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学者姓名：穆亮
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Abstract ：
在新工科建设的背景下,工程教育面临跨学科融合、创新能力培养等新需求.传热学作为工科学生的基础课程之一,承担着培养学生理论与实践结合能力的重要职责.然而,传统的传热学课程存在教学内容陈旧、教学方法单一、理论与实践脱节、学生创新能力和跨学科思维不足等问题,难以适应新工科要求.针对这些问题,提出了课程内容优化、教学方法创新、实践教学强化等教学改革措施,并通过实践探索了改革的效果.结果表明,这些措施显著提升了学生的学习兴趣和综合能力,符合新工科人才培养的需求.
Keyword ：
传热学 传热学 实践探索 实践探索 教学改革 教学改革 新工科 新工科
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| GB/T 7714 | 穆亮 , 崔勍焱 . 新工科背景下传热学课程教学改革与实践探索 [J]. | 当代教育实践与教学研究（电子刊） , 2025 , (6) : 41-44 . |
| MLA | 穆亮 等. "新工科背景下传热学课程教学改革与实践探索" . | 当代教育实践与教学研究（电子刊） 6 (2025) : 41-44 . |
| APA | 穆亮 , 崔勍焱 . 新工科背景下传热学课程教学改革与实践探索 . | 当代教育实践与教学研究（电子刊） , 2025 , (6) , 41-44 . |
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Natural gas hydrate (NGH) mining via CH4/CO2 exchange integrates CH4 extraction with CO2 geological sequestration, thereby facilitating the achievement of carbon neutrality. However, the relatively low replacement cost remains a significant bottleneck that hinders its large-scale application. In this study, we investigated the potential of intermittent ultrasonic assistance to enhance CH4/CO2 replacement in hydrate-bearing sediments. The effects of ultrasonic power, experimental pressure, and temperature, as well as initial water and hydrate saturations, were systematically analyzed. Results demonstrated that both CH4 recovery and CO2 sequestration rates exhibited an increasing trend with higher ultrasonic power. Specifically, at 100% ultrasonic power, the CH4 recovery and CO2 sequestration rates reached 79.06% and 55.94%, respectively. Additionally, both rates increased as the pressure decreased and the temperature rose. Notably, ultrasonic assistance significantly improved CH4/CO2 replacement even under conditions where the experimental pressure exceeded the CH4 hydrate phase boundary, or the temperature was below the freezing point. Increased initial water saturation was found to be beneficial for the ultrasonic-assisted CH4/CO2 replacement, whereas a higher hydrate saturation negatively impacted the process. These findings provide valuable insights into enhancing CH4/CO2 swapping and contribute to the advancement of NGH mining and CO2 geological sequestration technologies.
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| GB/T 7714 | Mu, Liang , Zeng, Jiguang , Lin, Xinhan et al. Intermittent Ultrasonic-Assisted CO2 Replacement for CH4 Extraction from Hydrate-Bearing Clay-Silt Sediments [J]. | ENERGY & FUELS , 2025 , 39 (17) : 7990-8000 . |
| MLA | Mu, Liang et al. "Intermittent Ultrasonic-Assisted CO2 Replacement for CH4 Extraction from Hydrate-Bearing Clay-Silt Sediments" . | ENERGY & FUELS 39 . 17 (2025) : 7990-8000 . |
| APA | Mu, Liang , Zeng, Jiguang , Lin, Xinhan , Liu, Menglong , Cui, Qingyan . Intermittent Ultrasonic-Assisted CO2 Replacement for CH4 Extraction from Hydrate-Bearing Clay-Silt Sediments . | ENERGY & FUELS , 2025 , 39 (17) , 7990-8000 . |
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The recovery of CH4 from coalbed gas (CBG) is significant for improving energy utilization and mitigating the greenhouse effect. In this study, CH4 was separated from CBG by forming sII hydrate with 5.56 mol % 1,3-dioxolane (DIOX) solution assisted by an eco-friendly promoter sodium lauroyl glutamate (SLG). The effects of SLG concentration, initial pressure and temperature, stirring rate, and CBG composition were systematically investigated. The results revealed that the addition of SLG notably diminished the hydrate induction time and reaction durations. The presence of 500 ppm of SLG decreased the CH4 concentration to 15.50 mol % from the initial 30.23 mol %, and the CH4 recovery and separation factor reached 81.70% and 3.34, respectively. Comparative analyses with other eco-friendly surfactants highlighted the substantial advantages of SLG. The CH4 concentration in the residual gas first decreased and then increased with the augmentation of the initial pressure, temperature, and stirring rate. An inverse pattern was observed in the variations of CH4 recovery and separation factor. This indicated that there existed an optimal initial pressure, temperature, and stirring rate for CBG separation. The CH4 content in the hydrate was increased to 91.59% after a fourth-stage enrichment, meeting the standards for the direct injection of CBG into natural gas pipelines. These findings provide valuable insights for CH4 separation from CBG by forming sII hydrate with eco-friendly promoters.
