The hot exit gas from the reformer enters the refractory-lined inlet chamber.
热出口气体从转化炉进入耐火材料衬里的进气室。
In order to allow Ni catalyst work at a mild temperature with little sintering and carbon formation, the influence of composition of reformer inlet gas on reforming temperature at a certain space velocity and conversion of feed CH4 was studied. At the same time, a method of changing inlet gas composition by introducing circulating gas into the feed gas was also discussed.
为了使Ni系催化剂在不易发生烧结积炭的温度下工作，分析了在一定原料CH4空速和转化率下人口气体组成对重整工作温度的影响，并探讨了在原料气中导入循环气来改变重整人口气体组成的方法。
The volume for this reformer system is set to be smaller than 500cm3, functioned with fuel storage, fuel inlet and vaporization, reformer, reformed gas purification.
重组器模组体积必须小於500 cm3，内部整合的功能包含甲醇储存、燃料入口与汽化、重组反应区、气体纯化。
The inlet section of the sandpack was preheated by injecting hot nitrogen gas, prior to starting ignition.
氮气由预先启动的点火器加热，沙包入口部件被注入热氮气预热。
The development of resource of marine oil gas is used, part of aux will be able to solves number of feed inlet of resource of our country oil gas to measure.
海洋油气资源的开发利用，将能部分解决我国油气资源进口数量。
Among these three factors, the increase in gas inlet pressure yields the highest efficiency.
其中，以增加燃气入口压力所造成的效果最好。
This does not pose a problem, however, with pipeline s and liquefied gas products where inlet pressure is maintained relatively constant.
但是，对于入口压力相对恒定的管道和液化气体产品而言，这不是一个问题。
This does not pose a problem, however, with pipelines and liquefied gas products where inlet pressure is maintained relatively constant.
但是，对于入口压力相对恒定的管道和液化气体产品而言，这不是一个问题。
The simulation results show that the gas flow rate increases linearly with the rotating rate of circulating fan, and the inlet gas pressure increases squarely with the rotating rate of circulating fan.
计算结果表明气体的流量与风机转速呈线性关系，风机进出口的气体的压力与风机转速呈二次方关系，与理论公式一致，说明该方法是可行的。
For this process, the paper discussed the selection and the optimization of the main cycle parameters, and tracked the variations of efficiency and specific work with overall gas turbine pressure ratio and turbine inlet temperatures.
本文对该流程中的主要参数，如汽气比、涡轮前温度、总总压比、回热度等参数，对循环性能的影响进行了分析比较，得出要提高循环效率的规律性的结论。
A FFAP capillary column (30 m×0.53 mm, 1 μm) was used at 60℃. Nitrogen was used as carrier gas. The column inlet pressure was 20 kPa. The temperature at the injection port and the FID detector were 220℃ and 250℃, respectively. The flow rate of air and hydrogen were 500 ml/min and 50 ml/min.
以FFAP毛细管柱(30 m×0.53 mm，1μm)为色谱柱，柱温为60℃，载气为氮气，柱前压20 kPa，进样口温度为220℃，FID检测器，检测器温度为250℃，空气流速500ml/min，氢气流速50ml/min。
The results of this investigation are as follows. Firstly, in the situation of different atomizer designs, the inlet gas pressure and the position, shape as well as inner-diameter of the liquid guide tube, which influence the orifice pressure, has been studied systematically. Also, the formation mechanism of ΔP has been presumed and analysized.
首先，为保证熔体能自导液管中顺利地流出，采用自制的气体压力测量装置，针对不同的喷嘴结构，系统地研究了雾化进气压力，导液管末端位置、形状及其内径等参数对导液管末端压力差ΔP的影响规律，并分析、探讨了导液管末端压力差ΔP的形成机制。
The method comprises the following steps: entering the mixture gas containing hydrogen, carbonaceous gas and inactive gas into antechamber through inlet duct with water-cooling tube, and spraying to hot wire and underlay; bring the hot wire array with low bias voltage of positive electrode relative to underlay support and upper bias voltage of negative voltage relative to relative to make the underlay deposit surface nucleation; bring the hot wire array with low bias voltage of negative electrode relative to underlay support and upper bias voltage of positive voltage relative to relative to make the underlay deposit surface diamond film.
它是将含有氢气、含碳气体、惰性气体的混合气体，通过内有水冷通道的进气装置进入沉积室内，喷向热丝和衬底。对热丝阵列施以相对于衬底支撑台为正电极的下偏压，以及相对于进气装置为负电压的上偏压，使衬底沉积表面成核；对于衬底支撑台为0电压或负电压的下偏压，以及相对热丝阵列施以相对于进气装置为负电压的上偏压，使衬底沉积表面金刚石膜生长。
Based on the productive capacity of spray rotary drier - granulator, the output of monoammonium phosphate reached 50～60 kt/a by replacing tank neutralizer with high - speed ammoniation evaporator, increasing the area of each slurry heater to 100 m2, raising the inlet temperature of the spray rotary drier - granulator to 550～600℃ and adopting original cleaning tail gas system.
磷铵工段扩大能力应该以喷浆造粒干燥机的生产能力为基准，可以用高速氨化蒸盅器代替槽式中和器，将料浆加热器面积增至100 m2／台，提高喷浆造粒干燥机进口温度，使其达到550～600℃，则尾气净化系统仍可使用，相应的磷酸一铵生产能力可以达到5～6万吨／年。
The fuel is changed to liquefied gas, and the fuel supply system as well as the ignition system is simplified. after the combustion chamber is installed, a heated muffler experimental platform is completed. the experiment shows that, to a muffler whose inlet diameter is 100 mm and inlet flow rate is 45 m/s, the chamber can keep the temperature above 400 degree centigrade.
将改造后的燃烧器装到消声实验管路上进行试验，结果表明，对于一个进口管径为100mm的消声器，该燃烧器在保证进口处流速为45m/s的条件下，能将温度保持在400℃以上。
High inlet pressure can be caused by too high gas flow.
高气压力可能造成的过高的气体流量。
It is found that the loss of sulfur in sulfurized catalyst for both catalysts will be observed when sulfur content in inlet gas is lower than 0.1%, however, the sulfur content in practical coal gas is enough to avoid the phenomenon.
然而在实际的热煤气含硫的情况下，它显示出相当高的催化转化反应活性，适于在热煤气净化的条件下使用。
As the importance of uniformity of the inlet gas distribution has been realized, to design a good feed gas distributor becomes essential.
人们在认识气体均布问题重要性的同时，开发和研制新型的进气结构成为人们热门的课题。
The factors of compressor inlet variable stator blade, port crushing, gas bleed of compressor, intensive cooling of turbine blades were also considered.
重点分析了在这种故障过程中继电保护及其通道的动作行为。针对这些继电保护的误动作提出了相应的反事故措施。2006中国电机工程学会年会，河南郑州，中国电机工程学会
Based on the STAR-90 simulation support platform and the idea of modular modeling, this paper proposed the simulation model of single-shaft gas turbine, which included the model of compressor, combustor and turbine. The factors of compressor inlet variable stator blade, port crushing, gas bleed of compressor, intensive cooling of turbine blades were also considered.
基于STAR-90仿真支撑平台，采用模块化建模思想，建立了简单循环单轴燃气轮机的仿真模型，模型包括压气机、燃烧室、燃气透平、转子等部件，同时考虑了压气机进口可调导角、进排气压损、压气机抽气及透平叶片冷却等因素。