability-16-10962" class="html-bibr">66</a>].</p>
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<p>Maps showing the sampling points (<b>a</b>) and field test points (<b>b</b>) of the study area.</p>
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<p>The evaluation framework of the BHE in the Yinchuan area.</p>
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<p>Geothermal geological conditions in the Yinchuan area.</p>
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<p>The hydrogeological conditions in the Yinchuan area.</p>
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<p>The thickness ratio of sand/clay in the Yinchuan area.</p>
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<p>Suitability zones of the BHE in the Yinchuan area.</p>
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<p>Heat capacity per unit area within a depth of 200 m in China’s provincial capitals (data collected from [<a href="#B91-sustainability-16-10962" class="html-bibr">91</a>]).</p>
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<p>Calculation sub-regions of heat exchange power.</p>
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<p>Calculation results of heat exchange power zones of the BHE (<b>a</b>) consider the land use coefficient, (<b>b</b>) do not consider the land use coefficient.</p>
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<p>Single hole heat exchange power of the Yinchuan area in winter (<b>a</b>) and in summer (<b>b</b>).</p>
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<p>The resource potential evaluation results of the BHE in Yinchuan area.</p>
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<p>Economic and environmental benefits of the BHE in the Yinchuan area.</p>
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26 pages, 3317 KiB  
Review
A Comprehensive Review on Technologies for Achieving Zero-Energy Buildings
by Yushi Wang, Beining Hu, Xianhai Meng and Runjin Xiao
Sustainability 2024, 16(24), 10941; https://doi.org/10.3390/su162410941 - 13 Dec 2024
Viewed by 461
Abstract
The booming of the building industry has led to a sharp increase in energy consumption. The advancement of zero-energy buildings (ZEBs) is of great significance in mitigating climate change, improving energy efficiency, and thus realizing sustainable development of buildings. This paper reviews the [...] Read more.
The booming of the building industry has led to a sharp increase in energy consumption. The advancement of zero-energy buildings (ZEBs) is of great significance in mitigating climate change, improving energy efficiency, and thus realizing sustainable development of buildings. This paper reviews the recent progress of key technologies utilized in ZEBs, including energy-efficient measures (EEMs), renewable energy technologies (RETs), and building energy management system (BEMS), aiming to provide reference and support of the wider implementation of ZEBs. EEMs can reduce energy demand by optimizing the envelope design, phase change materials integration, efficient HVAC systems, and user behavior. The renewable energy sources discussed here are solar, biomass, wind, and geothermal energy, including distributed energy systems introduced to integrated various renewable resources and meet users’ demand. This study focuses on the application of building energy management in ZEBs, including energy use control, fault detection and diagnosis, and management optimization. The recent development of these three technologies mainly focuses on the combination with artificial intelligence (AI). In addition, this paper also emphasizes possible future research works about user behavior and zero-energy communities to improve the energy efficiency from a more complicated perspective. Full article
(This article belongs to the Special Issue Net-Zero-Energy Building Solutions for Sustainability)
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<p>Amount of literature on ZEBs in different databases in 2013–2023.</p>
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<p>Density visualization of ZEBs research in 2013–2023.</p>
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<p>The trend of keyword co-occurrence of EEMs in ZEBs research from 2017 to 2022.</p>
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<p>The trend of keyword co-occurrence of RETs in ZEBs research from 2018–2021.</p>
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<p>The trend of keyword co-occurrence of BEMS in ZEBs research from 2019 to 2021.</p>
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<p>Number of published papers on building energy management in ZEBs from 2018 to 2023.</p>
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<p>Keyword co-occurrence of intelligent BEMSs in ZEBs research from 2020 to 2023.</p>
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<p>The framework of the research methodology in this work [<a href="#B136-sustainability-16-10941" class="html-bibr">136</a>].</p>
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20 pages, 6214 KiB  
Article
Flowing Salt Solution Thin Film Vaporization and Heat Transfer Mechanisms: A Molecular Dynamics Study
by Dayuan Yuan, Chao Li, Liuyang Zhang and Shengqiang Shen
Energies 2024, 17(24), 6286; https://doi.org/10.3390/en17246286 - 13 Dec 2024
Viewed by 228
Abstract
Geothermal energy offers a sustainable way, through heating a salt solution, to generate electricity and extract salt, minimizing environmental impact while supporting clean energy needs. The thermal behavior and vaporization mechanisms of flowing salt solution thin films are investigated in this study using [...] Read more.
