1) agitating bubbling reactor
振荡鼓泡反应器
2) bubble column reactor
鼓泡反应器
1.
Backmixing characteristics of heat pipe type bubble column reactor;
热管式固定床鼓泡反应器返混试验研究
2.
In view of engineering design, considering low energy consumption and main factors influencing gas-liquid mass transfer, this paper discussed the optimization of operation parameters and material working condition for bubble column reactor.
从工程设计的角度,以影响气液传质主要因素入手,低能耗为目标,应用鼓泡技术对鼓泡反应器的操作条件以及物料工况作了优化。
3) bubble-column reactor
鼓泡反应器
1.
Investigation of heat pipe type gas-liquid-solid three-phase fixed-bed bubble-column reactor;
热管式气液固三相固定床鼓泡反应器试验研究
2.
Heat transfer performance of heat pipe type gas-liquid-solid three-phase fixed-bed bubble-column reactor;
热管式气液固三相固定床鼓泡反应器的传热性能
4) bubbling reactor
鼓泡反应器
1.
The paper introduced a perfectly mixed flow mathematics model of wet flue gas desulfurization (WFGD) for a pilot scale jet bubbling reactor (JBR),including the absorption model of SO 2 in lime slurry and a JBR reactor model.
以中试喷射鼓泡反应器 (JBR)为基础 ,该文建立了一种基于全混流的JBR湿法烟气脱硫数学模型 ,包括SO2 在石灰浆液中的吸收模型和JBR反应器模型。
2.
In order to control the emission of NO and SO2,experiments on removal of SO2 and NOx by nitric acid are carried out in bench-scale bubbling reactor.
为了控制NO和SO2的排放,利用小型鼓泡反应器研究硝酸溶液的脱硫脱硝特性。
3.
Experiments on simultaneous removal of SO2 and NOX from simulated flue gas are carried out in bench-scale bubbling reactor in this paper.
本文模拟电厂实际烟气组成,利用小型鼓泡反应器进行亚氯酸钠溶液烟气同时脱硫脱硝实验。
5) bubble column reactor
鼓泡床反应器
1.
The flow behavior,axial liquid mixing and inter-phase mass transfer in bubble column reactor were reviewed.
总结了有关浆态鼓泡床反应器内流动、混合用气液传质特性的研究成果,详细地介绍了鼓泡床反应器内气含率、液速、液体轴向扩散系数、传质系数的测量方法,阐述了鼓泡床反应器性能的主要影响因素,如系统压力、温度、气体表观气速、液体性质及固含率等对流动、液相混合和传质特性的影响,并对鼓泡床反应器的应用前景进行了详述。
2.
Bubble size and velocities rising and descending were measured by dual-tip conductivity probe in a bubble column reactor,which operated with air and water.
5 m的鼓泡床反应器中,当表观气速(ug)为0。
6) bubble column reactor
鼓泡塔反应器
1.
Concentration profile of TA in p-xylene oxidation bubble column reactors;
PX氧化鼓泡塔反应器内的TA浓度分布
2.
A mathematic model coupled mass-transfer and reaction to match bubble column reactor with outside circulation for liquid-phase catalytic oxidation of ethylene was established.
以乙烯氧化生产乙醛的外循环鼓泡塔反应器为对象,建立了传质和反应耦合的数学模型,该模型为刚性常微分方程组,采用Gear算法求解。
3.
Bubble column reactor has its own strong points such as simple structure, low construction and operating cost, good heat transfer property.
鼓泡塔反应器具有结构简单、造价及操作费用低廉、传热性能好等诸多优点。
补充资料：鼓泡床反应器控制
分子式：
CAS号：
性质：除对床内压力、气液相原料流量、床内液位等进行控制外，鼓泡床反应器的主要控制指标是床内液相温度分布，控制手段为自下而上的多组换热器冷却剂流量。如果冷却剂流量不稳定，采用反应温度与冷却剂流量的串级调节方案。
CAS号：
性质：除对床内压力、气液相原料流量、床内液位等进行控制外，鼓泡床反应器的主要控制指标是床内液相温度分布，控制手段为自下而上的多组换热器冷却剂流量。如果冷却剂流量不稳定，采用反应温度与冷却剂流量的串级调节方案。
说明：补充资料仅用于学习参考，请勿用于其它任何用途。
参考词条