The efficiencies of photocatalytic degradation of orthocresol increased than the reactor with glass tube as support.
不仅克服了悬浮相光催化剂的缺点，而且便于改进和放大后应用于工业废水处理。
As a catalyst reactor coverage tower packing materials and support, the major role is to increase the distribution of gas or liquid, support and protect the intensity of low strength activity catalyst.
广泛用于石油、化工、化肥、天然气及环保等行业，作为反应器内催化剂的支撑材料和塔填料，其主要作用是支撑和保护强度不高的活性催化剂，增加气体或液体分布点。
So the indoor limiting reactor or 35kV switch cabinet can be connected in the high voltage chamber, the related support, fittings and civil work can be reduced.
由于母线跨距大，可直接进入高压室与户内限流电抗器或35千伏开关柜连接，减少了相应的母线支撑点、母线金具、以及土建构架基础。
The thesis takes the reactor vessels in China Experiment Fast Reactor as the research object, according to the ASME code, the nuclear power earthquake code etc. relevant nuclear safety guidelines and regulation codes, complete the safe function evaluation of mechanics of the reactor vessels in CEFR under the all conditions that various proper loads and the different load from the outside, complete the stress intensity calculation with assess of the main vessel and the guard vessel and the support skirt in CEFR except for the creep and fatigue analysis.
论文以中国实验快堆堆容器为研究对象，按照ASME规范、核电厂抗震设计规范等有关的核安全法规和规范，完成了中国实验快堆主容器、保护容器和堆容器支承裙在各种工况各种载荷组合作用下的除高温蠕变疲劳分析以外的一次和二次应力强度的计算、分析与评价。
International Thermonuclear Experimental Reactor gravity support system; finite element; cyclic symmetry; thermal analysis; coupling analysis
ITER重力支撑系统；有限元；周期对称性；热分析；耦合分析
The honeycomb support in the bioreactor demonstrated strong ability to attach bacteria, which promoted the maintenance of the special culture in the reactor and realization of bioaugmentation.
反应器内蜂窝陶瓷载体对微生物具有良好的固定化作用，进行生物强化时，有利于高效菌在反应器内的保持和强化效果的实现。
Numerical simulation of temperature field of pump support cooling system for China experimental fast reactor
中国实验快堆泵支承冷却系统温度场分析
Corrosion of the weldments for China experimental fast reactor main vessel and its neck support in high temperature sodium and sodium vapour
中国实验快堆主容器母材及其颈部支撑焊接件在高温钠及钠蒸气中的腐蚀
In this paper hydrogen exchange reaction between hydrogen and liquid water was performed successfully using hydrophobic resin of D type as support and Pt as active component. The kinetic equation in a concurrent flow reactor was discussed.
本文用憎水性D型树脂为载体，铂为活性组分，使氢-液体水之间成功地进行了氢同位素的交换反应，讨论了并流反应器的动力学方程。
The summary includes stress analyses and evaluations of internal support structure, core support structure, reactor thermal shield, etc.
主要构件包括堆内支承结构、堆芯支承结构、堆内热屏蔽等7类设备。
It was indicated that, support carriers could expand the activity scope of hydrogen production bacteria, make the system fairly stable in response to organic load impact and low pH value (pH < 3.8), and maintain high biomass concentration in the reactor at low HRT.
研究表明，投加生物载体能够扩大产氢细菌的活性范围，提高系统的抗冲击负荷能力和耐低pH值的能力，增加系统稳定性，并且可使系统在低HRT下保持较高的生物量。
Dealcoholization temperature markedly influences the surface area and porosity of the resultant MAO-supports. When the support was pretreated at lower or higher temperature, the corresponding MAO-support shows very low surface area; 2.XRD and IR analyses indicate that MAO has reacted with the residual ethanol in the supports, which is an important manner to get MAO fixed on the carrier. Morever, XPS analyse indicates that MAO can also be coordinated with MgCl_2, which is another way to get MAO fixed on the support; 3.ICP and EDX analyses indicate that dealcoholization temperature not only determined the element content on the solid catalyst, but also influences the element distribution on the carrier; 4.The activities of the supported phenoxy-imine catalysts and the properties of resultant polymers are strongly dependent on the dealcoholization temperature. The support (MSP-5) obtained by treating MgCl_2·2.56C_2H_5OH at 160℃for 4 h, then modified by MAO is very effective for immobilizing complex 3, the resultant solid catalyst (MSPC-5) shows very high activity in ethylene polymerization, and its kinetics of polymerization is stable during the reaction process. Finally, PEs with spherical morphology and high bulk density (over 0.35g/ml) were obtained, without reactor fouling; 5.In this work, polymerization conditions such as alkylaluminums, Al/Zr ratio, temperature and H_2 had a pronounced effect on the activity of MSPC-5 and properties of PE; (3). New MgCl_2-Supported Single-Site Catalysts for Ethylene PolymerizationIn this work, a kind of new MgCl_2 support was obtained by anhydrous MgCl_2 co-milled with solid MAO, and it is a creative contribution. Then some single-site catalysts were supported on the new MgCl_2 support, and the resulted solid catalysts were tested in ethylene polymerization, the results indicated that:1.XRD and IR analyses indicate that MAO does be coordinated with MgCl_2, which is in good agreement with the results obtained by XPS; 2.co-mlling time had no obvious effect on the texture of support after 12 hours; 3.In this work, MgCl_2 was co-milled with solid MAO for different hours, and then complex 3 was supported on these co-milled supports. It was found that co-milling time markedly influences the activity of solid catalysts, but it had negligible effect on the kinetic profile and the properties of resultant PE.