Geothermal energy offers a sustainable way, through heating a salt solution, to generate electricity and extract salt, minimizing environmental impact while supporting clean energy needs. The thermal behavior and vaporization mechanisms of flowing salt solution thin films are investigated in this study using molecular dynamics (MD) simulations. The research focuses on the evaporation dynamics of NaCl solutions at various temperatures (450 K and 550 K) and under different flow conditions, providing insights into the microstructural evolution and the role of ionic interactions. The simulations reveal critical aspects of evaporation, such as the formation and behavior of ion clusters, the impact of temperature on evaporation rates, and the effects of flow on heat transfer efficiency. Key findings include the observation that higher temperatures accelerate the evaporation process and promote ion clustering, while flow conditions enhance heat and mass transfer, leading to more efficient vaporization. These results contribute to a deeper understanding of the thermal dynamics in saline solutions, with implications for industrial processes such as desalination, crystallization, and thermal management. Full article
(This article belongs to the Special Issue The Status and Development Trend of Geothermal Resources)
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<p>Dilute NaCl solution evaporation at 450 K. Water is rendered as transparent, Na and Cl atoms are colored orange and green, respectively. (<b>a</b>–<b>f</b>) snapshots at 20 ps, 30 ps, 40 ps, 50 ps, 60 ps and 70 ps, respectively.</p>
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<p>Evaporation of a dilute NaCl solution at 550 K. Water molecules are rendered as transparent, with Na and Cl atoms colored orange and green, respectively. Snapshots are taken at (<b>a</b>) 20 ps, (<b>b</b>) 30 ps, (<b>c</b>) 40 ps, (<b>d</b>) 50 ps, (<b>e</b>) 60 ps, and (<b>f</b>) 70 ps.</p>
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<p>Contour plots of density evolution during the solution evaporation at different temperatures. (<b>a</b>) 450 K; (<b>b</b>) 550 K. The vertical axis indicates the location of the film.</p>
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<p>Temperature effect on vaporization rate.</p>
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<p>Snapshots of molecular dynamics simulation during boiling of water on a flowing plate. Oxygen atoms are colored dark blue, and hydrogen atoms are colored light blue. Aluminum atoms are colored red. NaCl ions are colored yellow and green.</p>
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<p>Contour plots of density evolution during solution evaporation at different flowing speeds. (<b>a</b>) Static; (<b>b</b>) 1 ns/10 fs. The vertical axis indicates the location of the film.</p>
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<p>Saturation pressure as a function of temperature for various solutions. The black line represents experimental data obtained from the NIST database. The red circles indicate values predicted by the TIP4P water model. The remaining symbols correspond to NaCl solutions with different mole fractions.</p>
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<p>Evaporation of a dilute NaCl solution at 550 K. Water molecules are rendered as transparent, with Na and Cl atoms colored orange and green, respectively. Snapshots are taken at (<b>a</b>) 20 ps, (<b>b</b>) 30 ps, (<b>c</b>) 40 ps, (<b>d</b>) 50 ps, (<b>e</b>) 60 ps, and (<b>f</b>) 70 ps.</p>
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<p>Contour plots of density evolution during solution evaporation at different temperatures. (<b>a</b>) 450 K; (<b>b</b>) 550 K. The vertical axis indicates the location of the film.</p>
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<p>Ion clustering evolution at different temperatures.</p>
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<p>Flow rate effects on heat efficiency.</p>
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14 pages, 7391 KiB  
Article
The Role of the Emeishan Large Igneous Province in Hydrocarbon Formation in the Anyue Gas Field, Sichuan Basin, China
by Zhiyong Ni, Chuanqing Zhu, Huichun Liu, Chengyu Yang, Ganggang Shao, Wen Zhang and Bing Luo
Minerals 2024, 14(12), 1266; https://doi.org/10.3390/min14121266 (registering DOI) - 12 Dec 2024
Viewed by 335
Abstract
This study investigates the impact of the Emeishan Large Igneous Province (ELIP) on hydrocarbon formation within the Anyue gas field in the Sichuan Basin. As a major Middle to Late Permian large igneous province, the ELIP hosted intense mantle plume activity that reshaped [...] Read more.
