热解温度的英文

• pyrolysis temperature

• "热解"英文翻译    pyrolyzation; pyrolysis; pyr ...
• "温度"英文翻译    temperature
• "电解温度" 英文翻译 :    temperature of electrolysis
• "分解温度" 英文翻译 :    breakdown temperature; decomposition temperature
• "离解温度" 英文翻译 :    di ociation temperature; dissociation temperature
• "热离解温度" 英文翻译 :    deposition temperature
• "热退解温度" 英文翻译 :    thermal degradation temperature
• "融解温度" 英文翻译 :    thaw temperature
• "熔解温度" 英文翻译 :    fluxing temperature; fusion temperature; melting temperature; meltingouttemperature; meltingtemperature; temperature of fusion; tm
• "溶解温度" 英文翻译 :    digestion temperature; dissolving temperature; solution temperature; tm
• "标准分解温度" 英文翻译 :    standard decomposition temperature
• "初始分解温度" 英文翻译 :    temperature of initial decomposition
• "电解温度计法" 英文翻译 :    electrolytic hygrometer method
• "共增溶解温度" 英文翻译 :    cosolute temperature
• "绝热分解温度" 英文翻译 :    adiabatic decomposition temperature; adiabatic decompositon temperature
• "临界溶解温度" 英文翻译 :    critical dissolution temperature; critical olution temperature; critical solution temperature; criticalsolutiontemperature; cst
• "热力分解温度" 英文翻译 :    thermodynamic decomposition temperature
• "解链温度,熔解温度" 英文翻译 :    melting out temperature
• "积分过程分解温度" 英文翻译 :    integral procedure decomposition temperature
• "上临界溶解温度" 英文翻译 :    upper criticalsolution temperatures
• "下限临界溶解温度" 英文翻译 :    lower critical solution temperature
• "自加速分解温度" 英文翻译 :    self-accelerating decomposition temperature （sadt）; self-acceleratingdecompositiontemperature（sadt）
• "最后一颗结晶溶解温度" 英文翻译 :    lctd temperature
• "热解" 英文翻译 :    pyrolyzation; pyrolysis; pyrogenic decomposition; themolysis
• "煤热解" 英文翻译 :    coalite pyrolysis; pyrolysis of coal