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| GB/T 7714 | Mu, Liang , Zhu, Xiaohai , Lai, Jintao et al. Methane Recovery from Coalbed Gas by Forming sII Hydrate with the Aid of a Novel Eco-Friendly Promoter [J]. | ENERGY & FUELS , 2025 , 39 (8) : 3752-3764 . |
| MLA | Mu, Liang et al. "Methane Recovery from Coalbed Gas by Forming sII Hydrate with the Aid of a Novel Eco-Friendly Promoter" . | ENERGY & FUELS 39 . 8 (2025) : 3752-3764 . |
| APA | Mu, Liang , Zhu, Xiaohai , Lai, Jintao , Zeng, Jiguang , Cui, Qingyan . Methane Recovery from Coalbed Gas by Forming sII Hydrate with the Aid of a Novel Eco-Friendly Promoter . | ENERGY & FUELS , 2025 , 39 (8) , 3752-3764 . |
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The gas-hydrate-sediment-water multiphase flow is often involved in drilling and exploitation of natural gas hydrate (NGH) reservoirs in seabed due to its weak cementation; therefore, understanding hydrate formation and decomposition in sediment-contained slurries is important. In this work, CH4 hydrate formation and decomposition in clay-silt slurries was explored, the effects of clay type and content, stirring rate, additives, experimental temperature, and pressure were systematically investigated. The presence of clay notably accelerated CH4 hydrate formation in slurries, and the montmorillonite exhibited a more obvious promotion effect than kaolinite. As the stirring rate increased, the induction time and reaction time were shortened, while the gas consumption rate and water conversion increased. The addition of 500 ppm sodium dodecyl sulfate (SDS) and 1.0 wt % fulvic acid (FA) significantly reduced the induction time and increased hydrate formation rate. During the interaction of SDS and sediment, CH4 hydrate formed in the slurries instantaneously. The CH4 hydrate decomposition rate in slurries increased as the experimental temperature increased or the pressure decreased. The temperature had a limited impact on the decomposition time above freezing point, while it was significant below freezing point. The presence of clay notably decreased the CH4 hydrate decomposition rate in slurries. Compared to the clay-free system, the Delta T d values (temperature decreased during hydrate decomposition) in the montmorillonite systems were decreased, while they were increased in the kaolinite systems. The findings provide valuable insights for the exploitation of marine NGH.
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| GB/T 7714 | Mu, Liang , Lai, Jintao , Li, Xianlong et al. Methane Hydrate Formation and Decomposition Process in Clay-Silt Slurries [J]. | ENERGY & FUELS , 2024 , 38 (16) : 15103-15115 . |
| MLA | Mu, Liang et al. "Methane Hydrate Formation and Decomposition Process in Clay-Silt Slurries" . | ENERGY & FUELS 38 . 16 (2024) : 15103-15115 . |
| APA | Mu, Liang , Lai, Jintao , Li, Xianlong , Zhao, Huixing , Zeng, Jiguang , Cui, Qingyan . Methane Hydrate Formation and Decomposition Process in Clay-Silt Slurries . | ENERGY & FUELS , 2024 , 38 (16) , 15103-15115 . |
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Although the hydrate-based coal bed gas (CBG) separations have been investigated, the obtained CH4 recovery ratios were not quite satisfactory. To further improve CH4 extraction, this study developed a high-efficiency CBG recovery method via hydrate formation in emulsions facilitated by an excellent anti-agglomerant. Thermodynamic promoters were introduced to lower operating pressure and the hydrate equilibrium conditions were determined. Then the effect of water-cut (40-100 vol%), initial pressure, experimental temperature, stirring rate and feed gas composition was investigated. The CH4 concentration in equilibrium gas first decreased then increased as the water-cut increased. Specifically, it decreased from 30.16 mol% to 8.23 mol% in the 60 vol% water-cut emulsions and CH4 recovery reached 88.02 % at 274.15 K and an initial pressure of 3.0 MPa, marking the highest CH4 recovery achieved in CBG separation thus far. The CH4 recovery was increased at low temperature while decreased at high pressure conditions. After a second-stage separation, the CH4 concentration in equilibrium gas decreased to 1.64 mol% from 30.16 mol%, signifying a remarkable 94.56 % recovery of CH4 from feed gas. The CH4 contents after a three-stage enrichment exceeded 87 mol%. This study furnishes valuable insights for CH4 recovery from CBG utilizing hydrate-based separation technology.
