1) coking chamber heat transfer model
炭化室传热模型
2) heat transfer model
传热模型
1.
Study on the heat transfer model ofheat transfer process for continuous cast slabs;
连铸板坯热送过程传热模型研究
2.
The research progress of heat transfer model of the heat exchanger for ground-source heat pump;
地源热泵埋管换热器传热模型的研究进展
3.
Laplace solution for heat transfer model of dam leakage;
大坝渗漏传热模型及拉氏变换解
3) Heat-transfer model
传热模型
1.
Two-dimensional steady-state heat-transfer model of ohno continuous casting process;
热型连铸过程的二维稳态传热模型
2.
A heat-transfer model for ice-on-pipe thermal storage apparatus was established and the curve of the glycol temperature, The ice thickness and ice thermal storage rates& totals versus time was obtained when the chiller keeps full load in practical project.
建立了盘管式储冰装置的传热模型，得出了实际工程中保持机组满负荷运行工况下乙二醇进出储冰槽的温度变化曲线、盘管上冰的厚度随时间的变化曲线以及储冰槽逐时储冷量与总储冷量随时间的变化曲线，认为这些探讨有益于冰储冷装置的设计和系统的控制运行。
3.
By calculations, the characteristics of the one-dimensional steady-state heat-transfer model were described, which had been suggested on heated mould continuous casting of pure metals.
通过计算分析阐述了已有的纯金属热型连铸一维稳态传热模型的特性;在当量热导率、当量换热系数和固液界面位置一定的情况下,铸型温度与拉铸速度之间保持近似直线的关系。
4) Thermal model
传热模型
1.
Due to the complexity of thermal boundary conditions and physical features,however,thermal model solely obtained from heat analysis aspect is somehow not as precise as expected by comparison with real test data.
由于复杂的物理和边界条件,单纯从传热的角度得到的航天器传热模型与真实情况存在差别。
2.
In this paper,the development of thermal models of this structure with concise analysis was reviewed.
由于该结构的最大优点是低温差传热、蓄热性及其冷热负荷的转移能力,因此传热模型对该结构的优化设计及优化运行极为重要。
5) coking chamber
炭化室
1.
In order to solve the problem of over-campaign service of No1 coke oven,the falling off of cover top brick at combustion chamber of flues 1-4 at the machine side of coking chamber and the big resistance of pushing on coke,the author adopts local patch and repair technology for north and south walls at the machine side of the coking chamber.
针对1#焦炉超龄服役,炭化室机侧1-4火道燃烧室盖顶砖脱落、推焦阻力大等现状,采用局部挖补技术对炭化室机侧南北墙进行修复,介绍了修复措施和实施方案。
6) wide oven chamber
宽炭化室
补充资料：炭化室压力
炭化室压力
gas pressure in oven chamber
切刀huashi押li炭化室压力(助spressureinovenchamber) 焦炉炭化室粗煤气析出时形成的压力。是焦炉加热调节的压力指标之一。装煤初期，煤气析出量大，炉墙近处的压力可达IkPa以上，这时粗煤气易从炉墙漏气处渗入燃烧系统，部分窜漏煤气分解生成沉积炭，可堵塞漏气缝隙而使炉墙严密。在结焦末期煤气析出终了，炭化室底部出现负压，燃烧系统中含有过剩氧的废气会烧掉炉墙缝隙中的沉积炭而漏入炭化室，外界空气也易从炉门吸入炉内。从维护炉体、保证焦炉正常加热出发，要求炭化室内各点压力在任何时间都要高于相邻燃烧系统的压力和大气压力。为此，要维持集气管的适当压力，以便煤气倒流入结焦末期的炭化室，使炭化室底部保持大于SPa的正压。测定方法是，以全炉炭化室压力最小的、位于吸气管下的炭化室作为测压点。测压管由炉门下部测压孔插入。测压孔位于距炉底约300~处、相当于上升管中心的近炉墙处。装煤初期炭化室压力用u型压力表测量，结焦后期压力减小后改用斜型微压计测量。每小时测一次，直到推燕前桥管水封阀关闭为止。在结焦末期，如发现压力低于SPa，应适当提高集气管压力。 (李弘毅马秉瑞)
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参考词条