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Deep oxidation of toluene on glass fiber catalysts in structured cartridges of various geometries 玻璃纤维催化剂在不同几何形状的结构筒中对甲苯的深度氧化
Pub Date : 2024-07-18 DOI: 10.18412/1816-0387-2024-4-25-34
D. V. Baranov, A. Elyshev, S. A. Lopatin, A. Zagoruiko
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引用次数: 0
Research of the Process of Producing Nitrous Oxide in a Microstructured Slit-type Reactor 在微结构狭缝型反应器中生产一氧化二氮的工艺研究
Pub Date : 2024-07-18 DOI: 10.18412/1816-0387-2024-4-94-108
A. Sheboltasov, N. Vernikovskaya, V. A. Chumachenko
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引用次数: 0
Improvement of mathematical model for catalytic reforming process with a stationary catalyst layer 带固定催化剂层的催化重整过程数学模型的改进
Pub Date : 2024-07-18 DOI: 10.18412/1816-0387-2024-4-78-93
I. V. Pchelintseva, E. N. Ivashkina, E. S. Chernyakova, D. B. Tazhmulikov, V. A. Chuzlov
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引用次数: 0
Block catalysts, based on Ce and Mn oxides and cordierite ceramics, for ozone decomposition 用于臭氧分解的基于铈和锰氧化物以及堇青石陶瓷的嵌段催化剂
Pub Date : 2024-07-18 DOI: 10.18412/1816-0387-2024-4-16-24
M. Chernykh, G. Mamontov
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引用次数: 0
Kinetic model for selective trimerization of ethylene to hexene-1 on chromium-pyrrole catalyst 铬-吡咯催化剂上乙烯向己烯-1 选择性三聚反应的动力学模型
Pub Date : 2024-07-18 DOI: 10.18412/1816-0387-2024-4-65-77
P. I. Kulchakovsky, V. S. Ermolaev, S. L. Saratovskikh, E. E. Faingold, I. V. Sedov, A. A. Biktimirov, D. A. Lenev
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引用次数: 0
Heterogeneous hydrogenation and isomerization of carbocyclic compounds of the norbornene series (review) 降冰片烯系列碳环化合物的异相氢化和异构化(综述)
Pub Date : 2024-07-18 DOI: 10.18412/1816-0387-2024-4-35-59
V. V. Zamalyutin, E. V. Okuneva, S. S. Moskvichev, V. Flid
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引用次数: 0
Influence of the Fe/Cr ratio on the catalytic activity of FeCr/C catalysts in the process of oxidative dehydrogenation of ethane 乙烷氧化脱氢过程中铁/铬比例对 FeCr/C 催化剂催化活性的影响
Pub Date : 2024-07-18 DOI: 10.18412/1816-0387-2024-4-60-64
I. I. Mishanin, T. V. Bogdan, T. V. Fedoseev, M. A. Skiba, P. A. Chernavsky, A. E. Koklin, K. I. Maslakov, V. I. Bogdan
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引用次数: 0
Analysis of the macrokinetics of CO2 sorption on a 10% NaNO3/MgO sorbent and modeling of an adsorber with a hydrogen productivity of 10 kg/h 二氧化碳在 10% NaNO3/MgO 吸附剂上吸附的宏观动力学分析以及制氢率为 10 公斤/小时的吸附器模型制作
Pub Date : 2024-07-17 DOI: 10.18412/1816-0387-2024-4-4-15
A. B. Shigarov, I. E. Nikulina, V. Pakharukova, D. Potemkin
The work proposed a macrokinetic model of first-order CO2 sorption on a 10 mol.% NaNO3/MgO sorbent. Based on the analysis of experimental gravimetric data, the maximum sorption capacity of the sorbent 10 mol.% NaNO3/MgO was determined, which does not depend on the partial pressure of CO2 and at 320 °C is 159% (based on the initial mass of the sample), or 13.4 mmol CO2/ gsorb. The calculated value of the sorption constant kads at temperatures of 280-320 °C and a partial pressure of CO2 of 0.50-0.75 atm is 0.017 min-1 atm-1. Based on the obtained kinetics, a simulation of an adiabatic and isothermal CO2 adsorber was made within the framework of a technological scheme for producing hydrogen 10 kg/h from natural gas at an operating pressure of 12 atm. During the calculations, it was shown that for the effective functioning of the adsorber, intensive removal of the heat released during the sorption process is necessary. This allows CO2 sorption to be carried out for 30 minutes at a temperature of 300 °C and a volumetric flow rate GHSV = 1170 h-1, while the concentration of CO2 at the outlet in dry gas does not exceed 1.5 mol.%.
