流化床反应器

工业流化床反应器结块监视的动态PCA方法

Dynamic principal component analysis method for chunk monitoring of industrial fluidized-bed reactor

一体式光催化氧化-膜分离三相流化床反应器

Integrative three-phase fluidized-bed reactor coupling with photocatalysis and organic membrane separation

采用负载型纳米TiO2/AC在流化床反应器中降解罗丹明B染料废水。

Rhodamine B dye wastewater was degraded by supported nanometer TiO_2 / AC in fluid bed reactor .

丙烯腈流化床反应器进料系统的PID自动整定

PID Auto-tuning of the Feed System of an Acrylonitrile Fluid Bed Reactor

PP气相流化床反应器平均停留时间的计算

Calculation of Mean Residence Time of the Powder in the Gas Fluid Bed Reactors

在流化床反应器中进行甲烷临氧CO2重整制合成气反应。

Methane reforming with CO2 in the presence of oxygen was studied in a fluidized bed reactor .

在鼓泡流化床反应器中进行了神木煤添加CaO的煤温和气化研究。

The mild gasification of Shenmu coal is investigated in an experimental fluidized bed reactor .

采用分步浸渍方法，制备了高分散的Ni/MgO-SiO2催化剂，并在固定床和流化床反应器中对该催化剂用于甲烷临氧CO2自热重整制合成气反应进行了评价。

Highly dispersed Ni / MgO-SiO2 catalysts were prepared by successive impregnations , and autothermal CO2 reforming of methane in presence of Q2 was carried out in both fluidized and fixed bed reactors .

Unipol流化床反应器结块原因分析及预防

Analysis and Prevention of Blocking in Unipol Fluid-Bed Reactor

针对UO3还原建立了多孔挡板流化床反应器的模型。

In this paper a perforated baffled fluidized bed reactor model is proposed using UO_3 reduction .

混合时间短，可以用全混流反应器（CSTR）模型来描述外循环流化床反应器。

On account of shorter mix time the model of CSTR can be used to describe the fluid-bed reactor with double outer circulation .

为了对颗粒表面进行改性，在自行设计组装的流化床反应器中，利用化学气相沉积法（CVD）制备了不同的复合颗粒。

In order to modify the surface properties of the particles , composite particles are prepared by the process of Chemical Vapor Deposition ( CVD ) in a fluidized bed reactor .

对铝氧粉（Al2O3）和油焦粉进行反应的流化床反应器进行设计计算，该方法可用于有流化床的工业生产中。

The design and calculation of the fluid - bed at the reaction of Al2O3 and the oil coke powder is given . The method can be used in industrial production .

进一步的，本文建立了MTO过程的湍动流化床反应器模型。

Fluidized bed reactor simulation . A turbulent fluidized bed reactor model was developed for the MTO process , which included two parts .

通过对鼓泡塔式（BC）和内循环气升式（AL）生物流化床反应器水力停留时间分布的研究，发现用组合模型可以描述这两种生物反应器的停留时间分布。

The resident time distribution ( RTD ) of bubble column bioreactor ( BC ) and airlift loop bioreactor ( AL ) could be described in combinated model according to the studies on the hydraulics of BC and AL .

对Unipol气相流化床反应器冷凝操作时聚乙烯树脂灰分增加的原因进行了分析。

Reasons of ash content increasing in Unipol polyethylene produced from gas fluidized bed reactor and operated in condensate mode , were analysed .

在流化床反应器中，以SAPO-34分子筛为催化剂，研究了反应温度对甲醇制烯烃反应副产物生成规律的影响。

The effects of reaction temperature on the byproducts formation in methanol to olefins were investigated based on the SAPO-34 zeolite catalyst in a fluidized bed reactor .

用H-198催化剂在流化床反应器中丁烯氧化脱氢生产丁二烯

Butadiene production by oxidation dehydrogenation of butadiene with h - 198 catalyst in fluidized bed reactor

GaN-MOCVD系统反应室流场的数值仿真声场强化微小流化床反应器流动特性研究

Numerical Simulation of Flow Patterns in the GaN-MOCVD Reactor Fluidization Properties in Micro-scale Fluidized Beds with Acoustic Intensification

在实验室小型固定流化床反应器上考察了工艺参数对国产GOR-Q催化剂降低催化汽油烯烃的影响。

Based on fixed fluid bed reactor and GOR Q catalyst , the influence of process parameters on decreasing gasoline olefin was studied .

本文报道了在φ63×740mm多孔挡板流化床反应器中，用裂解氨还原脱硝UO3制取UO2的有关试验数据。

Experimental data are reported for the reduction of UO_3 to UO_2 by cracked ammonia in a φ 63 × 740mm fluidized bed reactor equipped with perforated baffles .

以单一粒径2mm的聚丙烯树脂为试验物料，空气作为气化介质，在内径100mm，高3.5m流化床反应器内对聚丙烯类塑料的空气气化特性进行了试验研究。

An experimental study on air gasification of polypropylene ( PP ) with 2 mm in particle diameter was carried out in a gasifier with 100 mm inner diameter and 3.5 m total height .

通过内循环三相生物流化床反应器（ITFB）的清水试验，对其相含率及氧的传递特性进行了研究。

Study on the gas holdup and oxygen transfer in a internal-circulation three-phase biofluidised bed ( ITFB ) with tap water was conducted .

甲醇制烯烃（MTO）是一个重要的煤化工过程，本文针对新型MTO动力学及MTO湍动流化床反应器的模型化展开详细研究。

Methanol to olefins ( MTO ) is an important coal chemical process . In this paper , modeling and simulation of the turbulent fluidized bed reactor applied to MTO process were carried out . The works include the following three parts : 1 .

实验室规模的研究表明，用三相气提升内循环流化床反应器（AILR）处理焦化污水比活性污泥法为优。

The results of the experiments in a bench-scale airlift-internal-loop reactor ( AILR ) indicated that AILR was superior to the activated sludge process for the treatment of coke-chemical wastewater .

结果表明，同轴双锥两级气固分离器的分离效率在98%以上，气固分离器的压力损失在100Pa以下，设备磨损小，能够满足下行循环流化床反应器的要求。

The results indicate that the separating efficiency is more than 98 % , the pressure drop of the separator is less than 100 Pa , and the abrasion is very little .

石灰石流化床反应器处理矿山酸性废水

Limestone Fluidized Bed Reactor Used in Treating Mine Acid Waste Water

内循环三相生物流化床反应器的相含率及氧传递特性研究

Phase holdup and oxygen transfer in an internal-circulation three-phase Bio-Fluidised bed

气固并流下行快速流化床反应器颗粒运动规律的研究

Particle Flow Patterns in a Gas-Solid Cocurrent Downflow Fast Fluidized Bed

流化床反应器塔型内构件的研究

A Study of Pagoda Type Vertical Internal Baffle in Gas-Fluidized Bed