对连续催化重整反应器结焦含量软测量问题进行研究。
In this paper soft sensing on coking models of reactor in the process of continuous catalytic reforming is studied.
介绍了金陵分公司炼油厂重整反应器约翰逊外网的损坏情况及造成的危害。
The failure situation and caused damage of Johnson outer meshes reforming reactor for Jinling company refinery were recommended.
基于炭催化剂特性、原料气组成和重整转化反应器的尺寸参数，建立了重整反应器体系的物料平衡和热平衡方程；
Based on the properties of carbonaceous catalyst, composition of feed gas and the size parameters of reforming reactor, heat and material balance of reactor were established.
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。
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.
考察了催化剂涂层的配比、反应温度、水醇比、进料速度、反应时间对甲醇重整微槽道反应器性能的影响。
The effects of catalyst composition, reaction temperature, space velocity, molar ratio of methanol to water, and reaction time on the performance of the microchannel reactor were investigated.
本文介绍了生物油水蒸气催化重整反应机理与热力学分析，介绍了催化重整制氢过程催化剂、制氢工艺条件、代表性的反应器及工艺流程。
In this paper, some typical reactor designs, process engineering, operation conditions, catalyst, reaction mechanism, and thermal analysis of catalytic steam reforming of bio-oil are presented.
重整装置的核心反应主要是在四个反应器中进行，每一个反应器的正常运行都与产品质量的稳定密切相关。
The main Restructuring of the core reactor is carried out in four. the normal operation of a reactor are closely related to the stability and product quality.
第一和第二反应器中催化剂积炭量明显增高是重整进料携带重组分的特征之一。
The obvious coke increase on the catalysts in the 1 st and 2 nd reactors was one of the characteristics of feedstock having heavy com...
并针对形状不规则炭催化剂粒度分布的特点，研究了重整转化反应器内流体阻力特性。
Because of irregular carbonaceous catalyst with size distribution, the fluid resistance in reforming reactor has been studied.
相应推导出了径向反应器和轴向反应器的微分方程组，为重整反应过程计算机模拟提供了理论依据。
Differential equations of both reactors were deduced correspondently. These supply theoretical basis for computer simulation of reforming.
相应推导出了径向反应器和轴向反应器的微分方程组，为重整反应过程计算机模拟提供了理论依据。
Differential equations of both reactors were deduced correspondently. These supply theoretical basis for computer simulation of reforming.
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