XPS研究结果表明，MAO不仅仅只和乙醇作用，MAO还与MgCl_2本身有一定的作用，这是一个极为重要的发现；3、通过ICP和EDX表征，发现载体的脱醇温度直接影响着元素在固体催化剂中的含量及分布；4、脱醇温度极大地影响着负载苯氧基亚胺类催化剂的活性和聚合物的性能，特别是原始载体经160℃活化4小时制备得到的固体催化剂MSPC-5的活性明显高于其他脱醇温度条件下制得的固体催化，并且催化剂寿命长，表现出稳定的动力学行为，最终获得了高堆密度(大于0.35g／ml)的球形聚乙烯颗粒；5、本文选择MSPC-5为研究对象，考察了聚合反应参数对催化剂的活性及其聚合物的影响，研究发现：不同的烷基铝对催化剂具有非常重要的影响，特别足TIBA对MSPC-5的助催化活性最高，烷基铝的加入量有一个较佳值，聚合温度为80度时活性最高，H_2的加入使催化剂的活性明显降低且聚合物的分子量也减小；、新型氯化镁载体负载单活性中心催化剂催化乙烯聚合本文创造性采用固体MAO与无水氯化镁直接进行共研磨，制备出了一种的新型的氯化镁载体，并将该载体用于多种单活性中心催化剂的负载化研究，研究表明：1、通过BET、XRD的表征，再次证实了MAO与MgCl_2之间具有直接作用，与XPS的研究结果相一致；2、当研磨时间高于12小时时，延长研磨时间对载体的结构没有显著的影响；3、将配合物3负载于共研磨时间不同的一系列载体上，乙烯聚合结果表明，尽管共研磨时间对负载催化剂的活性具有明显的影响，但是它对聚合物的性能以及催化剂的影响不明显。
Dealcoholization temperature markedly influences the surface area and porosity of the resultant MAO-supports. When the support was pretreated at lower or higher temperature, the corresponding MAO-support shows very low surface area; 2.XRD and IR analyses indicate that MAO has reacted with the residual ethanol in the supports, which is an important manner to get MAO fixed on the carrier. Morever, XPS analyse indicates that MAO can also be coordinated with MgCl_2, which is another way to get MAO fixed on the support; 3.ICP and EDX analyses indicate that dealcoholization temperature not only determined the element content on the solid catalyst, but also influences the element distribution on the carrier; 4.The activities of the supported phenoxy-imine catalysts and the properties of resultant polymers are strongly dependent on the dealcoholization temperature. The support (MSP-5) obtained by treating MgCl_2·2.56C_2H_5OH at 160℃for 4 h, then modified by MAO is very effective for immobilizing complex 3, the resultant solid catalyst (MSPC-5) shows very high activity in ethylene polymerization, and its kinetics of polymerization is stable during the reaction process. Finally, PEs with spherical morphology and high bulk density (over 0.35g/ml) were obtained, without reactor fouling; 5.In this work, polymerization conditions such as alkylaluminums, Al/Zr ratio, temperature and H_2 had a pronounced effect on the activity of MSPC-5 and properties of PE; (3). New MgCl_2-Supported Single-Site Catalysts for Ethylene Polymerization In this work, a kind of new MgCl_2 support was obtained by anhydrous MgCl_2 co-milled with solid MAO, and it is a creative contribution. Then some single-site catalysts were supported on the new MgCl_2 support, and the resulted solid catalysts were tested in ethylene polymerization, the results indicated that: 1.XRD and IR analyses indicate that MAO does be coordinated with MgCl_2, which is in good agreement with the results obtained by XPS; 2.co-mlling time had no obvious effect on the texture of support after 12 hours; 3.In this work, MgCl_2 was co-milled with solid MAO for different hours, and then complex 3 was supported on these co-milled supports. It was found that co-milling time markedly influences the activity of solid catalysts, but it had negligible effect on the kinetic profile and the properties of resultant PE.
