The combustion characteristics of biomass, anthracite coal and their blends were investigated using thermogravimetry, and the kinetic parameters and combustion reaction mechanisms were tested by combining the iso-conv...The combustion characteristics of biomass, anthracite coal and their blends were investigated using thermogravimetry, and the kinetic parameters and combustion reaction mechanisms were tested by combining the iso-conversional method and Avrami method in order to find out the kinetics characteristics responsible for the combustion of samples. In biomass combustion, two peaks were observed at 332.3 and 472.3℃, but the reactive rate curve of coal showed one peak with maximum mass loss rate at 552.8℃. The ignition temperature and burnout temperature of blends decreased, and the ignition index and combustibility index increased with the increase in biomass content. Calculation of kinetic parameters showed that the values of activation energy of blends increased with increasing biomass content from 150.77 to 215.93 kJ/mol. The reaction orders of blends lay in the range of 0.44 and 0.78.展开更多
The iso-conversion method to could calculate the kinetics parameters effectively, the present paper built an evaluation equation for iso-conversion methods according to the thermo kinetics integral equation and analys...The iso-conversion method to could calculate the kinetics parameters effectively, the present paper built an evaluation equation for iso-conversion methods according to the thermo kinetics integral equation and analyses the temperatures of the same degree of conversion for different heating rates by ideal TG （thermo-gravity） curve data. It is obtained that the temperatures of the same degree of conversion for different heating rates＇ TG curve have good linearity connection validating the correction of the evaluation equation for iso-conversion methods and the scope of linear slope for theratio between heating rates being 2 is 1.05 to 1.09.展开更多
The crystallization kinetics of Se80In10Pb10 chalcogenide glass is studied using differential scanning calorimeter (DSC) at different heating rates (5, 10, 15 and 20 K/min) under non-isothermal conditions. Four iso-co...The crystallization kinetics of Se80In10Pb10 chalcogenide glass is studied using differential scanning calorimeter (DSC) at different heating rates (5, 10, 15 and 20 K/min) under non-isothermal conditions. Four iso-conversional methods (Kissinger-Akahira-Sunose, Flynn-Wall-Ozawa, Tang and Straink) were used to determine various kinetic parameters: crystallization temperature (Tα), activation energy of crystallization (Eα), Avrami exponent (nα) in non-isothermal mode. The transformation from amorphous to crystalline phase in Se80In10Pb10 is considered as a single step reaction mechanism.展开更多
Alloys of Se80-xTe20Inx glassy system are obtained by quenching technique and crystallization kinetics has been studied using Differential Scanning Calorimetric [DSC] technique. Well defined endothermic and exothermic...Alloys of Se80-xTe20Inx glassy system are obtained by quenching technique and crystallization kinetics has been studied using Differential Scanning Calorimetric [DSC] technique. Well defined endothermic and exothermic peaks are ob- served at glass transition temperature (Tg) and crystallization temperature (Tc). From DSC scans, Tc is obtained at dif- ferent heating rates (5, 10, 15, 20, 25 K/min). It is observed that Tc increases with increasing heating rate for a particular glassy alloy. Activation energy of crystallization (Ec) has been calculated by different Non-isothermal Iso-conversional methods, i.e., Kissinger-Akahira-Sunose [KAS], Friedman, Flynn-wall-Ozawa [FWO], Friedman-Ozawa [FO] and Sta-rink methods. It is observed that Ec is dependent on extent of crystallization (α). Activation energy is also found to vary with atomic percentage of In in ternary Se80-xTe20Inx glassy system. The compositional dependence of Ec shows a re-versal in the trend at x = 15 in Se80-xTe20Inx, which is explained in terms of mechanically stabilized structure at this composition.展开更多
