Simulation calculation was carried out on industrial oxidation reactor on the basis of building a suitable para-xylene oxidation reaction kinetics.
在建立合适的对二甲苯氧化反应动力学基础上，对工业氧化反应器进行了模拟计算。
Therefore, maintaining highly dissolved oxygen in the contact oxidation reactor has a high efficiency for the treatment of rosin processing effluent.
接触氧化段较高的溶解氧对难降解的松脂加工废水有较好的处理效果。
This paper introduced a pilot-research of using EGSB(Expand Granular Sludge Bed) reactor and bio-contact oxidation reactor combination to treat the wastewater.
本文介绍了采用EGSB厌氧反应器和生物接触氧化工艺两者相结合的方法处理该类污水的现场试验研究。
To maximize the production capability ofp-xylene oxidation reactor, the method of reactor network synthesis was proposed to optimize network combinations of multi-reactors.
为了获得对二甲苯氧化反应器的最大生产能力，采用反应器合成的方法对多个氧化反应器组成的网络进行了优化研究。
Systematic review is carried out about the structure of oxidation reactor and the correlation between flow condition and it. The effect of its structure on the process of flow is analyzed.
对氧化反应器的结构及其与流动的关系进行了系统的总结，并分析了其结构对流动过程的影响。
In the method of air phase oxidation the mixed gas that boiling 1,2,4,5-tetramethyl benzene is combined with air is carried into oxidation reactor and reacts and then product gas is cooled.
气相氧化法是将空气与汽化后的均四甲苯混合进入含有催化剂的氧化反应器进行氧化反应，反应产物经换热冷却后，均苯四甲酸二酐直接从气相中凝华捕集。
There are a many factors influencing the quality of the cyclohexanone product during the cyclohexanone production, the most significant one is the control of lean oxygen feeding the oxidation reactor.
在环己酮生产过程中，影响环己酮产品质量的因素很多，其中最为显著的是供入氧化反应器的贫氧控制。
The oxidation and molecular recomposition proceeded in the same time, when the isobutanol gas and air passed the fixed bed catalytic reactor continuously.
异丁醇气体和空气混合后通过催化剂层的固定床反应器，使氧化反应和分子重排反应同时进行。
Reactor like oxidation ditch was used for anaerobic bioremediation of urban river water, in which biofilm formed on ceramic honeycomb carrier was used instated of activated sludge.
采用一种类似氧化沟的反应器，其中利用蜂窝陶瓷为载体形成生物膜替代活性污泥，对城市受污染的河道水体进行缺氧生物修复。
Oxidation ditch should keep the feature of PF reactor to an extent as increasing circulation ratio.
在提高氧化沟循环比的同时，应使氧化沟在一定程度上保留推流式反应器的特点。
Study on start-up of anaerobic ammonia oxidation process in UASB reactor has been conducted.
利用UASB反应器进行了厌氧氨氧化工艺的启动运行研究。
According to the capacity of isopropyl benzene oxidation reaction in Yansan chemical factory, the airlift reactor in our laboratory is amplified.
将实验室规模的气升式反应器依照燕山化工二厂异丙苯氧化反应的生产能力进行了放大。
Wastewater containing acrylic acid was treated by supercritical water oxidation (SCWO) technology in a continuous transpiring wall reactor.
采用超临界水氧化(SCWO)技术在连续蒸发壁式反应器内处理高浓度丙烯酸废水。
Studies on the regeneration of vanadium phosphorous oxides (VPO) catalyst for selective oxidation of propane to acrylic acid and acetic acid has been carried out using a pulse reactor.
采用脉冲反应器，研究了VPO催化剂的再生性质及其对晶格氧选择氧化丙烷制丙烯酸和乙酸的影响。
The existence and uniform boundedness of the global solutions of the model for sulphur dioxide oxidation in a tubular reactor with periodic flow reversal are proved by the invariant domain method.
