建立链篦机篦床温度场与气压场综合控制系统。
The comprehensive controlling system for the temperature field and the air pressure of the grate bed of the grate is established.
干燥速率随流化床温度的提高和物料尺寸的减小而加快；
The drying rate increases with increasing bed temperature and decreasing product size.
通过对烧结过程中粉床温度的筛选，烧结出尺寸精度较高的蜡模。
The wax models with high accuracy were sintered by filtering powder bed temperature of sintering process.
为了使蜡模获得稳定的尺寸，烧结过程中的粉床温度应尽量低于蜡粉材料的板结温度。
Powder bed temperature of sintering process should be lower than agglomeration temperature of composite wax powder, which result in dimensional instability.
由于煤泥凝聚团的强度随沸腾床温度的降低，沸沸炉的燃烧效率也随床温降低而有较明显的降低。
Combustion efficiency also decrease with bed temperature because of the decrease in strength of the fuel agglomerates.
据布鲁斯说，人们在房间温度是65至75华氏度之间，床的表面温度是82至86华氏度之间的时候睡眠最好。
According to Breus, people sleep best when the room is between 65 and 75 degrees Fahrenheit and the bed's surface is between 82 and 86 degrees Fahrenheit.
建立了此反应器的二维拟均相模型，用正交配置方法离散后求解了床层的径向与轴向温度及浓度分布。
Orthogonal collocation method was used to discretize the two dimensional pseudo-homogeneous model used and the temperature and concentration profiles were calculated.
下泄热交换器将流体的温度降到合适的定值，这个温度下，净化床工作允许。
The letdown heat exchanger reduces letdown fluid temperature to a value that is compatible with the ion exchanger resin.
在一定的基本蒸汽负荷下，燃树皮产汽负荷的上限值可根据流化床中树皮的稳定燃烧温度和减温系统的工作能力来确定。
The maximum steam load produced by the bark was determined by the bark fixed combustion temperature and the capacity of attemperator system when the basic steam load was given.
认为对物料的传热是生产过程中的主要控制因素，由于料层中温度梯度的存在，影响到物料床中不同层次分解的钴粉聚集长大过程。
The results show that the main factor is the heat transferring to the material, the conglomeration and growing of the cobalt powder on different material bed is effected by the temperature gradient.
实验和计算结果显示，玄武岩颗粒料床的导热系数随温度线性的增加。
The experimental results show that the effective thermal conductivities of basalt beds increase linearly as temperature increases.
在固定床内随着温度的提高，反应速率增大，并能达到较高的转化率。
In the fixed bed reactor the rate increases with the temperature and the high conversion rate is achieved.
本文根据酵母废液的水质特点，采用了常温升流式厌氧污泥床处理工艺，即温度在26。
Under normal temperature, UASB is adopted to treat yeast sewage according to yeast solution, specielty T=26.
利用高低压发射装置，测定了含能颗粒床在不同环境温度下动态撞击与动态挤压的破碎程度；
The grain fracture of energetic particle bed as a result of dynamic impact and dynamic compression at different temperature was measured by using a high-low pressure launch set.
用到循环流化床锅炉启动，可以任意调整出口烟气温度、出口烟气射流长度。
Exit flue gas temperature, flue gas quantity and length of flue gas jet could be control conveniently according to requirement of the boiler start up process.
当温度升高、床层厚度增加及水蒸气流量增加时，锑的挥发率相应在增加。
The experimental results showed that the volatilization ratio increases with the increasing of the reaction temperature, steam flow rate and decreasing of bed thickness.
完成粉末的包衣供液量自动控制，床内温度稳定无飞溅。
Auto control of liquid amount to be supplied and the temperature in the bed is constant and no splash.
本文首先从理论上分析了温度对气固流化床的临界流化速度的影响。
In this paper, the influence of temperatures on the critical fluidization velocity was analyzed theoretically at first.
采用合适的反应器结构来保证催化剂床层温度的相对恒定，是合成过程高效、稳定运行的关键。
To apply suitable structure of the reactor may ensure the relative stable temperature in the catalysis layer, it is the key of stable performance of synthesis process.
结果表明，催化床进口温度是实现氨合成塔优化操作的最优调节参数。
The result indicates that temperature at the inlet of catalyst bed is the most optimal control parameter to realize the optimal operation of ammonia converter.
在固定床内随着温度的提高，反应速率增大，并能达到较高的转化率。
It is found that the rate increases with the rise of temperature and high conversion rate can be achieved.
提高起始反应温度使催化剂床层温度整体过高导致飞温。
同时发现，床层压力和温度对聚乙烯粒径分布的影响很小。
The effect of bed temperature and pressure on PSD can be neglected.
流化床实际运行负荷的上限值可根据基本蒸汽负荷、流化床中树皮的稳定燃烧温度和减温系统的工作能力来确定。
The upper limit of operating load of the fluidized bed is determined by the basic load, stable combustion temperature of barks and the ability of the attemperation system.
对高参数灵敏性固定床反应器的径向温度分布作了简化处理。
Simplified approach to the radial temperature profile in highly sensitive fixed-bed reactors is suggested.
以太阳能为驱动热源，分析了吸附床内温度在某时刻的静态分布以及温度、压力和脱附速率随时间的动态变化。
Taking solar energy as a drive thermal resource, the static temperature distribution at some time, the dynamic state change of temperature, pressure and desorption speed with time was analyzed.
在管内工质温度不同、容量不同的3台循环流化床锅炉上，测量了不同高度上膜式水冷壁的金属壁温。
The membrane wall's metal temperature was measured at different heights, of 3 circulating fluidized bed boilers, of different capacity, and with different working medium temperatures within the pipes.
实验表明，双喷嘴矩形喷动床的最小喷动速度与颗粒粒径、床层高度及操作温度有关。
The experiment shows that the minimum spouting velocity was related to the particle sizes, bed height, and operational temperatures.
考查了床层温度、进料浓度、表观气速和吸附剂粒径对吸附性能的影响。
The effects of bed temperature, input concentration, apparent gas speed, and absorbent grain size on the absorption performance were studied.
由于达到平衡很快，故测定床层出口处的气体和固体温度差是不实际的。
Because of this rapid attainment of equilibrium it is not practical to measure the temperature difference between gas and solid at the bed exit.
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