为获得可靠的煤焦-CO_2气化反应动力学参数,采用Flunm-Wall-Ozawa(FWO)等转化率法进行煤焦-CO_2气化动力学研究。在3个不同升温速率下进行了煤焦-CO_2气化热重试验,计算不同碳转化率下的反应活化能,用主曲线法分析了气化机理模型,并采...为获得可靠的煤焦-CO_2气化反应动力学参数,采用Flunm-Wall-Ozawa(FWO)等转化率法进行煤焦-CO_2气化动力学研究。在3个不同升温速率下进行了煤焦-CO_2气化热重试验,计算不同碳转化率下的反应活化能,用主曲线法分析了气化机理模型,并采用拟合法对等转化率法的结果进行验证。结果表明,气化主反应区不同碳转化率下(α为0.2~0.8)活化能的变化较小,为(228.25±5.22)k J/mol。煤焦-CO_2气化反应为均相模型,该模型标准曲线与试验曲线重合度较好,并符合目前常用的煤气化动力学模型。拟合法计算的活化能仅与等转化率法相差0.74 k J/mol,说明等转化率法研究煤焦-CO_2动力学可行。展开更多
In order to effectively recycle resource for the benefit of the global environment, the utilization of waste plastics as auxiliary injectant for blast furnaces is becoming increasingly important. Combustion kinetics o...In order to effectively recycle resource for the benefit of the global environment, the utilization of waste plastics as auxiliary injectant for blast furnaces is becoming increasingly important. Combustion kinetics of plastics-coal blends with 0, 10%, 20% and 40% waste plastics (WP) are investigated separately by thermogravimetric analysis (TGA) from ambient temperature to 900 ℃ in air atmosphere. These blends are combusted at the heating rates of 5, 10 and 20 ℃/min. The results indicate that, with the increase of waste plastics content, the combustion processes of blends could be divided into one stage, two stages and three stages. The waste plastics content and heating rates have important effects on the main combustion processes of blends. With the increase of waste plastics content, the ignition temperature and the final combustion temperature of blends tend to decrease, while the combustion reaction becomes fiercer. With the increase of the heating rate, the ignition temperature, the mass loss rate of the peaks and the final combustion temperature of blends combustion tend to increase. The Flynn-Wall-Ozawa (FWO) iso-conversional method is used for the kinetic analysis of the main combustion process. The results indicate that, when the waste plastics content varied from 0 to 40%, the values of activation energy increase from 126.05 to 184.12 kJ /mol.展开更多
The investigation of silicothermic reduction of CaO·MgO was carried out using a self-developed thermogravimetric analysis(TGA)instrument under vacuum and high temperature conditions.The TG data of pellets prepare...The investigation of silicothermic reduction of CaO·MgO was carried out using a self-developed thermogravimetric analysis(TGA)instrument under vacuum and high temperature conditions.The TG data of pellets prepared with calcined dolomite,ferrosilicon and fluorite were determined at the heating rates of 1.5,2.0,2.5 and 3.0℃/min in 5 Pa vacuum at 300−1400℃,respectively.Model-free analysis and model-based analysis were applied for simulating the kinetic mechanism.By analyzing the characteristics of the initial and final reaction temperatures of TG curve,ratio of half-width of derivative TG curve and kinetic parameters,a conclusion was made that the most probable mechanism function is the first order formal chemical reaction with activation energy of 233.42 kJ/mol and pre-exponential factor of 5.14×1010 s−1.This study provides the basic data of dynamics of silicothermic magnesium production under vacuum conditions.展开更多
Fiber-reinforced phenolic composite has become an ideal material for solid rocket motor’s(SRM)nozzle,because of its excellent high temperature resistance and ablation resistance.The physical and chemical properties o...Fiber-reinforced phenolic composite has become an ideal material for solid rocket motor’s(SRM)nozzle,because of its excellent high temperature resistance and ablation resistance.The physical and chemical properties of reinforcing fiber would significantly affect the cure reaction of phenolic(PF)resin,which results in the obvious difference between the cure characteristics of the fiberreinforced phenolic system and neat resin.To clarify the difference in cure reaction between fiber-reinforced phenolic system and PF resin,meanwhile,to obtain the kinetics of high silica