Be favor of industrialization using fixed bed reactor.
采用固定床反应器，有利于工业化。
In this paper lead in industrial wastewater can be removed by scrap-iron fixed bed reactor.
采用铁屑固定床反应器去除工业废水中的铅。
Pre-esterification of China wood oil catalyzed by solid acid in fixed bed reactor was researched.
利用固定床反应器，以固体酸为催化剂催化桐油预酯化反应。
Thus the hot spot which causes catalyst deactivation in conventional fixed bed reactor is avoided.
这样就避免了一般固定床反应器中过热部位使催化剂减活的现象。
The oligomerization test of mixed olefins in light coke gasoline was carried out in a fixed bed reactor.
在实验室小型固定床反应器上，以焦化汽油轻馏分为原料，进行了混合烯烃的叠合反应。
In the fixed bed reactor the rate increases with the temperature and the high conversion rate is achieved.
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。
The reactions were carried out in an isocratic reactor and an oil bath fixed bed reactor, which are designed by us.
反应是在实验室自行设计的无梯度反应器和油浴固定床反应器中进行。
Three different kinds of catalysts for methanol pyrolysis are screened out on a continuous fixed bed reactor system.
在固定床连续流动式反应装置上评选出了三种不同类型的甲醇裂解催化剂。
The control of catalyst bed temperature in a fixed bed reactor during high exothermic reactions is of primary concern to designers.
在强放热反应的固定床催化反应器的设计中，床层温度的控制常成为设计的主要焦点。
A new cascade nonlinear inferential control strategy for a nonadiabatic fixed bed reactor based on improved hybrid model is proposed.
提出了非绝热式固定床反应器基于改进混合模型的串级非线性推断控制策略。
The reaction took place in the fixed bed reactor. By using steady state model, each step kinetic parameter in the reaction net was acquired.
反应是在固定床的条件下进行的，通过建立稳态反应模型，求出了异构化反应网络中的每一步动力学参数。
The synthesis and processing conditions of the bifunctional catalyst for dimethyl ether were studied by using fixed bed reactor in the paper.
本论文采用固定床反应器，对合成二甲醚双功能催化剂及其工艺条件进行了研究。
The catalyst was prepared by impregnating depositing process and the catalyst activity was evaluated with a continuous flow fixed bed reactor.
采用固定床连续流动反应装置，对此催化剂用于气相苯加氢制环已烷的活性进行评价。
The structure forms of catalyst support for tubular fixed bed reactor underwent the evolution from complex to simple and from difficult to easy.
列管式固定床反应器催化剂支托的结构形式，经历了由繁到简、由难到易的演变。
The deoxygenation combustion reaction was researched in a fixed bed reactor and in a cycle reactor with alcohol and wood charcoal as deoxidizer.
研究了乙醇和木炭脱氧剂在固定床和循环反应器中的脱氧燃烧反应。
The characteristics of fixed bed reactor, fluidized bed reactor, membrane reactor and other reactors which were developed recently were summarized.
另外还对固定床、流化床、膜反应器以及一些新开发的反应器的特点进行了讨论。
The effect of mineral on conversion of coal and sulfur with different forms in Yima during pyrolysis and hydropyrolysis in a fixed bed reactor was studied.
在加压固定床上研究了矿物质对义马煤热解和加氢热解产物分布规律以及不同形态硫转化的影响。
The performance of the catalysts for hydrodeoxygenation of model organic compounds, butyric acid and butanol, was investigated in a continuous fixed bed reactor.
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 fixed bed reactor, fluidized bed reactor and slurry reactors were compared on their structure, production capacity, materials, products and operating conditions.
并对固定床、流化床和浆态床反应器的结构、生产能力、原料及产物组成和操作条件等进行了比较。
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.
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。
Their catalytic activities were measured by alkylation of benzene with 1-dodecene as model reaction in a slurry reactor under atmospheric pressure and fixed bed reactor.
在常压反应釜和固定床反应装置上进行，评价了催化剂对苯和1-十二烯烷基化反应催化性能。
An one dimensional homogenous adiabatic fixed bed reactor model was adopted to simulate a radial flow reactor for dehydrogenation of ethylbenzene to styrene under vacuum.
采用一维拟均相绝热径向反应器模型模拟乙苯负压脱氢径向反应器。
The two dimensional pseudohomogeneous model was often used for the non isothermal, non adiabatic fixed bed reactor that was widely used for the strongly exothermic reactions.
非恒温非绝热固定床反应器广泛应用于强放热的反应体系。
The results showed amount of enzyme adsorption were more in fixed bed reactor than in tank reactor, and there were close variations of enzyme activity in two types of reactor.
结果表明，固定床反应器的酶吸附比釜式多，而酶的活性变化在两种型式反应器中比较接近。
The selective catalytic synthesis of dimethylamine from ammonia and methylalcohol over cerium modified mordenite under ambient pressure in a fixed bed reactor has been studied.
研究了氨和甲醇以铈改性丝光沸石为催化剂，在常压固定床上选择性合成二甲胺的反应。
The nickel distribution of residue feedstock and products obtained from fixed bed reactor were studied and focused on the effect of reaction temperature and various hydrotreating catalysts.
对混合渣油及其经固定床加氢处理后生成油的镍分布进行了研究，考察反应温度和加氢处理催化剂对油样中镍分布的影响。
The oxidative dehydrogenation of butane to butene and butadiene was studied by using conventional fixed bed reactor (FBR), inert membrane reactor (IMR) and mixed inert membrane reactor (MIMR).
比较了固定床反应器（FBR）、惰性膜反应器（IMR）与混合式惰性膜反应器（MIMR）用于丁烷氧化脱氢制丁烯和丁二烯反应的性能。
Fatty acid methyl esters were prepared by esterification in a fixed bed reactor from methanol and fatty acids in palm oil deodorizer distillate (PODD) using a cation exchange resin as catalyst.
以强酸性阳离子交换树脂为催化剂，经过自制的固定床反应器，使棕榈油脱臭馏出物(PODD)中的脂肪酸与甲醇起酯化反应，合成脂肪酸甲酯。
A new equipment-column type suspension reactor with multiple trays, has been developed for the condensation of phenol with acetone in the production of BPA instead of conventional fixed bed reactor.
开发了一种被称为多段悬浮床塔式反应器的新型装置，以代替双酚a生产中苯酚与丙酮缩合反应所使用的固定床反应器。
A new equipment-column type suspension reactor with multiple trays, has been developed for the condensation of phenol with acetone in the production of BPA instead of conventional fixed bed reactor.
开发了一种被称为多段悬浮床塔式反应器的新型装置，以代替双酚a生产中苯酚与丙酮缩合反应所使用的固定床反应器。
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