利用不变区域方法，证明了二氧化硫催化氧化管式反应器流向变换强制操作模型整体解的存在性和一致有界性。
Multipipe reactor, vapor phase catalytic oxidation method using multipipe reactor, and start-up method applied to multipipe reactor.
多管反应器，使用多管反应器的气相催化氧化法，和应用于多管反应器的启动方法。
Research for intrinsic kinetics of ethylene oxidation on the YS-6 Silver Catalyst is done by using a fixed bed constant temperature integral reactor.
采用固定床恒温积分反应器，对YS—6型银催化剂进行乙烯氧化本征动力学研究。
The relation between biological and chemical oxidation of H2S was studied under different conditions in the aerobic reactor.
在好氧反应器中研究了不同条件下H2S生物氧化和化学氧化之间的关系。
The reside time of flue gas in the reactor has less effect on the NO oxidation.
NO的氧化受烟气在反应器内滞留时间的影响较小，而它受烟气流速的影响较大。
Hybrid anaerobic reactor (HAR), followed by biological contact oxidation (BC) technique, is used for treating domestic sewage.
试验采用复合式厌氧反应器(HAR)后续接生物接触氧化工艺(BC)处理生活污水。
A model of five-bubble-stirred-tank reactor (BSTR) for industrial uncatalyzed oxidation process of cyclohexane was established to predict and optimize the the industrial production.
论文针对环己烷液相无催化氧化的五釜串联鼓泡搅拌反应器生产装置(BSTR)，建立了氧化装置的过程数学模型。
The influence of filling inert stuffing on the partial oxidation of methane was investigated by fully filling inert material into the space of empty reactor or into the upper space of catalyst bed.
通过在催化剂床层上部气相空间填充惰性材料，考察了甲烷氧化反应中气相自由基反应对催化反应的影响。
The effects of technology parameters on reactor conversion rate and yield rate were investigated, the oxidation system stability sensitivity was analysed.
考察工艺参数对反应器转化率和收率的影响，分析了氧化系统稳定敏感性。
Using an inclined plate gas-liquid-solid separator UASB reactor followed by a biological contact oxidation process to treat fruit juice-producing wastewater, and excellent result is achieved.
采用斜板三相分离器uasb -生物接触氧化串联工艺处理果汁生产废水的工程实践，取得了良好的效果。
An anaerobic fluidized bed (AFB) reactor was used as anaerobic ammonium oxidation (ANAMMOX) reactor. The nitrogen removal of leachate was studied in this reactor.
采用厌氧流化床反应器(afb)作为厌氧氨氧化反应器，对垃圾渗滤液脱氮进行了研究。
The synthesis ofm—Cresol from o—toluic acid by air oxidation was studied in a 1 liter reactor under vigorous stirring conditions in order to eliminate film resistances.
在容积1升的反应釜中，在剧烈搅拌以消除膜阻的条件下研究了邻甲基苯甲酸空气催化氧化制间甲酚的反应。
This paper briefly introduces several techniques widely used in our country, such as oxidation ditch technology, SBR reactor, etc.
本文简单介绍了几种当前在我国已得到广泛使用处理工艺，如氧化沟工艺、SBR反应器等。
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。
Using an air-H_2O DC corona radical shower system, the influences of reside time of flue gas in the reactor, velocity of flue gas and NO concentration on NO oxidation process were studied.
运用以湿空气为自由基源物质的直流电晕自由基簇射系统，研究了烟气在反应器内的滞留时间、烟气流速和NO浓度对NO氧化过程的影响。
Using an air-H_2O DC corona radical shower system, the influences of reside time of flue gas in the reactor, velocity of flue gas and NO concentration on NO oxidation process were studied.
运用以湿空气为自由基源物质的直流电晕自由基簇射系统，研究了烟气在反应器内的滞留时间、烟气流速和NO浓度对NO氧化过程的影响。
应用推荐