This study investigates the impact of the Emeishan Large Igneous Province (ELIP) on hydrocarbon formation within the Anyue gas field in the Sichuan Basin. As a major Middle to Late Permian large igneous province, the ELIP hosted intense mantle plume activity that reshaped regional tectonics and thermal structures, indirectly influencing hydrocarbon accumulation. This paper examines three primary factors in hydrocarbon evolution linked to the ELIP: its thermal influence, induced fluid activity, and role in hydrocarbon cracking. Data reveal that the thermal effects of the ELIP extend to the central Sichuan Basin, where an elevated paleogeothermal gradient has driven hydrocarbon evolution in the Anyue gas field. Petrographic characteristics, chronological data, fluid inclusion features, and C–O, S, and Pb isotopic signatures collectively indicate that around 260 Ma, a hydrothermal event occurred in the Sichuan Basin, closely aligned with a natural gas charging event. The combined effects of a heightened geothermal gradient and hydrothermal fluids (with temperatures up to 320 °C) suggest that paleo-oil reservoirs had already cracked into natural gas during the peak ELIP activity. Full article
(This article belongs to the Special Issue Volcanism and Oil–Gas Reservoirs—Geology and Geochemistry)
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<p>(<b>a</b>) Geology of the ELIP, location of wells and boreholes sampling sites (modified after [<a href="#B8-minerals-14-01266" class="html-bibr">8</a>]); (<b>b</b>) sedimentary model map of the Sichuan Basin during the Late Permian Period (modified after [<a href="#B12-minerals-14-01266" class="html-bibr">12</a>]).</p>
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<p>Relationship between Ro and depth for the studied wells in the Sichuan Basin, (<b>a</b>) NJ well; (<b>b</b>) Y1 well; (<b>c</b>) JS28 well (data provided by the Exploration and Development Research Institute of Southwest Oil and Gas Field Company, PetroChina; well locations are shown in <a href="#minerals-14-01266-f001" class="html-fig">Figure 1</a>).</p>
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<p>Petrographic characteristics of the Zdn<sub>4</sub> Formation of the GS101 well of Anyue gas field (<b>a</b>) hand specimen of core; (<b>b</b>,<b>c</b>) photos of thin sections under transmitting light; (<b>d</b>,<b>e</b>) photos of thin sections under reflecting light; (<b>f</b>) SEM photo.</p>
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<p>Characteristics of inclusions in the Zdn<sub>4</sub> Formation of the GS6 well, (<b>a</b>) Fluid inclusions distributed along fractures in burial dolomite; (<b>b</b>) fluid inclusions located along mineral growth zones in hydrothermal dolomite; (<b>c</b>) fluid inclusions developed in the growth rims of quartz crystals; (<b>d</b>,<b>e</b>) Laser Raman spectra of CH₄ (methane) inclusions; (<b>f</b>) schematic diagram of the spatial distribution of fluid inclusions.</p>
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<p>(<b>a</b>) C and O isotopic compositions of the different types of dolomites in Sichuan Basin (GS101 well (this study); W99 well [<a href="#B52-minerals-14-01266" class="html-bibr">52</a>]; W112 and Z6 wells [<a href="#B53-minerals-14-01266" class="html-bibr">53</a>]); (<b>b</b>) plot of <sup>207</sup>Pb/<sup>204</sup>Pb vs. <sup>206</sup>Pb/<sup>204</sup>Pb plot of sulfide in the Zdn<sub>4</sub> Formation (5517.5 m) of the GS101 well (Pb evolution curves of upper crust, orogene, mantle, and lower crust after [<a href="#B54-minerals-14-01266" class="html-bibr">54</a>]).</p>
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<p>Schematic diagram of burial history, thermal history, and key timing events in hydrocarbon accumulation for well GS-6 (modified after [<a href="#B18-minerals-14-01266" class="html-bibr">18</a>]).</p>
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11 pages, 4319 KiB  
Article
Research on Monitoring Methods for Fluid Flow in Strata
by Feng Zhang
Processes 2024, 12(12), 2846; https://doi.org/10.3390/pr12122846 - 12 Dec 2024
Viewed by 271
Abstract
In many projects, it is important to monitor the direction of groundwater flow, but conventional methods make it difficult. Through streaming potential detection technology, under the action of external pressure, liquid can be forced to flow through solid pores to generate directional flow, [...] Read more.
In many projects, it is important to monitor the direction of groundwater flow, but conventional methods make it difficult. Through streaming potential detection technology, under the action of external pressure, liquid can be forced to flow through solid pores to generate directional flow, and a flow potential can be generated at both ends of solid pores. The phenomenon of different streaming potentials can help engineers determine the direction of fluid flow. In this study, tests were conducted using a core injection system and a streaming potential tester to carry out injections on sandstone samples of two different structures to study the effects of different injection pressures and different salinities on the variation in the streaming potential in sandstone. Moreover, a small-scale field water injection monitoring experiment was also carried out to observe the actual situation of the streaming potential generated during water injection in the field formation structure. The laboratory test results show that the flow potential is accompanied by the liquid injection process in the sandstone sample, and the flow potential produced by the sandstone with different porosities is obviously different, Therefore, the flow potential associated with the actual rock injection process can be used to infer porosity and permeability. This study provides a new method for monitoring underground fluids and is expected to improve the efficiency of oil extraction and geothermal development. Full article
(This article belongs to the Special Issue Oil and Gas Drilling Processes: Control and Optimization)
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<p>Model diagram of the streaming potential measurement system for indoor rock mass.</p>
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<p>Streaming potential measurement system diagram of the indoor core.</p>
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<p>Micrograph of the thin-slice structure of sandstone A (Magnify 50×).</p>
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<p>Micrograph of thin-slice structure of sandstone B (Magnify 50×).</p>
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<p>Sandstone core processing.</p>
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<p>Sandstone core placement in a high-pressure vessel.</p>
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<p>Curves of the relationships between the injection pressure and streaming potential.</p>
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<p>Curve of the relationship between the injection pressure and streaming potential.</p>
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<p>Comparison of the injection results for sandstone A and sandstone B.</p>
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<p>Underground strata distribution and water injection.</p>
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<p>(<b>a</b>) Potential at beginning of water injection; (<b>b</b>) after 12 min of water injection; (<b>c</b>) after 16 min of water injection; (<b>d</b>) after 20 min of water injection.</p>
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<p>(<b>a</b>) Potential at beginning of water injection; (<b>b</b>) after 12 min of water injection; (<b>c</b>) after 16 min of water injection; (<b>d</b>) after 20 min of water injection.</p>
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22 pages, 3843 KiB  
Article
Performance Improvement of the LNG Regasification Process Based on Geothermal Energy Using a Thermoelectric Generator and Energy and Exergy Analyses
by Amin Mohammadi and Akbar Maleki
Sustainability 2024, 16(24), 10881; https://doi.org/10.3390/su162410881 - 12 Dec 2024
Viewed by 344
Abstract
In this paper, a new approach is proposed to improve the performance of the LNG regasification process in a geothermal-transcritical CO2–LNG cycle by using thermoelectric generators. Energy and exergy analyses were applied to the proposed system and the plant’s performance is [...] Read more.