• It is shown that the pyrolysis temperature has a great effect on the yield and the properties of the bio - oi1
  实验结果表明，热解温度对生物油的产率和性质影响很大，生物油及沥青烯的产率在600 ~ 700达到最大值。
• With the increasing pyrolysis temperature , the specific surface area as well as micropore surface area and total volume increased accompanied with the narrower pore size distribution
  随热解温度的升高，气凝胶的比表面积、微孔表面积相应增加，孔径分布变窄，孔尺寸缩小，总孔容增大。
• The oil was studied in detail from different aspects , the results of which showed the effect of pyrolytic temperature on the properties of the oil and the characteristics of the pyrolysis reaction in the rotary kiln reactor
  通过不同角度全面考察热解油品质，从而反映出热解温度对热解油品质的影响和回转窑反应器内热解反应的特点。
• Then , analytical work was carried out as follows : the ultimate analysis and physi - chemical analysis of the pyrolytic oil comprised a sketch of the fuel properties of the oil ; then , through the distillation analysis of the oil , the fraction composition of the " unrefined " oil was known . after that , a general knowledge of the aromaticity and saturation of the hydrocarbons in the oil was provided by the outcome of the ft - ir functional group analysis . also , from the analysis , the form of the polar functional groups and their distribution in different fractions of the oil were learned
  文中首先对不同热解温度下热解油产率进行分析讨论，然后，针对热解油品质进行了一系列分析：通过元素组成和理化特性的分析，对热解油作为燃料特性有了一个大致了解；通过实沸点蒸馏分析，得到热解油作为一种未提炼油的馏分分布，并为后续热解油馏分的细入分析提供了前提；通过对热解全油和各窄馏分的ft - ir官能团分析，对热解油的芳香性、不饱和性有了整体的了解，并且清楚了热解油中的极性官能团存在型式及其在热解油不同馏分中的分布。
• B ) the concept of ratio of conversion ; c ) effect of temperature and residence time on tar conversion ratio ; increasing the temperature and residence time is beneficial to tar cracking , and the effect is not evidence when t > 900c and > 1 . 0s d ) effect of cracking temperature on the tar conversion ratio with sic ; e ) effect of different catalyst on the tar conversion ratio ; some catalyst was test in the experimental system and dolomite is a most promising one
  研究了生物质焦油含量随热解温度和生物质原料的变化趋势，提出了生物质焦油裂解率的概念、探讨了不同条件(热解温度、停留时间)下热裂解的效果和不同催化剂，不同反应条件下对焦油催化裂解效果的影响，催化剂在使用过程中由于积碳、中毒等原因会使得活性丧失，本文针对催化剂活性的丧失以及再生进行丁试验研究和理论分析。
• This text completely and systematically studies the status and the development of the pyrolysis and the fluidization of biomass , which distill the bio - oil in the domestic and international area , as well as the existing problems . this thesis primarily include following aspects : ( l ) , by experimenting and measuring the energy ( heat value ) and the content of c , h , n chemical element of right 20 kinds of common biomass , on the base of the experimental result , and respectively established the biomass energy predict experiment formula with the element of h and c is from change , and passed the ro . os examination , which provides the basis and convenience for flash pyrolysis fluidization device energy to convert the rate to compute with biomass energy utilization calculation ; ( 2 ) , proceeded the tg and dtg experimentation equal velocity ( 10 ? / min , 20 ? / min , 40 ? / min , 60 ? / min ) heating and constant temperature heating by studying on eight kinds of biomass samples , according to the experimental data and arrhenius formula , we established the dynamics model of pyrolysis of , then , using the goast - redfern and p function , we also solved the dynamics parameters and analyze out every kind of biomass ' s frequency factor and parameters of activation energy , and established the every kind of dynamics model of pyrolysis of biomass , all of these provide the theories and basis to make sure the reactor ' s flash pyrolysis work temperature scope design and the describing of pyrolysis reactor dynamics ; ( 3 ) , in order to study and ascertain the process of heat completely getting to pyrolysis time of varied size biomass particles , we observed and measured the ratio of length and diameter ( l / d ) with the varied biomass through electron microscope , we concluded the l / d ratios usually is from 5 . 0 to 6 . 0 , the average is 5 . 3 ; ( 4 ) , we studied the process of biomass transiting and the theory of complete pyrolysis time with the theory of complicated heat field , we got the time ( t ) of the varied size biomass particles arriving to complete pyrolysis , and we knew that the complete pyrolysis time and the time which get to the biggest production ratio are identical , all of these studies provide the theory base for design and forecasting the flash pyrolysis reactor solid state resort time ; ( 5 ) , according to the above experiment result , synthesize to make use of the engineering the mechanics , engineering the material , machine the design to learn the principle , deduce , establish the theory of rotation cone flash pyrolysis reactor material resort time ( t ) and reasonable rotation velocity ( or frequency ) relation theory ; and ( 6 ) , we gave the reactor ' s smallest cone angle certain , reactor cone wall strength design theory , the reactor production ability theory , the power design method and the critical rotation velocity theory
  本文较全面、系统地综述了国内外生物质热解液化制取生物燃油技术研究发展现状及存在的问题，主要研究内容有： ( 1 )实验、测定了20种常见生物质的能量(发热量)和c 、 h 、 n元素含量，根据实验结果分别建立了以h和c为自变量的生物质能量预测经验公式，并通过r _ ( 0 . 05 )检验；为闪速热解液化装置能量转化率计算和生物质能量利用率计算提供了依据和方便； ( 2 )选择了8种生物质试样作了等加热速率( 10 min 、 20 min 、 40 min 、 60 min )和恒温加热的tg和dtg实验，根据实验数据和阿伦尼乌斯公式建立了生物质热解反应动力学微分方程，并采用goast - redfem积分法和p函数对其动力学参数进行了求解，解析出各种生物质的频率因子和活化能参数，进而建立了各种生物质的热解动力学模型，为科学确定反应器的闪速热解工作温度范围及热解反应动力学描述，提供了理论和依据； ( 3 )为研究和确定不同尺度的生物质颗粒中心达到全热解的时间，在体视显微镜下对不同粒度的生物质颗粒的长径比进行了实验观察和测定，得出生物质的长径比( l d )一般在5 . 0 6 . 0之间，平均为5 . 3的结果； ( 4 )采用复杂温度场传热学理论对生物质传热过程及充分热解时间理论进行了研究，解析推导出了不同尺寸生物质颗粒中心温度达到充分热解温度的时间( t ) ，得出了理论推导的充分热解时间与最大产油率的热解时间相一致的结果，为闪速热解反应器固相滞留时间设计和预测提供了理论依据； ( 5 )根据上述实验结果，综合运用工程力学、工程材料、机械设计学原理，推导、建立了转锥式闪速热解反应器物料滞留时间( )与转速(或频率)合理匹配理论； ( 6 )提出了转锥式闪速热解反应器的最小锥角设计、锥壁强度设计、生产能力设计理论和功率计算方法及临界转速理论等。
• The law on component change of carbocoal from different temperature pyrolysis of yanzhou bituminous coal in ordinary pressure fluidized bed in nitrogen atmosphere is analyzed , especial change law of sulfur , and activation energy of pyrolysis carbocoal in different temperature is analyzed in thermogravimetric analyzer , it is found that activation decreases with pyrolysis temperature increasing
  摘要利用兖州烟煤在不同温度下常压流化床氮气气氛的热解半焦作为样品，分析了半焦成分变化的规律，特别是硫的变化规律，并利用热重分析仪分析了不同温度下热解半焦的活化能，研究表明随着热解温度的升高，活化能逐渐降低。