流动床

离子交换软化系列：如三塔流动床、组合式软水器和全自动软水器。

Ion exchange softening Series : If Mobile-bed tower , Combined softener and Automatic softener .

在流动床反应器上利用原位还原类钙钛复合氧化物所得纳米金属颗粒（Fe、Cu）催化裂解CH4可大量制备尺寸均一的碳纳米管。

Carbon nanotubes ( CNTs ) of uniform size can be abundantly produced by the catalytic decomposition of CH4 over metal ( Fe , Cu ) nano - particles prepared in situ by the reduction of perovskite-type oxides in a fluidized-bed catalytic reactor .

固定化藻类细胞流动床处理生活污水研究

Research on Immobilized Algae Cell Flow Bed for Treatment Living Sewage

流动床离子交换工艺在己二酸催化剂回收中的应用

Applications of Flowing Ion Exchange Technology in Adipic Acid Retrieve Catalyst

生物流动床氧化法处理核糖霉素废水的研究

Studies on the wastewater treatment of Ribostamycin by fluidized-bed oxidation process

流动床生物膜技术处理污水及资源化的研究

Study on Flowing Bed Biological Diaphragm Technique to Handle Waste Water and Its Resources

溶解被渗滤液溶解或分离塞摩福型流动床连续渗滤

To be dissolved or passed out by a percolating liquid . Thermofor continuous percolation

流动床生物膜与石灰混凝污水处理系统的研究

Study on Waste Water Treatment System of Floating Bed Biological Membrane with Lime Mixture Coagulation

平原细沙河流动床泥沙模型试验的模型相似律及设计方法

Similarity criterions and design method of hydraulic models with a movable bed for plain rivers carrying fine sediment

由于絮凝沉淀物形成的流动床有活性碳的作用，所以比气浮或沉淀的物化处理工艺提高10%～20%的去除率。

The removal rate can be 10 % 20 % higher than that of normal air flotation or setting physicochemical treatment process .

模拟流动床及固定床的改进为离子排斥法提糖注入了活力。载流子漂移型晶体管

The current development of simulated , moving bed and fixed-bed modeling have given a new impetus to molasses desugarization by ion exclusion . carrier drift transistor

A/O~2/移动床生物膜反应器组合工艺处理炼油废水的中试研究采用流动床生物膜工艺处理炼油污水

Pilot research of oil refinery wastewater treatment by combination process of A / O2 / MBBR Treatment of oil-refining wastewater by moving bed biofilm reaction technology

城市污水经流动床生物膜与石灰相结合的深度处理后，可用于电厂循环冷却水补充水。

The urban wastewater after deep treatment through the floating bed biological membrane in combination with lime can be used for make-up water of circulating cooling of power plant .

生化处理系统采用A~2O法处理工艺，好氧段结合流动床生物膜反应器的特点，采用活性污泥与生物膜的集成工艺进行处理的方案。

A ~ 2O process is applied in the biochemistry treatment system . The aerobic phase is linked with the character of Moving Bed Biofilm Reactor , Activated Sludge and Biofilm integration process is determined .

按照本发明的方法、按发明的装置（1）和按发明的供气系统的特征在于，所有输入到流动床室（3）里的空气都通过吸条机构（14）排出。

The whole air flowed into the flowing bed space ( 3 ) in the method , the apparatus ( 1 ) and the pneumatic system is discharged by a sucking rod-forming device ( 14 ) .

以KOAc/NaY为催化剂，在连续流动固定床反应器内，邻甲基苯酚（OC）与碳酸二甲酯（DMC）经过气固相催化反应合成了邻甲基苯甲醚（OM）。

Synthesis of o-methoxy toluene from o-cresol and methyl-carbonate ( DMC ) on KOAc / NaY catalyst in fixed bed reactor was investigated .

在常压连续流动固定床石英反应器上考察其在CO2氧化乙烷制乙烯反应的催化性能，实验结果表明：CeO2/-γAl2O3催化剂对CO2氧化乙烷制乙烯反应具有较好的催化活性。

The catalytic performance for oxidative dehydrogenation of ethane was studied in the continuous flowing fixed-bed reactor at room pressure . Experimental results indicated that the CeO_ ( 2 ) / γ - Al_ ( 2 ) O_ ( 3 ) catalyst showed higher catalytic activity .

