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煤气温度
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  gas temperature
    The process indexes such as blow in air time in the gasification production, blow in steam pressure and time, upper/lower stream coal gas temperature, CO 2 content in the coal gas and so on are analyzed and studied, in addition the management work gist of the process indexes is also described briefly.
    对造气生产中吹风时间、吹蒸气的压力和时间、上下行煤气温度、半水煤气中CO2 含量等项工艺指标进行了分析和研究 ,并简述了工艺指标管理工作的要领
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  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.
      
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  coal gas temperature
The effects of coal gasifying rate, pre-heating air temperature, and coal gas temperature on the performances of the power system are studied.
      


In view of the fact that the control system of coal-fired glass furnaces so far is still in less-advanced condition, some control designs of both combustion system and gas producing system are therefore presented in this paper. And the principle of automatic adjustment of gas temperature, blast air temperature and furnace temperature is described. In addition, the control process is also illustrated.

鉴于目前燃煤玻璃熔窑的生产控制处于落后状态,本文对熔窑的燃烧系统及煤气制备的自动控制提出了一些设计方案,介绍了煤气温度、鼓风温度和熔窑温度的自动调节原理,并图示了控制过程。

In this paper, a new infeasible path optimization method for complex modules is developed. It differs from the existing infeasible path optimization method in that it does not need the convergence of calculation for each round of iteration in complex modules. The problems of selecting the initial values of trial variables and scaling factors are also discussed and the algorithms for their selection are proposed separately. The new method has been successfully applied to the optimization of the flowrate of circulating...

In this paper, a new infeasible path optimization method for complex modules is developed. It differs from the existing infeasible path optimization method in that it does not need the convergence of calculation for each round of iteration in complex modules. The problems of selecting the initial values of trial variables and scaling factors are also discussed and the algorithms for their selection are proposed separately. The new method has been successfully applied to the optimization of the flowrate of circulating water for the CO shift section in ammonia synthesis.

本文将不可行路径法推广到复杂模块中,提出了一种新的不可行路径法,该法与现有不可行路径法的区别在于:在每轮优化迭代计算中,不要求复杂模块的模拟收敛.本文还对初值及标度因子的选取进行了讨论,提出了相应的选取原则.通过对合成氨变换工段循环热水系统以饱和塔出口半水煤气温度最大为目标函数进行优化计算,证明本文方法是成功的.

The process indexes such as blow in air time in the gasification production, blow in steam pressure and time, upper/lower stream coal gas temperature, CO 2 content in the coal gas and so on are analyzed and studied, in addition the management work gist of the process indexes is also described briefly.

对造气生产中吹风时间、吹蒸气的压力和时间、上下行煤气温度、半水煤气中CO2 含量等项工艺指标进行了分析和研究 ,并简述了工艺指标管理工作的要领

 
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