In this paper, a new approach is proposed to improve the performance of the LNG regasification process in a geothermal-transcritical CO2–LNG cycle by using thermoelectric generators. Energy and exergy analyses were applied to the proposed system and the plant’s performance is compared with the conventional CO2–LNG cycle. To achieve the optimal solution for the system, a multi-objective optimization technique based on a genetic algorithm is used. This study’s findings revealed that in the conventional CO2–LNG cycle, the highest exergy destruction occurs in the preheater. However, integrating a thermoelectric generator allows a portion of this destroyed exergy to be converted into power. The proposed system demonstrated 2% less exergy destruction compared to the conventional system. Moreover, the TEG contributes additional power, increasing the net output power of the system by 24%. This improvement ultimately enhances the overall exergy efficiency of the system. The analysis also concluded that, although a lower LNG mass flow rate reduces the system’s net power output, it improves the exergy efficiency. Overall, the proposed system exhibits an 8.37% higher exergy efficiency and a 24.22% greater net output power compared to the conventional CO2–LNG cycle. Full article
(This article belongs to the Section Energy Sustainability)
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<p>Conventional integration of the transcritical CO<sub>2</sub> cycle and LNG.</p>
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<p>Schematic diagram of the new system proposed.</p>
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<p>The EDR of different equipment in conventional systems and the proposed system.</p>
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<p>Comparison of the share of each equipment in the total exergy destruction of conventional systems and the proposed system.</p>
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<p>Total exergy efficiency and NOP vs. CO<sub>2</sub> TIT.</p>
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<p>Generated power vs. inlet temperature of the CO<sub>2</sub> turbine.</p>
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<p>Exergy efficiency and NOP vs. the inlet pressure of the CO<sub>2</sub> turbine.</p>
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<p>Scheme performance vs. condenser pressure.</p>
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<p>Power production vs. condenser pressure.</p>
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<p>System performance vs. the minimum temperature difference in the condenser.</p>
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<p>Mass flow rate variation and power generation vs. the minimum temperature difference in the condenser.</p>
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<p>System performance vs. the TEG outlet temperature.</p>
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<p>System performance vs. the minimum temperature difference in the preheater.</p>
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<p>Pareto front for the new proposed system.</p>
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18 pages, 3635 KiB  
Article
Diagnostic Approach and Tool for Assessing and Increasing the Sustainability of Renewable Energy Projects
by Jing Tian, Sam Culley, Holger R. Maier, Aaron C. Zecchin and James Hopeward
Sustainability 2024, 16(24), 10871; https://doi.org/10.3390/su162410871 - 11 Dec 2024
Viewed by 524
Abstract
The imperative of achieving net zero carbon emissions is driving the transition to renewable energy sources. However, this often leads to carbon tunnel vision by narrowly focusing on carbon metrics and overlooking broader sustainability impacts. To enable these broader impacts to be considered, [...] Read more.