XPS研究结果表明，MAO不仅仅只和乙醇作用，MAO还与MgCl_2本身有一定的作用，这是一个极为重要的发现； 3、通过ICP和EDX表征，发现载体的脱醇温度直接影响着元素在固体催化剂中的含量及分布； 4、脱醇温度极大地影响着负载苯氧基亚胺类催化剂的活性和聚合物的性能，特别是原始载体经160℃活化4小时制备得到的固体催化剂MSPC-5的活性明显高于其他脱醇温度条件下制得的固体催化，并且催化剂寿命长，表现出稳定的动力学行为，最终获得了高堆密度(大于0.35g／ml)的球形聚乙烯颗粒； 5、本文选择MSPC-5为研究对象，考察了聚合反应参数对催化剂的活性及其聚合物的影响，研究发现：不同的烷基铝对催化剂具有非常重要的影响，特别足TIBA对MSPC-5的助催化活性最高，烷基铝的加入量有一个较佳值，聚合温度为80度时活性最高，H_2的加入使催化剂的活性明显降低且聚合物的分子量也减小；、新型氯化镁载体负载单活性中心催化剂催化乙烯聚合本文创造性采用固体MAO与无水氯化镁直接进行共研磨，制备出了一种的新型的氯化镁载体，并将该载体用于多种单活性中心催化剂的负载化研究，研究表明：1、通过BET、XRD的表征，再次证实了MAO与MgCl_2之间具有直接作用，与XPS的研究结果相一致； 2、当研磨时间高于12小时时，延长研磨时间对载体的结构没有显著的影响； 3、将配合物3负载于共研磨时间不同的一系列载体上，乙烯聚合结果表明，尽管共研磨时间对负载催化剂的活性具有明显的影响，但是它对聚合物的性能以及催化剂的影响不明显。
The monolith catalytic reactor whose catalyst support is monolith structure has much higher surface area per unit volume of the bed, which guarantees a good heat transfer throughout the reactor.
在整体式催化反应器中，整体式并具有规整结构的催化剂载体每单位体积的外表面积大，能保证反应器中良好的传热。
On the other hand, the metallic honeycomb support with micro-channel not only can improve the mechanical strength of the catalyst, but can compact the reactor volume.
另外，微通道的金属整体式载体不仅可以提高催化剂载体的机械强度，还可以实现反应器的小型化，但其核心问题是载体与催化剂的粘附强度问题。
Internal airlift loop with cells immobilized onto ceramic honeycomb support (IAL-CHS) reactor was used for ammonia nitrogen removal aiming at polluted urban surface water, and results showed that ammonia nitrogen in the water could be removed effectively.
针对受污染的城市地表水，采用新型蜂窝陶瓷载体气升式内循环反应器（IAL-CHS）对其中的氨氮去除进行研究。结果表明，该生物膜反应器能有效地去除地表水中的氨氮。
Internal airlift loop with ceramic honeycomb support (IAL-CHS) reactor was respectively used for degradation of 2, 4-DCP by Achromobacter sp. and treatment of brewery wastewater by complex microorganisms.
利用IAL-CHS反应器分别吸附单一的微生物Achromobactersp.来降解2,4-二氯酚（2,4-DCP）和吸附复合微生物菌群来处理啤酒废水。
This paper introduces the major procedures and results of scaling-up design of commercial mechanically stirred reactor with the support of cool-model experiment in stirred tank.
通过冷模实验为机械搅拌反应釜的工业放大设计提供补充性依据及工业搅拌釜的放大设计的主要过程及结果。
The existing problems of shell side structure for domestic current tubular fixed bed reactor are discussed and evaluated. The improvement of shell side structure by adopting outside flow deflector type inlet and outlet structure and adopting baffle rod to support reaction tube are proposed.
探讨和评介了国内现行列管式固定床反应器的壳程结构存在的问题，提出壳程采用外导流筒式进、出口结构和采用折流杆支撑反应管的结构改进措施。
The finite element method is applied to analysis and optimize the design of the hydrogenation reactor skirt support area, and stress of the risk section is assessed and strength is checked.
采用有限元法对加氢反应器裙座支撑区进行有限元分析及优化设计，并对其危险截面作应力评定和强度校核。