glass fiber/phenolic(GF-HSi/PF)prepreg and carbon fiber/phenolic(CF/PF)prepreg,the dynamic experiments of PF resin,GF-HSi/PF prepreg and CF/PF prepreg are carried out by differential scanning calorimetry(DSC).Iso-conversional kinetics is proposed,and the activation energy is determined as a function of cure degree.The reaction model f(α)is obtained by introducing the kinetics compensation effect,founding that the f(α)of PF resin is influenced significantly by reinforcing fiber.The kinetics of three materials are determined by the model-fitting method,founding that the kinetic models of PF resin,GF-HSi/PF prepreg and CF/PF prepreg are a one-step autocatalytic model,two-step model from autocatalytic reaction to N-order reaction and three-step model from autocatalytic reaction to N-order reaction respectively.展开更多
文摘The combustion characteristics of biomass, anthracite coal and their blends were investigated using thermogravimetry, and the kinetic parameters and combustion reaction mechanisms were tested by combining the iso-conversional method and Avrami method in order to find out the kinetics characteristics responsible for the combustion of samples. In biomass combustion, two peaks were observed at 332.3 and 472.3℃, but the reactive rate curve of coal showed one peak with maximum mass loss rate at 552.8℃. The ignition temperature and burnout temperature of blends decreased, and the ignition index and combustibility index increased with the increase in biomass content. Calculation of kinetic parameters showed that the values of activation energy of blends increased with increasing biomass content from 150.77 to 215.93 kJ/mol. The reaction orders of blends lay in the range of 0.44 and 0.78.
文摘The iso-conversion method to could calculate the kinetics parameters effectively, the present paper built an evaluation equation for iso-conversion methods according to the thermo kinetics integral equation and analyses the temperatures of the same degree of conversion for different heating rates by ideal TG （thermo-gravity） curve data. It is obtained that the temperatures of the same degree of conversion for different heating rates＇ TG curve have good linearity connection validating the correction of the evaluation equation for iso-conversion methods and the scope of linear slope for theratio between heating rates being 2 is 1.05 to 1.09.
文摘The crystallization kinetics of Se80In10Pb10 chalcogenide glass is studied using differential scanning calorimeter (DSC) at different heating rates (5, 10, 15 and 20 K/min) under non-isothermal conditions. Four iso-conversional methods (Kissinger-Akahira-Sunose, Flynn-Wall-Ozawa, Tang and Straink) were used to determine various kinetic parameters: crystallization temperature (Tα), activation energy of crystallization (Eα), Avrami exponent (nα) in non-isothermal mode. The transformation from amorphous to crystalline phase in Se80In10Pb10 is considered as a single step reaction mechanism.
文摘Alloys of Se80-xTe20Inx glassy system are obtained by quenching technique and crystallization kinetics has been studied using Differential Scanning Calorimetric [DSC] technique. Well defined endothermic and exothermic peaks are ob- served at glass transition temperature (Tg) and crystallization temperature (Tc). From DSC scans, Tc is obtained at dif- ferent heating rates (5, 10, 15, 20, 25 K/min). It is observed that Tc increases with increasing heating rate for a particular glassy alloy. Activation energy of crystallization (Ec) has been calculated by different Non-isothermal Iso-conversional methods, i.e., Kissinger-Akahira-Sunose [KAS], Friedman, Flynn-wall-Ozawa [FWO], Friedman-Ozawa [FO] and Sta-rink methods. It is observed that Ec is dependent on extent of crystallization (α). Activation energy is also found to vary with atomic percentage of In in ternary Se80-xTe20Inx glassy system. The compositional dependence of Ec shows a re-versal in the trend at x = 15 in Se80-xTe20Inx, which is explained in terms of mechanically stabilized structure at this composition.