The imperative of achieving net zero carbon emissions is driving the transition to renewable energy sources. However, this often leads to carbon tunnel vision by narrowly focusing on carbon metrics and overlooking broader sustainability impacts. To enable these broader impacts to be considered, we have developed a generic approach and a freely available assessment tool on GitHub that not only facilitate the high-level sustainability assessment of renewable energy projects but also indicate whether project-level decisions have positive, negative, or neutral impacts on each of the sustainable development goals (SDGs). This information highlights potential problem areas and which actions can be taken to increase the sustainability of renewable energy projects. The tool is designed to be accessible and user-friendly by developing it in MS Excel and by only requiring yes/no answers to approximately 60 diagnostic questions. The utility of the approach and tool are illustrated via three desktop case studies performed by the authors. The three illustrative case studies are located in Australia and include a large-scale solar farm, biogas production from wastewater plants, and an offshore wind farm. Results show that the case study projects impact the SDGs in different and unique ways and that different project–level decisions are most influential, highlighting the value of the proposed approach and tool to provide insight into specific projects and their sustainability implications, as well as which actions can be taken to increase project sustainability. Full article
(This article belongs to the Section Energy Sustainability)
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<p>The proposed approach for identifying the project–level decisions that have to be made during the development of renewable energy projects that affect SDGs.</p>
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<p>Developed relationships between Project–level Decision Themes and the SDGs. This consists of a Sankey diagram [<a href="#B29-sustainability-16-10871" class="html-bibr">29</a>] showing which project–level decision themes impact different SDGs, colour-coded by SDG, enabling project–level decisions that require attention to be identified. Note that the widths of the lines indicate the number of questions in the developed questionnaire that either fall within the category of project–level decision themes or potentially cause an impact (positive or negative) on an SDG.</p>
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<p>The proposed approach for identifying the relationships between Project–level Decision Themes and the SDGs for specific renewable energy projects, as well as screenshots of required user inputs via the MS Excel-based implementation tool.</p>
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<p>Illustrative result figures plotted by the MS Excel-based implementation tool. (<b>a</b>) presents the high-level sustainability assessments for the energy project under consideration. (<b>b</b>) presents the identification of project actions most suited to increasing sustainability.</p>
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<p>High-level summary of the key characteristics of the three illustrative case studies used to demonstrate the application and benefit of the proposed approach and MS Excel tool.</p>
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<p>Summary of high-level SDG impacts for the three illustrative case studies.</p>
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<p>Impact of project–level decision themes on relevant SDGs for the three illustrative case studies considered. The “traffic light” indicators on the right-hand side of the figure summarise the impact on a particular SDG due to project–level decisions. The traffic light indicators on the left-hand side of the figure summarise the contribution of a particular project–level decision theme to the overall impact of a particular SDG.</p>
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26 pages, 5768 KiB  
Article
Thermal Hazard Evaluation and Prediction in Deep Excavations for Sustainable Underground Mining
by Linqi Huang, Yunfeng Wei, Zhiying Chen, Zhaowei Wang, Yinan Liu, Lu Sun and Chao Li
Sustainability 2024, 16(24), 10863; https://doi.org/10.3390/su162410863 - 11 Dec 2024
Viewed by 382
Abstract
With the advent of the deep mining era, thermal damage in mines has become increasingly significant. The high-temperature environment in underground mines adversely impacts the physiological and psychological health of operators, reduces work efficiency, elevates the risk of accidents, and disrupts sustainable mining [...] Read more.
With the advent of the deep mining era, thermal damage in mines has become increasingly significant. The high-temperature environment in underground mines adversely impacts the physiological and psychological health of operators, reduces work efficiency, elevates the risk of accidents, and disrupts sustainable mining operations. Consequently, the development of accurate and reliable methods for classifying thermal hazards is essential for enabling mining enterprises to implement effective prevention strategies. Furthermore, such methods provide a theoretical basis for the sustainable management and utilization of geothermal energy. This study systematically considered factors influencing underground thermal damage and selected 10 quantitative indicators, encompassing both natural and human factors, as evaluation criteria. The CRITIC method was employed to determine the weight of each indicator, which was then integrated with uncertainty measurement theory to develop a novel thermal hazard assessment framework (CRITICUM). This framework enables the classification of thermal hazards in deep mine roadways. The evaluation results generated by the CRITICUM system were subsequently used to train machine learning predictive models. During the training process, the particle swarm optimization algorithm (PSO) was utilized to identify the most suitable prediction model parameters for the complex thermal environment of deep mines by leveraging its capability for continuous iterative evolution. The optimized parameters replaced the original random forest (RF) model parameters, resulting in an enhanced thermal damage prediction model (PSO-RF) with an accuracy of 96.55%, outperforming the standard RF model by 3%. Finally, the prediction model’s accuracy was validated using engineering case data, demonstrating that the results met practical engineering requirements. In summary, the proposed CRITICUM-PSO-RF evaluation and prediction model can accurately classify thermal damage in deep mines and provide a valuable reference for ensuring site safety and supporting the sustainable utilization of geothermal energy. Full article
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<p>Site conditions of the roadway in the Sanshandao Gold Mine (1000 m deep): (<b>a</b>) 1050 m levels and (<b>b</b>) 1065 m levels.</p>
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<p>CRITICUM thermal hazard evaluation system.</p>
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<p>Distribution of indicators for all methods.</p>
