1)gas-solid fluidization气固流态化
1.Application of gas-solid fluidization technology to coal preparation气固流态化技术在选煤领域的应用
2.The principle of gas-solid fluidization and classification towers are introduced.根据气固流态化原理,介绍了流化精分塔的工作原理,依据波纹填料塔的计算方法,首次进行了超细粉体流化精分塔的试验结构设计,塔内构造简单,没有动元件,便于大规模分级应用。
3.The application of airflow in cereal cleaning is summarized, and the characteristics and principle of cereal winnowing by gas-solid fluidization are analyzed, thus providing a certain basis for developing a new type of air separation equipment.综述了气流在谷物清理中的应用情况 ,分析了气固流态化风选的特点和原理 ,为研究开发新型风选设备提供了一定的理论基
英文短句/例句
1.Study on Gas-Solids Fluidization Behaviors in Centrifugal Fluidized Beds;离心流化床中气固流态化行为的研究
2.Research on Baosteel OMC Iron Ore Reduction Process of Gas-solid Fluidization宝钢OMC铁矿粉气固流态化还原过程的研究
3.Numerical Simulation and Experiment on the Gas Solid Flow and Combustion Character in Circulating Fluidized Bed Combustion for Solid Medical Waste;固态医疗垃圾循环流化床气固流动与燃烧特性数值分析及实验
4.Simulation of the Behavior of Gas-Solid Flow in a Novel Rotating Fluidized Bed in a Static Geometry新型静态旋转流化床内气固流动行为的数值模拟
5.the process of changing from a gaseous to a liquid or solid state.由气态向液态或固态变化的过程。
6.Numerical simulation of gas-solid two-phase flow in a Texaco entrained-flow coal gasifierTexaco气流床煤气化炉内气固两相流动的数值模拟
7.Microscopical experimental investigation on complex flow with gas-liquid-solid phase change through porous media气-液-固变相态复杂渗流微观实验研究
8.Research on the Gas-solid Two-phase Characteristics of Swirl Tube in Third Stage Separators for FCC催化裂化三旋内部气固两相流动分析
9.In aerated flow,solids are fluidized or suspended by the gas.在充气流动中，固体颗粒被气体流化或悬浮起来。
10.Cold Model Experiments and Numerical Simulation of the Gas-Solids Flow Characteristics on a Selective Fluidized Bed Bottom Ash Coler for a 410t/h CFB Boiler;410t/h CFB锅炉选择性流化床冷渣器气固流动特性冷态试验研究与数值模拟
11.Experimental Investigation on Drying Characteristics of Gas-Solid Stirred Fluidized Bed;气固搅拌流化床的干燥特性实验研究
12.Detection of distributor dead-zone in gas-solid fluidized bed by acoustic emission method气固流化床分布板死区的声发射检测
13.Study on the Solid Food Fluidization Ultra High Temperature Sterilization Technology;固体食品流态化超高温杀菌技术研究
14.A New Type of Dry Slag Extraction Device for Fluidized Bed一种用于流化床的新型固态排渣装置
15.A liquid-solid dynamic coupling modelof ultrasound enhanced coalbed gas desorption and flow声场促进煤层气渗流的应力-温度-渗流压力场的流固动态耦合模型
16.(chemistry) a change directly from the solid to the gaseous state without becoming liquid.（化学）物质由固态不经过液态直接转化为气态的变化。
17.Numerical Simulation and Experimental Study on the Gas-Solid Flow in Internally Circulating Fluidized Beds;内循环流化床气固流动数值模拟与试验研究
18.Study on Characteristics of the Gas-Solid Two Phase Flow in Magnetically Fluidized Bed and Its Application;磁流化床气固两相流动特性及其应用的研究
相关短句/例句
nonfluidized gas-particle flow非流态化气固流
3)gas-liquid-solid fluidization气液固流态化
4)solid-liquid fluidization液固流态化
1.Investigation of density consist of coal by use of the technique of solid-liquid fluidization;利用液固流态化技术测量煤炭密度组成的研究
5)fluidization (of solid)固体流态化
6)gas-solid fluidized bed气固流化床
1.Electrostatic potential distribution in gas-solid fluidized beds and measurement of bed level;气固流化床中静电压分布及料位检测
2.Electrostatic behavior with fines of different sizes added into gas-solid fluidized bed;细颗粒对气固流化床中静电行为的影响
3.Measurement of acoustic emissions and flow pattern in gas-solid fluidized bed;气固流化床中声发射和流动模式关系
延伸阅读
液-固流态化反应器解析液-固流态化反应器解析analysis of liquid-solid system fluidizing reactor ye一gu liutaihua fanylngq.Jiexi液一固流态化反应器解析(analysis。f liquid-solid system fluidizing reaetor)为优化液一固流态化反应器的湿法冶金过程及其设备而进行的数学解析。目的是为了建立描述流态化湿法冶金(见流态化浸出)体系中固体颗粒与液相间相对运动状态方程和反应速率方程，通过对方程分析求解，为合理设计流态化浸出器、洗涤器和置换器制定最佳操作制度提供依据。 广义流态化关系式湿法冶金过程的流态化现象多属液固系统的散式流态化。均匀颗粒的散式流态化，可用 △P=(乃一P，)(l一。)H(1) u=u，扩(2)近似关系式描述。对于同时加入和排出固体颗粒的流态化系统，可用颗粒和液体之间的相对速度代替(2)式中的u，从而形成广义流态化的关系式: C 双n一左刁t—)~亡一配t3) 1一C式中u。和u己分别为液体和颗粒的空管线速度;“‘为颗粒终端速度;。为空隙度，即反应器内液相所占空间与总空间之比;众为颗粒一液体空塔线速的换算因子;n为空隙度指数，取决于颗粒的直径、形状及颗粒和液体的属性。对特定的颗粒一液体体系，“，和n值恒定，根据式(l)可绘制广义流态化等n图。图中的矿。一u0/ut，矿d~ud/。。。图中分为三个主要区域，分别描述颗粒与液体同时向上(BC线以右)、同时向下(AGE线以左)和相互逆向(AGECB区)三种运动方式。流I一撅一海 ，L、S、￡ (二七)+(一吮)(—)=扩u， 、户户今’、八A’‘1一。j一‘ ’“厂兰三三三砰三三藉乏三三之之i二~厂二{不石互二二二二二月(3b) ‘、nL一~、~1、、、、b宁l令7/〔扮/0.爹尹产一习若令N~二代入(3b)式，即可 0 sr、丈户短l世l钧李I//Z夕/J才尹乡卜/{，，AN(1一。)+。 {\艺1节l、性’户///之//了/一洲产产IA尹二~~二二-上止二~-二乙~J止 一\垢}绝1 VI//，，/7/z/’//}一A，扩(1一￡) 。07卜\\l职U了/劝万///灯)。乌/尸州(4) !\.勺11了/劝才////性{//}一一.5、，_‘、_一~、.、一 、1冲。1/}/麒黔//引//1式中儿一赢为颗粒在终端速 ‘叫丫一少_扩姗附/骂丫丫乡洲度。:下，厦洗设备所需的断面 }\”了朋盯///{//}积，称为“终端断面积”;川称为 0 .5卜\了I口I月rl////产l 一}\、\d万尹涅左//一//}“对比断面积”。在设计计算时， 。