Keyword ：
Coal bed gas Coal bed gas Emulsion Emulsion Hydrate Hydrate Methane recovery Methane recovery Separation Separation
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| GB/T 7714 | Mu, Liang , Zhou, Ziqi , Zhao, Huixing et al. High-efficiency recovery of methane from coal bed gas via hydrate formation in emulsions [J]. | ENERGY , 2024 , 290 . |
| MLA | Mu, Liang et al. "High-efficiency recovery of methane from coal bed gas via hydrate formation in emulsions" . | ENERGY 290 (2024) . |
| APA | Mu, Liang , Zhou, Ziqi , Zhao, Huixing , Zhu, Xiaohai , Cui, Qingyan . High-efficiency recovery of methane from coal bed gas via hydrate formation in emulsions . | ENERGY , 2024 , 290 . |
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Natural gas hydrates (NGH) as a potential energy resource gain much attention, the depressurization-assisted CH 4 /CO 2 replacement is a combined method proposed recently for NGH mining. This work experimentally investigated the depressurization-assisted CH 4 /CO 2 replacement behavior in the muddy-silt slurries, and the effect of depressurization moment, amplitude and frequency was systematically examined. The results revealed that the depressurization after replacement significantly promoted reaction within a short period. The CH 4 replacement ratio was increased by delaying the depressurization moment and increasing the depressurization magnitude. The maximum CH 4 replacement ratio reached 61.28% at the depressurization moment of 48 h and 274.15 K. Additionally, the CH 4 replacement ratio was further increased in the secondary depressurization event compared to that at the primary depressurization. This research indicated that the depressurization was beneficial for CO 2 sequestration when the replacement pressure is higher than CO 2 hydrate equilibrium pressure. While it did not facilitate CO 2 sequestration when the replacement pressure is close to CO 2 hydrate equilibrium pressure. The free water consumption decreased with the increase of the depressurization moment, amplitude and frequency. These findings would contribute to the development of the depressurization-assisted CO 2 /CH 4 replacement in the future.
Keyword ：
CH4 production CH4 production CO2 replacement CO2 replacement Depressurization Depressurization Hydrate Hydrate Muddy silt Muddy silt
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| GB/T 7714 | Mu, Liang , Zhao, Huixing , Li, Xianlong et al. Experimental investigation on the depressurization-assisted CH4/CO2 replacement behavior in the muddy silt slurries [J]. | GAS SCIENCE AND ENGINEERING , 2024 , 126 . |
| MLA | Mu, Liang et al. "Experimental investigation on the depressurization-assisted CH4/CO2 replacement behavior in the muddy silt slurries" . | GAS SCIENCE AND ENGINEERING 126 (2024) . |
| APA | Mu, Liang , Zhao, Huixing , Li, Xianlong , Zeng, Jiguang , Cui, Qingyan . Experimental investigation on the depressurization-assisted CH4/CO2 replacement behavior in the muddy silt slurries . | GAS SCIENCE AND ENGINEERING , 2024 , 126 . |
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The existence of organic matters in naturally hydrate-bearing sediments would notably impact the CH4 extraction from reservoirs via CO2 swapping. In this work, the depressurization-assisted flue gas replacement was explored with artificial hydrate-bearing clay-silt sediments containing organic matter. The effect of organic matter type and content, depressurization moment and amplitude was systematically investigated. The results showed that the replacement was promoted at 5.0 wt% sulfonated lignin (SL) before depressurization, while it was inhibited at a lower SL content and this inhibition was weakened after depressurization. The CH4 replacement ratio and CO2 sequestration ratio increased as the fulvic acid (FA) content increased. For the organic matter-contained systems, the earlier depressurization moment was conducted, the higher CH4 recovery was obtained. The CH4 replacement ratio increased with the increase of depressurization amplitude, which reached 71.48 % in the 3.0 wt% FA system at the depressurization amplitude of 3.0 MPa. Aspen simulation revealed that the energy consumption was mainly caused by compression, there exist an optimum injection pressure of flue gas for the energy return on investment. The findings provide useful information for the depressurization-assisted flue gas replacement and would contribute to the actual NGH exploitation in the future.