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<p>Single-indicator measurement functions: (<b>a</b>) airflow temperature; (<b>b</b>) relative humidity; (<b>c</b>) geothermal gradient; (<b>d</b>) depth of workface; (<b>e</b>) roadway section area; (<b>f</b>) air volume; (<b>g</b>) wind speed; (<b>h</b>) rock temperature; (<b>i</b>) geothermal water heat dissipation; (<b>j</b>) electromechanical heat dissipation.</p>
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<p>Single-indicator measurement functions: (<b>a</b>) airflow temperature; (<b>b</b>) relative humidity; (<b>c</b>) geothermal gradient; (<b>d</b>) depth of workface; (<b>e</b>) roadway section area; (<b>f</b>) air volume; (<b>g</b>) wind speed; (<b>h</b>) rock temperature; (<b>i</b>) geothermal water heat dissipation; (<b>j</b>) electromechanical heat dissipation.</p>
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<p>Prediction accuracy curve and confusion matrix for n_trees = 500. (<b>a</b>) The prediction accuracy of the test set; (<b>b</b>) the confusion matrix.</p>
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<p>Prediction accuracy curve for training set and test sets.</p>
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<p>Prediction accuracy curves of SVM on training and testing sets. (<b>a</b>) The prediction accuracy on the training set; (<b>b</b>) the prediction accuracy on the test set.</p>
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<p>The BP neural network prediction accuracy curve. (<b>a</b>) The prediction accuracy on the training set; (<b>b</b>) the prediction accuracy on the test set.</p>
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<p>Schematic diagram of random forest structure for PSO.</p>
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<p>Prediction accuracy curve and confusion matrix for n_trees = 581. (<b>a</b>) The prediction accuracy on the test set; (<b>b</b>) the confusion matrix.</p>
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<p>Ranking of feature importance.</p>
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<p>A map showing the geographic location of the Xiadian Gold Mine.</p>
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<p>A schematic diagram of the location of the mining roadway at the −662 m~−780 m levels of the Xiadian Gold Mine model [<a href="#B52-sustainability-16-10863" class="html-bibr">52</a>].</p>
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10 pages, 5198 KiB  
Article
A Study on the Application of a Deep Thermal Reservoir by Using a Magnetotelluric Sounding Method: Taking an Example of Geothermal Resources’ Exploration in the Western Taikang Uplift of the Southern North China Basin
by Bowen Xu, Huailiang Zhu, Min Zhang, Zhongyan Yang, Gaofeng Ye, Zhilong Liu, Zhiming Hu, Bingsong Shao and Yuqi Zhang
Processes 2024, 12(12), 2839; https://doi.org/10.3390/pr12122839 - 11 Dec 2024
Viewed by 326
Abstract
Geothermal resources are abundant in the Southern North China Basin, which is one of the prospective areas hosting low–medium-temperature geothermal resources in sedimentary basins in China. The purpose of this work is to reveal the formation and storage conditions of the geothermal resources [...] Read more.
Geothermal resources are abundant in the Southern North China Basin, which is one of the prospective areas hosting low–medium-temperature geothermal resources in sedimentary basins in China. The purpose of this work is to reveal the formation and storage conditions of the geothermal resources in the western margin of the Taikang Uplift and delineate the range of potential geothermal reservoirs. This paper uses five magnetotelluric sounding profiles for data processing and analysis, including the calculation of 2D skewness and electric strike. Data processing, analysis, and NLCG 2D inversion were performed on MT data, which consisted of 111 measurement points, and reliable two-dimensional resistivity models and resistivity planes were obtained. In combination with drilling verification and the analysis of geophysical logging data, the stratigraphic lithology and the range of potential geothermal reservoirs were largely clarified. The results show that using the magnetotelluric sounding method can well delineate the range of deep geothermal reservoirs in sedimentary basins and that the MT method is suitable for exploring buried geothermal resources in deep plains. The analytical results showed that the XZR-1 well yielded 1480 cubic meters of water per day, with the water temperature of the wellhead being approximately 78 °C, and combined with the results of this electromagnetic and drilling exploration, a geothermal geological model and genesis process of the west of the Taikang Uplift area was constructed. The water yield and temperature were higher than those of previous exploration results, which has important guiding significance for the future development and utilization of karst fissure heat reservoirs in the western Taikang Uplift. Full article
(This article belongs to the Special Issue Oil and Gas Drilling Processes: Control and Optimization)
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<p>A regional tectonic map of the Taikang Uplift in the Southern North China Basin.</p>
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<p>Geological map of bedrock in western Taikang Uplift of Southern North China Basin.</p>
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<p>Analysis results of skewness of MT01~MT05 profiles.</p>
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<p>Analyzed principal electric axes of MT01~MT05 profiles.</p>
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<p>Two-dimensional inversion TE+TM model fitting situation diagram of profile of MT02: (<b>a</b>) measured apparent resistivity; (<b>b</b>) predicted resistivity; (<b>c</b>) measured impedance phase; (<b>d</b>) predicted impedance phase.</p>
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<p>Two-dimensional inversion resistivity model (<b>a</b>) and explanation diagram (<b>b</b>) of MT02 profile.</p>
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<p>Two-dimensional inversion resistivity model (<b>a</b>) and explanation diagram (<b>b</b>) of MT04 profile.</p>
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<p>Pumping test of XZR-1 well.</p>
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<p>Genetic model of hydro-geothermal system of Taikang Uplift in Southern North China Basin.</p>
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19 pages, 8263 KiB  
Article
Effect of Volumetric Flow Rate on Heat Transfer Characteristics of Single-Fractured Rock with Different Surface Morphology and External Temperature
by Ying Zhuang, Na Huang and Yujing Jiang
Processes 2024, 12(12), 2821; https://doi.org/10.3390/pr12122821 - 9 Dec 2024
Viewed by 432
Abstract
The primary aim of this study is to explore how varying flow rates impact the heat transfer in single fractures, taking into account the effects of surface roughness, aperture and external temperature of the rock. Utilizing COMSOL Multiphysics, the fluid flow and heat [...] Read more.
