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In this paper, one dimension homogeneous model was used to analyze globally the multiplicity, stability and operable regions of counter current reactor in which an order simple irreversible highly exothermal reaction is conducted.

本文应用一维均相模型对进行一级简单不可逆强放热反应的间壁冷却管式反应器在冷却介质逆流流动时的多态、稳定性和可操作域进行全局分析。

The deep knowledge repository of temperature profile was yielded based on the determinant mathematical model, which increased the 'extrapolative ability' and 'reliability'. Simulation results have proved that the model presented in this paper is simple, and can satisfy the control requirements.In order to predict and control, A real-time prognosticate model of temperature profile for a reverse flow reactor was built based on dynamic RBFNN with online correcting model parameters.

5基于改进的RBFNN的非线性内模控制策略充分利用神经网络的自学习及非线性逼近能力,建立流向变换反应器的动态模型和逆模型,非线性内模控制器由逆模型和带有一个调节参数的鲁棒滤波器组成,并采用递推最小二乘在线校正模型参数,仿真结果验证了此控制方案的有效性。

The main metabolites in each reactor were detected by UV/VIS, infrared and high performance liquid chromatography and mass spectrometry. Probably, the mother dye molecule facultatively hydrolyzed to produce 1-NH2-2-hydroxy anthraquinon, OH-substituted anthraquinon and 3,4-dihydroxy-benzonic acid.

对各反应器中主要的代谢产物分别进行紫外-可见、红外和高效液相色-质联谱仪检测分析后发现,母体染料经兼氧水解首先生成1-氨基-2-羟基蒽醌以及还原态的—OH基取代蒽醌隐色体,进一步水解生成3,4-二羟基苯甲酸。

It is very difficult to directly research the shape of the high temperature fluidal free surface in the metallurgical reactor.

直接研究冶金反应器内高温流体的自由表面形状是比较困难的。

Ethylene glycol process is a long process, which includes more than ten fractionating columns and fixed-bed catalytic reactor.

乙二醇生产流程是一个包含十几个精馏塔和固定床催化反应器的长流程。

The company occupies over 18,000 square meters, the existing set of high-performance vacuum fractionating tower, a high-performance gas chromatograph devices, many sets of reactor, high temperature oil, one Taiwan.

公司占地18000多平方米,现有一套高效减压分馏塔,一套高效气相色谱仪装置,反应罐多套,高温油锅一台。

Supported noble metallic catalysts were prepared with different kind of noble metals and of supports,their catalytic performance for furoic acid hydrogenation were investigated in fixed bed micro-reactor in water under different conditions such as reaction pressure,temperature,H2 space velocity,space velocity of furoic acid and solvent and so on.

采用水作溶剂的固定床操作系统,用钌、铑、钯、铂等作为担载金属,氧化硅、活性炭、γ-三氧化二铝等作为载体,制备了多种负载型催化剂,评价了它们的糠酸选择性杂环加氢催化性能。

The hydrogenation and methyl esterification of furoic acid over Pd/γ-Al2O3 catalysts was investigated in fixed bed micro-reactor by one-step method.

采用连续流动固定床微反应器,以糠酸、甲醇、氢气为原料,Pd/γ-Al2O3为催化剂,使糠酸一步加氢甲醋化生成α-四氢糠酸甲酯。

The hydrogenation and methyl esterification of furoic acid over Pd-Ni/γ-Al2O3 catalysts was investigated in fixed bed micro-reactor under different conditions such as reaction temperature,pressure,H2 space velocity,space velocity of furoic acid and methol,ratio of H2 and furoic acid and so on.

以糠酸、甲醇、氢气为原料,采用连续流动固定床微反应器,Pd-Ni/γ-Al2O3为催化剂,使糠酸一步加氢甲酯化生成α-四氢糠酸甲酯。

The hydrogenation and methyl esterification of furoic acid over Pd-Ni/γ-Al2O3 catalysts was investigated in fixed bed micro-reactor under different conditions such as reaction temperature,pressure,H2 space velocity,space velocity of furoic acid and methol,ratio of H2 and furoic acid and so on.

以糠酸、甲醇、氢气为原料,采用连续流动固定床微反应器,Pd-Ni/γ-Al2O3为催化剂,使糠酸一步加氢甲酯化生成α-四氢糠酸甲酯。研究了反应的温度,压力,气、液体流速,进料流量等因素对催化反应的影响。结果表明:在1.5MPa,250℃,氢气空速3300 h-1,液体空速3.0 h-1(氢油比为50)时,糠酸转化率为96.6%,四氢糠酸甲酯的选择性97.2.0%,产率94.0%。催化剂稳定性较好,连续运转280小时后未见活性下降。该反应体系活性高,选择性好,反应压力低,催化剂性能稳定,操作简单,产物易分离

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好消息是,从指挥线后格式化了FAT32(格式/曾荫权:了FAT32/答:4096年径:)所有问题,但其中的游戏测试工作,我很好。

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