Keyword ：
CH 4 hydrate CH 4 hydrate Clay-silt sediment Clay-silt sediment Depressurization-assisted Depressurization-assisted Flue gas replacement Flue gas replacement Organic matter Organic matter
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| GB/T 7714 | Mu, Liang , Zhao, Huixing , Zeng, Jiguang et al. Insight into the depressurization-assisted flue gas replacement behavior with the artificial hydrate-bearing clay-silt sediment containing organic matter [J]. | ENERGY , 2024 , 308 . |
| MLA | Mu, Liang et al. "Insight into the depressurization-assisted flue gas replacement behavior with the artificial hydrate-bearing clay-silt sediment containing organic matter" . | ENERGY 308 (2024) . |
| APA | Mu, Liang , Zhao, Huixing , Zeng, Jiguang , Zhu, Xiaohai , Lai, Jintao , Cui, Qingyan . Insight into the depressurization-assisted flue gas replacement behavior with the artificial hydrate-bearing clay-silt sediment containing organic matter . | ENERGY , 2024 , 308 . |
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Although some thermodynamic models for hydrate equilibrium conditions in the single porous media or in-hibitor solution have been reported, there are limited studies for those in the (porous media + inhibitor solution) complex systems. In this work, the CH4, CO2, C2H6, C3H8 and (CH4+C3H8) hydrate phase equilibrium data in the (porous media + NaCl or MeOH solution) systems was first examined by the thermodynamic consistency assessment. Then two thermodynamic models were proposed to predict their hydrate equilibrium conditions, which are established based on the Chen-Guo (C-G) model and Hu-Lee-Sum (HLS) correction. In the first model (Model 1), the changes of water molar volume and the effect of temperature on interfacial tension was considered. While the water activity was deemed to be independent of temperature in the second model (Model 2). The predictions agreed well with literature data, the overall AADP of 165 data sets for Model 1 and Model 2 was less than 6.01% and 4.56%, respectively, and the prediction accuracy was improved compared with other models. Results showed that Model 2 had good performance in both the (porous media + NaCl solution) systems and the (porous media + MeOH solution) systems. For the predictions of Model 1 in the (porous media + NaCl solution) systems, the average absolute deviation percent in pressure (AADP) increased as the increase of NaCl concentration, while no obvious variation trend was observed in the prediction of Model 2.
