助手标题  
全文文献 工具书 数字 学术定义 翻译助手 学术趋势 更多
查询帮助
意见反馈
   煤气温度 在 燃料化工 分类中 的翻译结果: 查询用时:0.11秒
图标索引 在分类学科中查询
所有学科
燃料化工
冶金工业
自动化技术
电力工业
无机化工
有机化工
工业通用技术及设备
动力工程
更多类别查询

图标索引 历史查询
 

煤气温度    
相关语句
  gas temperature
    Discussion on Gas Temperature at the Final Cooling Stage
    终冷段煤气温度的探讨
短句来源
    Effect of Wet Gas Temperature on Production and the Control
    湿煤气温度对生产的影响及其控制
短句来源
    The temperature of desulfurization solution is 35℃~45℃ and gas temperature is 25℃~35℃.
    控制脱硫液温度35℃ ̄40℃,煤气温度25℃ ̄35℃,保证系统正常运行;
短句来源
    Research on raw coal gas temperature to judge final coking time
    用粗煤气温度判断结焦终了时间的研究
短句来源
    Reasons and harm of higher gas temperature at the final cooling stage are analyzed and solutions are proposed.
    分析了终冷段煤气温度偏高的危害及原因,并提出了处理办法。
短句来源
  gas temperature
    Discussion on Gas Temperature at the Final Cooling Stage
    终冷段煤气温度的探讨
短句来源
    Effect of Wet Gas Temperature on Production and the Control
    湿煤气温度对生产的影响及其控制
短句来源
    The temperature of desulfurization solution is 35℃~45℃ and gas temperature is 25℃~35℃.
    控制脱硫液温度35℃ ̄40℃,煤气温度25℃ ̄35℃,保证系统正常运行;
短句来源
    Research on raw coal gas temperature to judge final coking time
    用粗煤气温度判断结焦终了时间的研究
短句来源
    Reasons and harm of higher gas temperature at the final cooling stage are analyzed and solutions are proposed.
    分析了终冷段煤气温度偏高的危害及原因,并提出了处理办法。
短句来源
  gas temperature
    Discussion on Gas Temperature at the Final Cooling Stage
    终冷段煤气温度的探讨
短句来源
    Effect of Wet Gas Temperature on Production and the Control
    湿煤气温度对生产的影响及其控制
短句来源
    The temperature of desulfurization solution is 35℃~45℃ and gas temperature is 25℃~35℃.
    控制脱硫液温度35℃ ̄40℃,煤气温度25℃ ̄35℃,保证系统正常运行;
短句来源
    Research on raw coal gas temperature to judge final coking time
    用粗煤气温度判断结焦终了时间的研究
短句来源
    Reasons and harm of higher gas temperature at the final cooling stage are analyzed and solutions are proposed.
    分析了终冷段煤气温度偏高的危害及原因,并提出了处理办法。
短句来源
查询“煤气温度”译词为用户自定义的双语例句

    我想查看译文中含有:的双语例句
例句
为了更好的帮助您理解掌握查询词或其译词在地道英语中的实际用法,我们为您准备了出自英文原文的大量英语例句,供您参考。
  gas temperature
At exhaust gas temperature range of 350-500°C, the maximum NOx conversion reached about 90%.
      
The temperature of the wall surface is assumed to be constant and equal to the gas temperature at a large distance from the droplet.
      
The motion of a hypersonic body is accompanied by an increase in the gas temperature in the boundary layer up to tens of thousands of degrees, which causes the gas to ionize.
      
An equation is derived for the gas temperature and velocity probability distributions.
      
The process is considered for low intensities of the incident wave, behind which the gas temperature hardly differs from the initial wall temperature.
      
更多          
  gas temperature
At exhaust gas temperature range of 350-500°C, the maximum NOx conversion reached about 90%.
      
The temperature of the wall surface is assumed to be constant and equal to the gas temperature at a large distance from the droplet.
      
The motion of a hypersonic body is accompanied by an increase in the gas temperature in the boundary layer up to tens of thousands of degrees, which causes the gas to ionize.
      
An equation is derived for the gas temperature and velocity probability distributions.
      
The process is considered for low intensities of the incident wave, behind which the gas temperature hardly differs from the initial wall temperature.
      
更多          
  gas temperature
At exhaust gas temperature range of 350-500°C, the maximum NOx conversion reached about 90%.
      
The temperature of the wall surface is assumed to be constant and equal to the gas temperature at a large distance from the droplet.
      
