抽油机变速运行智能控制技术深化研究与应用

探究了抽油机合理的下冲程时间比,建立了多控制目标与自寻优相结合的抽油机井变速运行智能控制模型;应用功率峰值平衡度与功率均值平衡度,提出了判断抽油机井平衡度的新方法,解决了峰值电流法因反向发电而无法准确判断抽油机井平衡度的问题,实现了抽油机井平衡度的实时监测与调整;设计了前端控制与后台云端分析相结合的变速运行控制方案,弥补了抽油机变速运行智能控制技术井况适应区间狭窄,控制策略可变参数单一的局限性,拓展了井况适用范围,取得了良好的节电、增油效果。     

Prediction of the water content of biodiesel using ANN-MLP: An environmental application

Fuel quality, especially biodiesel, is highly dependent on its water content, and the major sources of water in the fuel relate to the transportation, production, and storage processes. In this present contribution, the multilayer perceptron artificial neural network (MLP-ANN) was applied to predict the water content of biodiesel and diesel blend in terms of temperature and composition. The proposed algorithm was trained and tested by utilizing 400 experimental data points which were extracted from the literature. Based on the results, the MLP-ANN model has great ability to estimate the water content of biodiesel and diesel blend. The R-squared (R²), root mean square error, average absolute relative deviation, and a?bsolute deviation parameters for the total data set are obtained, respectively, as 0.99784, 123919.1172, 3.3632, and 1.17%, which indicate the effective performance suggested by ANN. As the computational study is cheaper and easier than the experimental study, the developed software could be considered as an alternative for laboratory study, and the environmental effect of biodiesel and produced undesired product after biodiesel combustion which is directly related to the water content of biodiesel is estimable with the information released in this study.     

采动影响区抽采钻井井身固化及抽采效果考察

为提高地面瓦斯抽采效果,对抽采期间钻井进行了窥视,发现当回采工作面推过地面钻井位置后,钻井井壁迅速破坏,无法充分发挥其应有的瓦斯抽采效应。通过对煤层顶板岩层受采动影响顶板活动过程的分析,优化地面抽采钻井井身结构,在原有的施工工艺上增加三开下筛管,增强钻孔的防护强度,抽采浓度提高了1.54.5倍,抽采纯量提高了1.55倍,工作面回风流和回风隅角瓦斯浓度显著下降,抽采效果明显提高。     

Preparation of Al2O3-mullite thermal insulation materials with AlF3 and SiC as aids by microwave sintering

Al₂O₃-mullite composites were prepared under the synergy effect of AlF₃ and SiC aids by microwave heating. The phase composition, microstructure, porosity, flexural strength, thermal shock resistance, and thermal conductivity were investigated. The XRD results revealed that the content of mullite phase steadily increased with the increasing of AlF₃ content. The microstructure showed that the lower content (≤1 wt%) of AlF₃ led to the formation of granular mullite and the higher content (≥3 wt%) of AlF₃ led to the formation of mullite whiskers, which could form an interlocking structure. In addition, the SiC hot spots can also promote the generation of mullite whiskers by microwave sintering. The thermal shock resistance was significantly improved by the interlocking structure of mullite whiskers. The residual rate of flexural strength of the composite with 3 wt% AlF₃ was 86%. The composite with 3 wt% AlF₃ additives got its optimized thermal conductivity from 30°C to 950°C, the value was between 0.819 and 1.021 W/(mK), which possess excellent thermal insulation performance.     

Catalytic hydrogenation of CO2 from 600 MW supercritical coal power plant to produce methanol: A techno-economic analysis

Electricity and water from renewable hydropower plant are used as input for electrolysis unit to generate hydrogen, while CO₂ is captured from 600 MW supercritical coal power plant using post-combustion chemical solvent based technology. The captured CO₂ and H₂ generated through electrolysis are used to synthesize methanol through catalytic thermo-chemical reaction. The methanol synthesis plant is designed, modeled and simulated using commercial software Aspen Plus^®. The reactor is analyzed for two widely adopted kinetic models known as Graaf model and Vanden-Bossche (VB) model to predict the methanol yield and CO₂ conversion. The results show that the methanol reactor based on Graaf kinetic model produced 0.66 tonne of methanol per tonne of CO₂ utilized which is higher than that of the VB kinetic model where 0.6 tonne of methanol is produced per tonne of CO₂ utilized. The economic analysis reveals that 1.2 billion USD annually is required at the present cost of both H₂ production and CO₂ abatement to utilize continuous emission of 3.2 million tonne of CO₂ annually from 600 MW supercritical coal power unit to synthesize methanol. However, sensitivity analysis indicates that methanol production becomes feasible by adopting anyone of the route such as by increasing methanol production rate, by reducing levelised cost of hydrogen production, by reducing CO₂ mitigation cost or by increasing the current market selling price of methanol and oxygen.     