Keyword ：
Hydrate Hydrate Inhibitor solution Inhibitor solution Modeling Modeling Phase equilibrium Phase equilibrium Porous media Porous media
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| GB/T 7714 | Mu, Liang , Li, Xianlong , Tan, Qiqi et al. Thermodynamic modeling of gas hydrate phase equilibrium conditions in porous media in the presence of inhibitor solution [J]. | FLUID PHASE EQUILIBRIA , 2023 , 568 . |
| MLA | Mu, Liang et al. "Thermodynamic modeling of gas hydrate phase equilibrium conditions in porous media in the presence of inhibitor solution" . | FLUID PHASE EQUILIBRIA 568 (2023) . |
| APA | Mu, Liang , Li, Xianlong , Tan, Qiqi , Zhou, Ziqi , Zhao, Huixing , Cui, Qingyan . Thermodynamic modeling of gas hydrate phase equilibrium conditions in porous media in the presence of inhibitor solution . | FLUID PHASE EQUILIBRIA , 2023 , 568 . |
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Solidified natural gas (SNG) has been viewed as a promising method for the storage and transportation of natural gas, while a primary challenge for this technology remains how to effectively enhance the hydrate formation kinetics as well as its storage capacity. In this study, a natural soil organic matter fulvic acid (FA) was used as the hydrate promoter, and the effect of the FA concentration and experimental pressure and temperature on CH4 hydrate formation kinetics and gas uptake was systematically investigated. The findings revealed that the presence of FA significantly reduced the CH4 hydrate induction time and accelerated its gas uptake rate. The CH4 storage capacity in the 0.25 wt % FA solution reached 105.8 +/- 1.1 V/VH at 274.15 K and 5.5 MPa, which was much higher than that of pure water (19.8 +/- 0.9 V/VH) and increased by 18% compared to that of the 500 ppm sodium dodecyl sulfate (SDS) solution (89.8 +/- 0.7 V/VH) under the same conditions. A high initial pressure and low temperature were favorable to obtain a high gas uptake, and the CH4 storage capacity reached 158.5 +/- 0.6 V/VH (volume ratio of gas to hydrate, with the theoretical value being 172 V/V-H) in the 0.5 wt % FA solution at 274.15 K and 8.5 MPa. Morphological observations showed that the CH4 hydrate formed in the FA solutions was in a small-grained form, suggesting that FA presented the anti-agglomerant effect in the pure water system. No foam was generated during CH4 hydrate formation in the FA solutions. In comparison to the SDS system, much less foam was observed during the CH4 hydrate decomposition in the FA solutions, and the foam completely disappeared after hydrate decomposition.
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| GB/T 7714 | Mu, Liang , Zhao, Huixing , Zhou, Ziqi et al. Improving Methane Hydrate Formation Kinetics and Gas Storage Capacity with a Promoter [J]. | ENERGY & FUELS , 2023 , 37 (19) : 14778-14789 . |
| MLA | Mu, Liang et al. "Improving Methane Hydrate Formation Kinetics and Gas Storage Capacity with a Promoter" . | ENERGY & FUELS 37 . 19 (2023) : 14778-14789 . |
| APA | Mu, Liang , Zhao, Huixing , Zhou, Ziqi , Zeng, Jiguang , Cui, Qingyan . Improving Methane Hydrate Formation Kinetics and Gas Storage Capacity with a Promoter . | ENERGY & FUELS , 2023 , 37 (19) , 14778-14789 . |
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Natural gas (NG) storage in the form of clathrate hydrates gains much attention due to their non-explosive and eco-friendly characteristics. This study developed a novel method to store methane by forming hydrate in the high water cut (40-100 vol%) emulsions, in which an excellent anti-agglomerant (AA) cocamidopropyl dimethylamine (CDA) was employed in combination with sorbitan monododecanoate (Span 20). The CH4 storage achieved 151.1 v/vh (volume ratio of gas to hydrate, the theoretical value is 172 v/vh) in the 60 vol% systems within 60 min, which was significantly increased than the hydrate formation tests in the presence of single (Span 20, CDA) and combined additives (Span 20 coupled with tetrabutylammonium bromide (TBAB), fatty alcohol polyoxyethylene ether, N = 3 (AEO-3), L-tryptophan (L-Trp), sodium dodecyl sulfate (SDS), respectively). The effect of CDA concentration, initial pressure and stirring speed on hydrate formation was investigated. The fastest hydrate growth lasted 20 min for the test with 1000 rpm and the CH4 storage attained 151.9 v/vh. The maximum gas uptake achieved 166.2 v/vh within 2 h for the test with 8.2 MPa. No foams were observed in hydrate dissociation and the tests can be repeatable.
Keyword ：
Anti-agglomerant Anti-agglomerant Clathrate hydrate Clathrate hydrate Formation kinetics Formation kinetics High water cut emulsions High water cut emulsions Methane storage Methane storage
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| GB/T 7714 | Mu, Liang , Tan, Qiqi , Li, Xianlong et al. A novel method to store methane by forming hydrate in the high water-oil ratio emulsions [J]. | ENERGY , 2023 , 264 . |
| MLA | Mu, Liang et al. "A novel method to store methane by forming hydrate in the high water-oil ratio emulsions" . | ENERGY 264 (2023) . |
| APA | Mu, Liang , Tan, Qiqi , Li, Xianlong , Zhang, Qingyun , Cui, Qingyan . A novel method to store methane by forming hydrate in the high water-oil ratio emulsions . | ENERGY , 2023 , 264 . |
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