The primary aim of this study is to explore how varying flow rates impact the heat transfer in single fractures, taking into account the effects of surface roughness, aperture and external temperature of the rock. Utilizing COMSOL Multiphysics, the fluid flow and heat transfer through 3D fracture models characterized by different roughness and apertures were simulated with volumetric flow rates ranging from 1 × 10−6 m3/s to 1 × 10−5 m3/s. The combined effects of these factors on key metrics, including outlet temperature, thermal breakthrough time, energy extraction efficiency, and heat transfer coefficients were systematically analyzed. The results indicate that water flow rate dominantly influences heat transfer, followed by fracture surface morphology and rock external temperature. Higher flow rates enhance both heat transfer and total heat extraction, while also increasing temperature non-uniformity, which improves overall heat extraction efficiency. Surface roughness significantly affects temperature distribution, leading to heterogeneous thermal profiles, especially in narrower fractures. Additionally, higher external temperatures and flow rates facilitate faster thermal breakthroughs by reducing thermal resistance. The interplay between surface roughness and thermal breakthrough time is intricate, with increased roughness prolonging breakthrough times in smaller apertures but potentially reducing them in larger ones. At smaller apertures, increasing the JRC from 2.29 to 17.33 results in a 1.01 to 1.20 times increase in thermal breakthrough time, whereas at larger apertures, thermal breakthrough time decreases by a factor of 1.01 to 1.29. This highlights the importance of carefully selecting fluid parameter in the design of geothermal projects to optimize heat extraction efficiency. Full article
(This article belongs to the Section Chemical Processes and Systems)
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<p>Rough surfaces generated using different H values. (<b>a</b>) A 2D representation of the fracture surface height using different colors, parameter <span class="html-italic">z</span> denotes the height of the fracture surface; (<b>b</b>) 3D representation of the fracture surface, where the grayscale intensity and surface undulations represent the roughness (for both figures the upper is JRC1 and the lower is JRC2, Cartesian coordinates have been used).</p>
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<p>Initial and boundary conditions for heated-flow model.</p>
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<p>Mesh of the simulation model (including fracture and the half part of the rock mass).</p>
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<p>Fluid temperature fields in JRC2 when volumetric flow rate <span class="html-italic">Q</span> = 1 × 10<sup>−6</sup> m<sup>3</sup>/s with different external temperature <span class="html-italic">T</span><sub>ext</sub> and fracture aperture <span class="html-italic">b</span> ((<b>a</b>–<b>d</b>) correspond with different <span class="html-italic">b</span>, and the <span class="html-italic">T</span><sub>ext</sub> from left to right at each aperture is 333.15 K, 353.15 K, 373.15 K and 393.15 K).</p>
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<p>Fluid temperature fields in JRC2 when volumetric flow rate <span class="html-italic">Q</span> = 1 × 10<sup>−6</sup> m<sup>3</sup>/s with different external temperature <span class="html-italic">T</span><sub>ext</sub> and fracture aperture <span class="html-italic">b</span> ((<b>a</b>–<b>d</b>) correspond with different <span class="html-italic">b</span>, and the <span class="html-italic">T</span><sub>ext</sub> from left to right at each aperture is 333.15 K, 353.15 K, 373.15 K and 393.15 K).</p>
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<p>Fluid temperature fields in JRC2 when <span class="html-italic">b</span> = 2 mm with different <span class="html-italic">Q</span> and <span class="html-italic">T</span><sub>ext</sub> ((<b>a</b>–<b>d</b>) correspond with different <span class="html-italic">Q</span>, and the <span class="html-italic">T</span><sub>ext</sub> from left to right at each aperture is 333.15 K, 353.15 K, 373.15 K and 393.15 K).</p>
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<p>Fluid temperature fields under <span class="html-italic">b</span> = 2 mm and <span class="html-italic">Q</span> = 9 × 10<sup>−6</sup> m<sup>3</sup>/s with different <span class="html-italic">T</span><sub>ext</sub>293.15–311.15.</p>
