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Selection of mass transfer devices for absorption concentration of hydrogen-containing gas (HCG) in catalytic reforming units

https://doi.org/10.31660/0445-0108-2026-2-89-103

EDN: HVCWRS

Abstract

This article examines the pressing issue of improving the efficiency of semi-regenerative catalytic reforming units by increasing the cycle length between catalyst regenerations. This work also considers the possibility of using absorption purification of hydrogen-containing gas to remove hydrocarbons to minimize coke deposition on the catalyst surface. This article aims to prove the feasibility of absorption concentration within the unit and to achieve a target hydrogen gas concentration of up to 98 % in the circulating stream. The tasks involve analysis of packed contact devices and development of recommendations for their selection for this process. To solve these tasks, the authors employ a combination of calculation and analytical methods. These methods include evaluating different packing types, technological and hydraulic calculations to determine the geometric parameters of packed beds. The work compares several structured and random packing types that differ in size, material, and numerical values of key characteristics – specific surface area, and void fraction. Based on a parametric analysis performed, the authors identify a correlation between the performance of contact devices and the geometric characteristics of absorption columns. This correlation can support predictive selection of suitable packings. On this basis, the article proposes a methodological approach for comparative analysis and selection of packings based on specific mass transfer conditions, and a criterion for evaluating their applicability. In order to achieve these objectives, the authors select two most efficient types of packing that meet the process requirements. The selection considers geometric constraints, the minimization of packing volume, and the proposed applicability coefficient. This approach aids in reducing coke formation and increasing the catalyst cycle length between regenerations.

About the Authors

L. V. Taranova
Industrial University of Tyumen
Russian Federation

Lyubov V. Taranova - Candidate of Engineering Sciences, Associate Professor at the Department of Oil and Gas Processing.

Tyumen



V. S. Sergeev
Industrial University of Tyumen
Russian Federation

Vadim S. Sergeev – Student.

Tyumen



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Review

For citations:


Taranova L.V., Sergeev V.S. Selection of mass transfer devices for absorption concentration of hydrogen-containing gas (HCG) in catalytic reforming units. Oil and Gas Studies. 2026;(2):89-103. (In Russ.) https://doi.org/10.31660/0445-0108-2026-2-89-103. EDN: HVCWRS

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ISSN 0445-0108 (Print)
ISSN 3033-8174 (Online)