板框式压滤机在煤矿清挖水仓中的应用

煤矿每年雨季前都要清挖一次水仓淤泥,传统的人工清挖方式需要职工下到水仓底部,将底部沉淀物连同污水一并装入矿车,工作效率低,劳动强度大。利用板框式压滤机在矿井中直接将水仓污水中的煤泥压滤成饼状输送至地面,可节省人员,消除安全隐患,减少矿车运输,降低生产成本。     

Developing an innovative soft computing scheme for prediction of air overpressure resulting from mine blasting using GMDH optimized by GA

Engineering with Computers - Air overpressure (AOp) is one of the most important undesirable effects induced by blasting operations in the mining or tunneling projects. Hence, the present precise...     

Thermodynamic analysis of ethanol synthesis from hydration of ethylene coupled with a sequential reaction

Coal-based ethanol production by hydration of ethylene is limited by the low equilibrium ethylene conversion at elevated temperature. To improve ethylene conversion, coupling hydration of ethylene with a potential ethanol consumption reaction was analyzed thermodynamically. Five reactions have been attempted and compared: (1) dehydration of ethanol to ethyl ether ({\mathrm{2C}}_{\mathrm{2}}{\mathrm{H}}_{\mathrm{5}}\mathrm{OH}\iff{\mathrm{C}}_{\mathrm{2}}{\mathrm{H}}_{\mathrm{5}}{\mathrm{OC}}_{\mathrm{2}}{\mathrm{H}}_{\mathrm{5}}{\mathrm{+H}}_{\mathrm{2}}\mathrm{O}), (2) dehydrogenation of ethanol to acetaldehyde ({\mathrm{C}}_{\mathrm{2}}{\mathrm{H}}_{\mathrm{5}}\mathrm{OH}\iff {\mathrm{CH}}_{\mathrm{3}}{\mathrm{CHO+H}}_{\mathrm{2}}), (3) esterification of acetic acid with ethanol ({\mathrm{C}}_{\mathrm{2}}{\mathrm{H}}_{\mathrm{5}}{\mathrm{OH+CH}}_{\mathrm{3}}\mathrm{COOH}\iff {\mathrm{CH}}_{\mathrm{3}}{\mathrm{COOC}}_{\mathrm{2}}{\mathrm{H}}_{\mathrm{5}}{\mathrm{+H}}_{\mathrm{2}}\mathrm{O}), (4) dehydrogenation of ethanol to ethyl acetate ({\mathrm{2C}}_{\mathrm{2}}{\mathrm{H}}_{\mathrm{5}}\mathrm{OH}\iff {\mathrm{CH}}_{\mathrm{3}}{\mathrm{COOC}}_{\mathrm{2}}{\mathrm{H}}_{\mathrm{5}}{\mathrm{+2H}}_{\mathrm{2}}), and (5) oxidative dehydrogenation of ethanol to ethyl acetate ({\mathrm{2C}}_{\mathrm{2}}{\mathrm{H}}_{\mathrm{5}}{\mathrm{OH+O}}_{\mathrm{2}}\iff {\mathrm{CH}}_{\mathrm{3}}{\mathrm{COOC}}_{\mathrm{2}}{\mathrm{H}}_{\mathrm{5}}{\mathrm{+2H}}_{\mathrm{2}}\mathrm{O}). The equilibrium constants and equilibrium distributions of the coupled reactions were calculated and the effects of feed composition, temperature and pressure upon the ethylene equilibrium conversion were examined. The results show that dehydrogenation of ethanol to acetaldehyde has little effect on ethylene conversion, whereas for dehydrogenation of ethanol to acetaldehyde and ethyl acetate, ethylene conversion can be improved from 8% to 12.8% and 18.5%, respectively, under conditions of H₂O/C₂H₄ = 2, 10 atm and 300°C. The esterification of acetic acid with ethanol can greatly enhance the ethylene conversion to 22.5%; in particular, ethylene can be actually completely converted to ethyl acetate by coupling oxidative dehydrogenation of ethanol.     

缓冷出口温度对连续退火SPCC冷轧薄板屈服强度的影响

研究了缓冷出口温度对连续退火SPCC冷轧薄板组织和屈服强度的影响。结果表明:连续退火SPCC冷轧薄板的组织由等轴的铁素体晶粒和晶界处的块状渗碳体及晶粒内的颗粒状渗碳体组成。随着缓冷出口温度从680 ℃提高至700 ℃,平均晶粒尺寸从10.1 μm增加至12.5 μm;此外,提高缓冷出口温度还能够抑制晶界处块状渗碳体的形成,促进晶粒内细小渗碳体更加细小弥散的析出。当缓冷出口温度从680 ℃提高至700 ℃时,冷轧薄板的屈服强度约降低了28 MPa。