1) COREX smelter-gasifier
COREX熔融气化炉
1.
In this paper, a 2-D static model has been developed to evaluate the gas-solid flow transport phenomena in the COREX smelter-gasifier, application of Computational Fluid Dynamics (CFD) combined with the porous media and multi-phase models are employed.
本研究主要以COREX熔融气化炉反应器为对象,结合多孔介质模型和多相流模型,并考虑气固相间作用力,建立了描述其内部气固传输现象的二维数学模型,并采用计算流体动力学(CFD)方法进行了数值仿真研究。
2) melting gasifier
熔融气化炉
1.
Smelting process of melting gasifier is simulated.
模拟了熔融气化炉冶炼过程，通过解剖熔融气化炉得到试验结果，根据热力学原理分析了炉内［Si］的来源、反应机理和分配规律，以及影响含[Si］量的各种因
2.
The influence of melting velocity of en block DRI and melting rate of charging DRI on the COREX melting gasifier has been studied.
研究了预还原矿单体熔化速度和预还原矿熔化速率对ＣＯＲＥＸ熔融气化炉的影响，得出了限制预还原矿熔化的主要因素是炉内压差、碳－氧反应和铁水含硫量。
3) COREX smelting reduction
COREX熔融还原
4) gasification and melting
气化熔融
1.
By comparing with the domestic and foreign disposal methods of solid waste, it was pointed out that MSW gasification and melting combustion technology has the characteristics of little secondary pollution, completely harmless and higher resource degrees and so on.
本文阐述了国内外城市垃圾的处理现状，通过比较国内外常用的城市垃圾处理方法，指出城市垃圾气化熔融焚烧技术具有二次污染小，无害化彻底，资源化程度高等特点。
2.
More and more attention has been paid to Municipal refuse gasification and melting technology with dioxins zero-emissions and minimizing secondary pollution to environment.
介绍了国外四种比较成熟的城市垃圾气化熔融技术,但这些技术运行费用偏高,不适合我国高水分、低热值和未有效分类的垃圾特点,因而制约了在国内推广应用。
5) smelting gasifier
熔化气化炉
1.
The cold model of COREX smelting gasifier is developed according to the COREX3000.
依据 COREX3000原型建立了 COREX 熔化气化炉冷态模型。
2.
According to the different metallurgical functions,the smelting gasifier is divided into five zones:hearth, tuyere,packed bed,fluidized bed and free board.
按照不同的冶金功能把熔化气化炉划分为炉缸、风口、填充床、流化床和自由空间5个区域。
6) melter-gasifier
熔化气化炉
1.
Developing a cold-state model of COREX melter-gasifier in its symmetric half and using a high-speed video camera to track tracer particles,the information on the moving particles in and around the raceway near observing panel can be obtained.
通过建立COREX熔化气化炉的对称半体冷态模型,利用高速摄影的手段跟踪示踪颗粒,得到观察面板处风口回旋区域的颗粒运动信息。
2.
The coal consumption is calculated by using of heat balance for the melter-gasifier.
在对各反应器内化学反应和热交换作必要假设的基础上,分别对熔化气化炉、还原竖炉和热旋风除尘器等设备进行单元模化。
补充资料：[3-(aminosulfonyl)-4-chloro-N-(2.3-dihydro-2-methyl-1H-indol-1-yl)benzamide]
分子式：C16H16ClN3O3S
分子量：365.5
CAS号：26807-65-8
性质：暂无
制备方法：暂无
用途：用于轻、中度原发性高血压。
分子量：365.5
CAS号：26807-65-8
性质：暂无
制备方法：暂无
用途：用于轻、中度原发性高血压。
说明：补充资料仅用于学习参考，请勿用于其它任何用途。
参考词条