The evaluation of catalytic pyrolysis catalyst using Daqing vacuum gas oil as feed stock was carried out on a heavy oil micro reactor.
采用重油微反应装置，以大庆蜡油为原料对催化裂解催化剂进行了反应评价。
Etherification activities of various molecular sieve catalysts were investigated with FCC light ends as feedstock carrying on a fixed bed micro reactor.
以炼油厂催化裂化汽油轻馏分为原料，在固定床微型反应器中对几种分子筛催化剂的醚化活性进行了考察。
The reaction ability and products' distribution of catalytic pyrolysis of Daqing vacuum gas oil (VGO) were investigated by using heavy oil micro reactor.
采用重油微反装置考察了大庆蜡油催化裂解反应的主要产物随反应温度的变化规律。
A set of impulse micro reactor chromatogram system was established in order to explore endothermic fuel's coking performance and coking inhibitor's effect.
建立了一套脉冲微型反应色谱系统，用以研究吸热型碳氢燃料结焦性能和结焦抑制剂效果。
The effects of reaction temperature, space velocity, molar ratio of water to methanol, and reaction time on the performance of the micro reactor were investigated.
试验研究分析了反应温度、进料速度、水醇比（水和甲醇的物质的量的比）、反应时间对甲醇水蒸气重整制氢微型反应器性能的影响。
Pyrolysis performance of Daqing light diesel was studied with a micro-pulsed reactor and a continuous tubular reactor.
以大庆轻柴油为原料，对比了微型脉冲热解和连续式管式反应器热解的性能。
The micro hollow fiber cell reactor consists of silica gel tube of permeable silica gel material, permeable silica gel stopper and hollow fiber filament.
本发明公开了一种微型细胞中空纤维反应器，它是由透气硅胶材料的硅胶管，透气硅胶塞和中空纤维丝组成。
Method Build bio-reactor and three-dimensional structure of the stent making use of advanced manufacturing methods of rapid prototyping technology and micro-stamping technology.
方法利用先进制造方法中的快速成型技术和微压印技术构建生物反应器和三维支架结构；
A biological activated carbon membrane reactor (BACMR) was studied for treating micro-polluted water through lab and spot experiments for a process developing of micro-polluted water treatment.
为了开发低温环境下微污染水源水净化工艺，本课题通过实验室试验和现场试验，开展了膜-生物活性炭反应器净化微污染水源水的研究。
An integrated wastewater treatment equipment incorporating micro-electrolysis technology is designed, the continuous flow of sewage in reactor as a pilot apparatus is realized.
设计出一套包含微电解等数种废水处理工艺的一体化废水处理装置，达到了中试规模，实现了废水的连续流。
The thermal stability ofthe crystal structure of modified USY zeolite is increased, and n-hexane cracking activity ina pulse micro-reactor is decreased, while the olefin selectivity is increased.
改性后超稳Y型分子筛的晶体结构热稳定性增加，脉冲微反试验的正已烷裂解活性下降而烯烃选择性得到提高。
The major feature of Submerged Circulative impinging Steam Reactor (SCISR) is significantly promoted micro-mixing in the impinging zone.
浸没循环撞击流反应器(SCISR)的主要特点是撞击区能显著强化微观混合。
The deactivation kinetics for the vapor-phase disproportionation of toluene over mordenite catalyst has been studied by using a combined unit of micro-reactor under pressure and gas chromatography.
本文采用加压微反-包谱-数据处理机联合装置研究了在丝光沸石催化剂上甲苯歧化反应的失活动力学。
The catalytic activities and ageing resistant performance of above catalysts for methane combustion was evaluated in a continuous-flow micro-reactor.
利用连续流动微型反应装置研究了催化剂的反应性能，抗老化性能及反应条件对反应性能的影响。
These catalysts were characterized, and evaluated in acetylene selective hydrogenation with an atmospheric micro-reactor.
表征了催化剂，并考察催化剂的乙炔选择性加氢性能。
The micro-whirling reactor and its working mechanism which is whirling-coagulation and contact-flocculation are illustrated.
介绍了微涡流混凝工艺的核心-涡流反应器的特点及其微涡流凝聚与立体接触絮凝的混凝反应机理。
Micro-channel reactor is a 3-dimensional structure unit used for chemical reaction in fuel cell, manufactured through special micro-processing of solid matrix.
微通道反应器，是一种借助特殊微加工技术以固体基质制造的可用于进行化学反应的三维结构单元。
This paper studied the alkylation of cumene on fixed bed micro-reactor to discuss the effect of product diffusion.
本论文在固定床微反装置上，考察扩散效应对异丙苯烷基化反应产物中异构体组成的影响。
The hydrotreating performance of catalysts was also examined in a fixed-bed continuous-flow micro-reactor, using CGO from the Liaohe Oilfield as feedstock.
用固定床连续流动微反装置，以辽河焦化蜡油为反应原料，考察了催化剂的加氢精制性能。
The hydrotreating performance of catalysts was also examined in a fixed-bed continuous-flow micro-reactor, using CGO from the Liaohe Oilfield as feedstock.
用固定床连续流动微反装置，以辽河焦化蜡油为反应原料，考察了催化剂的加氢精制性能。
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