固定床反应器

在固定床反应器内，乙醇和乙二胺经分子间催化胺化反应合成了N-乙基乙二胺（NEED），考察了一系列铜系催化剂的活性，并筛选出催化性能较好的Cu-Mg/Al2O3催化剂；

N-ethylethylenediamine ( NEED ) was catalytically synthesized from ethanol and 1,2-ethylenediamine ( ED ) in a fixed-bed reactor .

本文对甲醇制丙烯（MTP）反应体系上的固定床反应器进行了模拟。

The fixed-bed reactor of methanol to propylene was studied in this paper .

固定床反应器进行n级反应的飞温判据

The Criterion for Runaway of the n-th Order Reaction in Fixed Bed Reactor

PLC在固定床反应器加氢试验中的应用

Application of PLC in the Hydrogenation Unit on the Fixed Bed Reactor

用固定床反应器对苯胺和醇类气相N烷基化反应进行了研究。

The study was made of gas N alkylation of aniline and alcohol in fixed bed reactor .

传递函数法求取H2在B-204低变催化剂固定床反应器上的吸附和传递系数

Evaluation of adsorption and transport coefficients of porous catalyst in fixed-bed reactors by transfer function method

CO选择性催化氧化性能是在固定床反应器上进行的。

The catalytic properties for CO selective oxidation reaction were evaluated in a fixed-bed reactor .

在固定床反应器上对Mo修饰前后β沸石醚化性能进行了评价。

The etherification activity of β - zeolite was evaluated in a fix-bed reactor .

微波诱导Fe2O3／γ-Al2O3催化氧化固定床反应器处理含酚废水

Application of Fe_2O_3 / γ - Al_2O_3 packed-bed reactor by microwave induced catalytic oxidation process to treat phenol

固定床反应器中Ti-MWW催化H2O2分解

Hydrogen Peroxide Decomposition Catalyzed by Ti-MWW in a Fixed-Bed Reactor

由过渡金属A和B活性组分与硅铝载体制备的催化剂，在固定床反应器中通过氢转移技术降低催化裂化汽油烯烃含量，达到改质目的。

FCC gasoline can be upgraded by hydrogen transfer to reduce the content of olefin using active A and B components supported on silica-alumina as catalysts in fixed-bed reactor .

本文采用Cu基催化剂，在连续流动管式固定床反应器中，研究了SE气相加氢反应本征动力学。

The intrinsic kinetics study of the gas phase hydrogenation of SE over a Cu-based catalyst was performed in a continuous flow fixed bed reactor .

在固定床反应器上对吸收/催化剂CuO/γAl2O3吸收SO2的过程进行了实验研究。

The absorption process of SO 2 by CuO / γ Al 2O 3 on a fixed bed reactor was studied .

在固定床反应器中，研究用改性活性半焦来脱除烟气中SO2的动力学问题。考察半焦粒径、反应温度和空速对SO2转化率的影响，建立了本征动力学方程。

The kinetics for removal of SO2 from flue gas using modified activated semi-coke was studied in a fixed bed reactor .

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 .

用常规固定床反应器考察了PdSiW12/SiO2催化剂还原条件对乙烯直接氧化合成乙酸催化性能的影响。

The effect of reduction conditions of Pd SiW 12 / SiO 2 catalyst was examined for direct oxidation of ethylene to acetic acid in a fixed bed reactor .

固定床反应器MgO／BaCO3甲烷氧化偶联催化剂的稳定性

Stability Test of MgO / BaCO_3 Catalyst for Oxidative Coupling of Methane in Fixed-Bed Reactor

列管式固定床反应器振荡操作研究&以Bang-Bang控制方法产生强制振荡

Forced Oscillating Operation of Non-isothermal and Non-adiabatic Fixed Bed Reactor & Forced Oscillations Caused by Bang-Bang Control

微型固定床反应器评价Pd-Al2O3催化剂活性

Evaluation of the activity of Pd-Al_2O_3 catalysts for anthraquinone hydrogenation by the fixed-bed microreactor

在常压固定床反应器中评价了各种添加剂对PbO/γ-Al2O3催化剂上甲烷氧化偶联反应的影响。

The effect of various additives on the performance of PbO / γ - Al2O3 catalyst for the titled reaction was evaluated in a fixed bed reactor at atmospheric pressure .

采用浸渍法制备V2O5/TiO2催化剂，在固定床反应器中对NH3选择性催化还原（SCR）NOx进行了实验研究。

Selective catalytic reduction ( SCR ) of NOX with NH3 has been investigated in a fixed-bed reactor by the use of the V2O5 / TiO2 catalysts prepared by impregnation .

分别在流化床和固定床反应器中考察了该催化剂对甲烷临氧CO2重整制合成气反应的催化性能及稳定性。

Catalytic performance and stability of Ni / MgO-CeO_2-SiO_2 were investigated for reforming of methane with CO_2 and O_2 to produce syngas , in fluidized bed and fixed bed reactor , respectively .

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 .

介绍了在流化床和固定床反应器中对高温煤气中硫化物、NH3、HCl、焦油组分和碱金属化合物等脱除的全面研究。

The removal methods of NH 3 , sulfur compounds , HCl , tar component and alkali metal compounds in hot coal gas are reported .

通过共混法制备MoO3/TiO2催化剂，并在固定床反应器中进行了NH3选择性催化还原脱除NOx的研究。

Selective catalytic reduction NO x with NH 3 was conducted in fixed bed reactor catalyzed by MoO 3 / TiO 2 which were prepared by mixing .

以SO2－4／TiO2型固体超强酸为催化剂，在固定床反应器上，通过连续法考察了乙酸与乙醇酯化反应的情况。

The reaction of acetic acid with ethanol was studied in fixed bed micro reactor by continuous process under the catalyst of SO 2 - 4 / TiO 2 type solid super acid .

实验在固定床反应器中，研究了催化剂的酸度，原料液的含水量，反应温度，液体进样量和N2流量对于催化性能的影响。

In the experiments , the effects of acidity of the catalyst , the ratio of water / methyl lactate in feeding stock , reaction temperature , flow rate of N_2 and feeding stock on the conversion ratio and yield were investigated .

并以二苯并噻吩（DBT）为模型化合物在固定床反应器上考察了MoP催化剂的HDS性能。

The HDS performance of the prepared MoP catalysts were evaluated in a fixed bed reactor using dibenzothiophene ( DBT ) in decalin as the feed .

采用连续法在固定床反应器中合成出了乙二醇单叔丁基醚（GBE）。

Ethylene glycol mono-tert-butyl ether ( GBE ) was synthesized continuously in a fixed bed reactor , and the characteristics of the reaction were studied .

在柱式固定床反应器中，固定化酶连续催化油酸与十二醇酯化时，连续运行50d酯化率仍高达73%。

The esterification ratio was still 73 % after running in continuous flow column reactor for 50 days .