该研究提出了 10 mol.% NaNO3/MgO 吸附剂对二氧化碳一阶吸附的宏观动力学模型。根据对实验重量数据的分析,确定了 10 mol.% NaNO3/MgO 吸附剂的最大吸附容量,该容量与二氧化碳分压无关,在 320 °C 时为 159%(基于样品的初始质量),即 13.4 mmol CO2/ gsorb。在温度为 280-320 °C 和二氧化碳分压为 0.50-0.75 atm-1 时,吸附常数 kads 的计算值为 0.017 min-1 atm-1。根据所获得的动力学原理,对绝热和等温二氧化碳吸附器进行了模拟,模拟的技术方案是在 12 个大气压的工作压力下,利用天然气生产每小时 10 公斤的氢气。计算结果表明,为了使吸附器有效运行,必须大量去除吸附过程中释放的热量。这使得二氧化碳吸附可以在 300 °C 的温度和 GHSV = 1170 h-1 的容积流量条件下进行 30 分钟,而干气出口处的二氧化碳浓度不超过 1.5 摩尔%。
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引用次数: 0
The use of microalgae biomass for the production of marketable products. Part 5. Jet fuel from microalgae biomass 利用微藻生物质生产适销产品。第 5 部分。微藻生物质喷气燃料
Pub Date : 2024-03-20 DOI: 10.18412/1816-0387-2024-2-66-75
Y. V. Samoylova, K. N. Sorokina, V. N. Parmon
Boreskov Institute of Catalysis, Novosibirsk, RussiaThe review focuses on jet fuel from microalgae biomass. Modern standards that biojet fuel obtained from microalgae biomass must meet are presented. The main ways of producing jet fuel from microalgae are considered, namely the processes of “oil to fuel”, “gas to fuel” and “carbohydrates to fuel”, as well as the production of this fuel along with other valuable products as a result of complex bioprocessing of biomass. Data on the potential for using biofuels from microalgae biomass in mixtures with traditional petroleum fuels are presented. The prospects for using this alternative fuel in modern aviation are considered.
俄罗斯新西伯利亚 Boreskov 催化研究所 这篇综述的重点是微藻生物质喷气燃料。介绍了从微藻生物质中提取的生物喷气燃料必须达到的现代标准。文章考虑了利用微藻生产喷气燃料的主要方法,即 "油变燃料"、"气变燃料 "和 "碳水化合物变燃料 "的过程,以及通过对生物质进行复杂的生物加工生产这种燃料和其他有价值的产品。报告还提供了有关将微藻生物质制成的生物燃料与传统石油燃料混合使用的潜力数据。还考虑了在现代航空中使用这种替代燃料的前景。
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引用次数: 0
Oxidative chlorination of hydrocarbons. Part 2. Oxidative chlorination of propylene, 1,3-butadiene, acetylene and benzene 碳氢化合物的氧化氯化。第 2 部分。丙烯、1,3-丁二烯、乙炔和苯的氧化氯化反应
Pub Date : 2024-03-20 DOI: 10.18412/1816-0387-2024-2-15-25
M. Flid
The review paper considers main regularities of the oxidative chlorination of some unsaturated hydrocarbons: propylene, acetylene, butadiene-1,3 and benzene. It was shown that the implementation of such processes in the gas phase requires the presence of heterogeneous catalysts based on copper or palladium in the system. Depending on the process conditions, the products of additive or substitutive chlorination are formed. Kinetic equations and probable conversion mechanisms were proposed for the oxidative chlorination of propylene, acetylene and benzene. Prospects of the practical implementation of the oxidative chlorination of some unsaturated hydrocarbons were considered.
这篇综述论文探讨了一些不饱和碳氢化合物(丙烯、乙炔、丁二烯-1,3 和苯)氧化氯化的主要规律。研究表明,在气相中实施此类工艺需要在系统中加入基于铜或钯的异相催化剂。根据工艺条件的不同,会形成添加型或替代型氯化产物。针对丙烯、乙炔和苯的氧化氯化提出了动力学方程和可能的转化机制。考虑了一些不饱和碳氢化合物氧化氯化的实际应用前景。
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引用次数: 0
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Kataliz v promyshlennosti
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