在10mL连续流动固定床反应装置上，以苯的转化为模型反应考察了Pt／SAPO-11异构化催化剂的加氢性能及苯对正十四烷异构化反应的影响。

Hydrogenation of Pt / SAPO - 11 isomerization catalyst and effect of benzene on n - tetradecane hydroisomerization were investigated using benzene hydrogenation as a model reaction in a 10 mL fixed - bed down-flow reactor system .

在连续流动固定床反应器上，以氧气为氧源，活性炭作为催化剂用于催化氧化三氟二氯乙烷（HCFC-123）制备三氟乙酰氯（TFAC）的反应中。

Activated carbon was used as the catalyst for catalytic oxidation of 1,1-dichloro-2,2,2-trifluoroethane ( HCFC-123 ) to trifluoroacetyl chloride ( TFAC ) in fixed bed reactor .

2.8m~2流动干燥床

2.8 m ~ 2 fluidized-bed dryer

利用三维数值模型研究了具有自由液面的稳定流中直立墩柱周围的流体流动及床面冲刷过程。

The flow around a vertical circular pile piercing a free surface exposed to a steady current and the local scour process are studied numerically .

当具备了各个变量的校正数值之后，对于床层流动及床层体积的方程式也可以相应地修正。

As improved values for the various quantities become available , the equation given for flow and volumes of the bed may be modified correspondingly .

结果表明，在连续流动固定床反应器中异丁烷的转化率较高，但产物的分布很复杂，并与温度和空速有很大关系；邻苯二酚与异丁烯的烷基化反应

The results indicate that reaction in membrane reactor have a lower conversion rate , a much higher selectivity to isobutylene . Alkylation of Catechol by Isobutylene

以有机含氧化合物丁酸和丁醇为合成油品的模型化合物，在连续流动固定床反应器中考察了催化剂的加氢脱氧性能。

The performance of the catalysts for hydrodeoxygenation of model organic compounds , butyric acid and butanol , was investigated in a continuous fixed bed reactor .

对其中的关键设备，如混练机、流动干燥床的结构形式和工作原理，及其主要技术参数做了较为详细的介绍。

The structure , working mechanism and the main technical data of the key devices such as the mixer and the fluid bed dryer are given in detail .

在双功能催化剂上，利用连续流动固定床微反装置，进行了四氢萘加氢裂化反应动力学研究，得到了详细的产物分布并推测了7集总反应网络。

A study on kinetics of tetralin hydrocracking reaction had been completed by using a continuous flow fixed bed micro reactor on the dual functions hydrocracking catalyst . Detail product distribution was determined and the reaction network of 7 lumps is supposed .

在连续流动式固定床高压微反&色谱联合装置上做了C5／C6烷烃异构化动力学考察。

Kinetic experiment was carried out on high - pressure - micro - reactor that uses continuous flow fixed - bed and chromatography unit .

在流动相固定床反应器中对低浓度含氯有机废气在金属氧化物（MO）和钯/金属氧化物（Pd/MO）催化剂上的催化降解进行了研究。

Catalytic decomposition of organic waste gas containing chloride with low concetration over MO and Pd / MO catalysts were studied in a flowing fixedbed reactor .

没有热解室时，立管内为稀相流动和移动床流动同时存在，立管内平衡料柱高度随Ur的增加而升高。

If without pyrolysis chamber , the lean phase flow and the moving bed flow co-existed in the standpipe . And with the increase of U_r , the equilibrium height of the solid in the standpipe was heightened .

采用连续流动式固定床高压微反-色谱联合装置，考察了氧化镍、氧化钼含量对正戊烷加氢异构化镍-钼-氢型丝光沸石（Ni-Mo-HM）催化剂反应性能的影响。

Effect of loaded nickle and molybdenum contents on the reactivity of modified mordenite Ni-Mo-HM for pentane isomerization in the presence of hydrogen was investigated on a continuous flow high pressure fixed-bed micro reactor-chromatography unit .