文摘为获得可靠的煤焦-CO_2气化反应动力学参数,采用Flunm-Wall-Ozawa(FWO)等转化率法进行煤焦-CO_2气化动力学研究。在3个不同升温速率下进行了煤焦-CO_2气化热重试验,计算不同碳转化率下的反应活化能,用主曲线法分析了气化机理模型,并采用拟合法对等转化率法的结果进行验证。结果表明,气化主反应区不同碳转化率下(α为0.2~0.8)活化能的变化较小,为(228.25±5.22)k J/mol。煤焦-CO_2气化反应为均相模型,该模型标准曲线与试验曲线重合度较好,并符合目前常用的煤气化动力学模型。拟合法计算的活化能仅与等转化率法相差0.74 k J/mol,说明等转化率法研究煤焦-CO_2动力学可行。
基金Item Sponsored by National Key Technology Research and Development Program in 11th Five-Year Plan of China (2008BAB32B05)
文摘In order to effectively recycle resource for the benefit of the global environment, the utilization of waste plastics as auxiliary injectant for blast furnaces is becoming increasingly important. Combustion kinetics of plastics-coal blends with 0, 10%, 20% and 40% waste plastics (WP) are investigated separately by thermogravimetric analysis (TGA) from ambient temperature to 900 ℃ in air atmosphere. These blends are combusted at the heating rates of 5, 10 and 20 ℃/min. The results indicate that, with the increase of waste plastics content, the combustion processes of blends could be divided into one stage, two stages and three stages. The waste plastics content and heating rates have important effects on the main combustion processes of blends. With the increase of waste plastics content, the ignition temperature and the final combustion temperature of blends tend to decrease, while the combustion reaction becomes fiercer. With the increase of the heating rate, the ignition temperature, the mass loss rate of the peaks and the final combustion temperature of blends combustion tend to increase. The Flynn-Wall-Ozawa (FWO) iso-conversional method is used for the kinetic analysis of the main combustion process. The results indicate that, when the waste plastics content varied from 0 to 40%, the values of activation energy increase from 126.05 to 184.12 kJ /mol.
基金Project(2016YFB0301100)supported by the National Key R&D Program of ChinaProject(51804277)supported by the National Natural Science Foundation of ChinaProject(2018ZE007)supported by the Rare and Precious Metal Materials Genome Engineering Project of Yunnan Province,China。
文摘The investigation of silicothermic reduction of CaO·MgO was carried out using a self-developed thermogravimetric analysis(TGA)instrument under vacuum and high temperature conditions.The TG data of pellets prepared with calcined dolomite,ferrosilicon and fluorite were determined at the heating rates of 1.5,2.0,2.5 and 3.0℃/min in 5 Pa vacuum at 300−1400℃,respectively.Model-free analysis and model-based analysis were applied for simulating the kinetic mechanism.By analyzing the characteristics of the initial and final reaction temperatures of TG curve,ratio of half-width of derivative TG curve and kinetic parameters,a conclusion was made that the most probable mechanism function is the first order formal chemical reaction with activation energy of 233.42 kJ/mol and pre-exponential factor of 5.14×1010 s−1.This study provides the basic data of dynamics of silicothermic magnesium production under vacuum conditions.
基金This work was supported by the National Natural Science Foundation of China(Grant No.U1837601).
文摘Fiber-reinforced phenolic composite has become an ideal material for solid rocket motor’s(SRM)nozzle,because of its excellent high temperature resistance and ablation resistance.The physical and chemical properties of reinforcing fiber would significantly affect the cure reaction of phenolic(PF)resin,which results in the obvious difference between the cure characteristics of the fiberreinforced phenolic system and neat resin.To clarify the difference in cure reaction between fiber-reinforced phenolic system and PF resin,meanwhile,to obtain the kinetics of high silica glass fiber/phenolic(GF-HSi/PF)prepreg and carbon fiber/phenolic(CF/PF)prepreg,the dynamic experiments of PF resin,GF-HSi/PF prepreg and CF/PF prepreg are carried out by differential scanning calorimetry(DSC).Iso-conversional kinetics is proposed,and the activation energy is determined as a function of cure degree.The reaction model f(α)is obtained by introducing the kinetics compensation effect,founding that the f(α)of PF resin is influenced significantly by reinforcing fiber.The kinetics of three materials are determined by the model-fitting method,founding that the kinetic models of PF resin,GF-HSi/PF prepreg and CF/PF prepreg are a one-step autocatalytic model,two-step model from autocatalytic reaction to N-order reaction and three-step model from autocatalytic reaction to N-order reaction respectively.