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<p>Fluid temperature fields under <span class="html-italic">b</span> = 2 mm and <span class="html-italic">Q</span> = 9 × 10<sup>−6</sup> m<sup>3</sup>/s with different <span class="html-italic">T</span><sub>ext</sub>293.15–311.15.</p>
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<p>Evolution of <span class="html-italic">T</span><sub>out</sub> with <span class="html-italic">Q</span> under different <span class="html-italic">T</span><sub>ext</sub> values: (<b>a</b>) JRC1; (<b>b</b>) JRC2.</p>
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<p>Double-parameter characterizations of <span class="html-italic">T</span><sub>out</sub>: (<b>a</b>) JRC1; (<b>b</b>) JRC2 (the variations in <span class="html-italic">T</span><sub>out</sub> under the same <span class="html-italic">T</span><sub>ext</sub> and <span class="html-italic">Q</span> reflect the results for different <span class="html-italic">b</span>).</p>
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<p>Variation of <span class="html-italic">T</span><sub>out</sub> with time at different <span class="html-italic">T</span><sub>ext</sub> and <span class="html-italic">Q</span> when <span class="html-italic">b</span> = 0.5 mm; (<b>a</b>) <span class="html-italic">Q</span> = 1 × 10<sup>−6</sup> m<sup>3</sup>/s; (<b>b</b>) <span class="html-italic">Q</span> = 2 × 10<sup>−6</sup> m<sup>3</sup>/s; (<b>c</b>) <span class="html-italic">Q</span> = 3 × 10<sup>−6</sup> m<sup>3</sup>/s; (<b>d</b>) <span class="html-italic">Q</span> = 4 × 10<sup>−6</sup> m<sup>3</sup>/s. (The horizontal dashed lines from top to bottom represent the thermal breakthrough temperatures at 393.15, 373.15, 353.15 and 333.15K, respectively).</p>
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<p>Relationship between thermal breakthrough time <span class="html-italic">t</span> and <span class="html-italic">Q</span> under different <span class="html-italic">T</span><sub>ext</sub> and JRC. (<b>a</b>) <span class="html-italic">b</span> = 0.5 mm; (<b>b</b>) <span class="html-italic">b</span> = 1 mm; (<b>c</b>) <span class="html-italic">b</span> = 1.5 mm; (<b>d</b>) <span class="html-italic">b</span> = 2 mm.</p>
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<p>Relationship between thermal breakthrough time <span class="html-italic">t</span> and <span class="html-italic">Q</span> under different <span class="html-italic">T</span><sub>ext</sub> and <span class="html-italic">b</span>; (<b>a</b>) JRC1; (<b>b</b>) JRC2.</p>
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<p>Relationship between heat transfer quantities <span class="html-italic">Q</span><sub>t</sub> and <span class="html-italic">Q</span> for different <span class="html-italic">T</span><sub>ext</sub>; (<b>a</b>) JRC1; (<b>b</b>) JRC2 (the variations in <span class="html-italic">Q</span><sub>t</sub> under the same <span class="html-italic">T</span><sub>ext</sub> and <span class="html-italic">Q</span> reflect the results for different <span class="html-italic">b</span>).</p>
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<p>Double-parameter characterizations of heat transfer quantities <span class="html-italic">Q</span><sub>t</sub>. The differences between the real and fitting values are denoted by the error bar with the vertical lines. (<b>a</b>) JRC1; (<b>b</b>) JRC2 (the variations in <span class="html-italic">Q</span><sub>t</sub> under the same <span class="html-italic">T</span><sub>ext</sub> and <span class="html-italic">Q</span> reflect the results for different <span class="html-italic">b</span>).</p>
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<p>Relationship between heat transfer coefficients <span class="html-italic">h</span> and <span class="html-italic">Q</span>; (<b>a</b>) <span class="html-italic">T</span><sub>ext</sub> = 333.15 K; (<b>b</b>) <span class="html-italic">T</span><sub>ext</sub> = 353.15 K; (<b>c</b>) <span class="html-italic">T</span><sub>ext</sub> = 373.15 K; (<b>d</b>) <span class="html-italic">T</span><sub>ext</sub> = 393.15 K.</p>
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<p>Relationship between heat transfer coefficients <span class="html-italic">h</span> and <span class="html-italic">Q</span>; (<b>a</b>) <span class="html-italic">T</span><sub>ext</sub> = 333.15 K; (<b>b</b>) <span class="html-italic">T</span><sub>ext</sub> = 353.15 K; (<b>c</b>) <span class="html-italic">T</span><sub>ext</sub> = 373.15 K; (<b>d</b>) <span class="html-italic">T</span><sub>ext</sub> = 393.15 K.</p>
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