The motion of a hypersonic body is accompanied by an increase in the gas temperature in the boundary layer up to tens of thousands of degrees, which causes the gas to ionize.
      
An equation is derived for the gas temperature and velocity probability distributions.
      
The process is considered for low intensities of the incident wave, behind which the gas temperature hardly differs from the initial wall temperature.
      
更多          
  temperature of gas
The solution of a set of equations of motion and energy balance (with specific energy input of up to 3 J/cm3) for a weakly compressible gas is used to obtain the profiles of components of velocities and temperature of gas flow.
      
Measurement of the temperature of gas media containing carbon dioxide by the laser-probing method
      
The effect of the temperature of gas phase CO upon the kinetics of the oxygen titration reaction: COg +Oa → CO2,g, has been studied.
      
Measurement of the temperature of gas between the busbars of a flat magnetocumulative generator
      
Measurement of the atomic temperature of gas discharges through the absorption of ultra-soft x rays
      
更多          


Two new parameters—TG, PK are proposed and researched in this paper. TG is the critical temperature of the gas leaving the active coke zone. PK is the difference between the theoretic output of pig iron and the amount of pig iron carried in furnace by the charged burden in a period of time. The off-line testing with actual operating data leads to following conceptions: (1)There is a negative linear relationship in some extent between TG and the thermal status of BF; (2)The more PK, the more possibility of burden...

Two new parameters—TG, PK are proposed and researched in this paper. TG is the critical temperature of the gas leaving the active coke zone. PK is the difference between the theoretic output of pig iron and the amount of pig iron carried in furnace by the charged burden in a period of time. The off-line testing with actual operating data leads to following conceptions: (1)There is a negative linear relationship in some extent between TG and the thermal status of BF; (2)The more PK, the more possibility of burden slipping and collapsing.

本文提出并研究了两个与炉的热交换和气体力学过程有关的新信息参数—TG、PK.TG为离开滴下带的临界煤气温度,它与高炉热状态有关并影响着高炉内煤气的压差;PK为一段期间内高炉理论产铁量与炉料带人铁量之差,它影响着高炉顺行,用它可以表征炉内剩余空间大小。本文利用高炉的实际生产运行参数数据,在计算机上对参数TG、PK实用性进行了离线试验分析,结果表明:参数TG与高炉热状态呈一定程度的负相关;参数PK越大,高炉发生崩料的可能性越大。

The heating control systems of coke oven at home and abroad are briefly introduced. The heating control system of coke oven for the 3rd phase of Baosteel is presented and its functions include oven temperature feedback control through regulating gas flowrate, air ratio control by use of smoke flue attraction force regulation system with correction for oxygen content in waste gas and determination of “fire drop”time according to temperature change of crude gas through the rise tube to avoid unripe coke or heating...

The heating control systems of coke oven at home and abroad are briefly introduced. The heating control system of coke oven for the 3rd phase of Baosteel is presented and its functions include oven temperature feedback control through regulating gas flowrate, air ratio control by use of smoke flue attraction force regulation system with correction for oxygen content in waste gas and determination of “fire drop”time according to temperature change of crude gas through the rise tube to avoid unripe coke or heating time too long. The special measuring instruments used in the system are described. At last, the mentioned system is evaluated.

宝钢三期焦炉加热控制系统通过控制加热煤气量实现炉温的反馈调节,通过烟气中含氧量校正的烟道吸力调节系统控制空气配比, 根据上升管荒煤气温度的变化进行火落时间的判定以免推出生焦或加热时间过长。作者介绍了该加热控制系统和系统中应用的特殊检测仪表,简单介绍了国内外焦炉加热控制系统并对本系统进行了评价。

Reasons and harm of higher gas temperature at the final cooling stage are analyzed and solutions are proposed.

分析了终冷段煤气温度偏高的危害及原因,并提出了处理办法。

 
<< 更多相关文摘    
图标索引 相关查询

 


 
CNKI小工具
在英文学术搜索中查有关煤气温度的内容
在知识搜索中查有关煤气温度的内容
在数字搜索中查有关煤气温度的内容
在概念知识元中查有关煤气温度的内容
在学术趋势中查有关煤气温度的内容
 
 

CNKI主页设CNKI翻译助手为主页 | 收藏CNKI翻译助手 | 广告服务 | 英文学术搜索
版权图标  2008 CNKI-中国知网
京ICP证040431号 互联网出版许可证 新出网证(京)字008号
北京市公安局海淀分局 备案号:110 1081725
版权图标 2008中国知网(cnki) 中国学术期刊(光盘版)电子杂志社