<?xml version="1.0" encoding="UTF-8"?>
<!DOCTYPE article PUBLIC "-//NLM//DTD JATS (Z39.96) Journal Publishing DTD v1.3 20210610//EN" "JATS-journalpublishing1-3.dtd">
<article article-type="research-article" dtd-version="1.3" xmlns:mml="http://www.w3.org/1998/Math/MathML" xmlns:xlink="http://www.w3.org/1999/xlink" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xml:lang="ru"><front><journal-meta><journal-id journal-id-type="publisher-id">catal</journal-id><journal-title-group><journal-title xml:lang="ru">Катализ в промышленности</journal-title><trans-title-group xml:lang="en"><trans-title>Kataliz v promyshlennosti</trans-title></trans-title-group></journal-title-group><issn pub-type="ppub">1816-0387</issn><issn pub-type="epub">2413-6476</issn><publisher><publisher-name>LLC "KALVIS"</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.18412/1816-0387-2023-6-70-79</article-id><article-id custom-type="elpub" pub-id-type="custom">catal-978</article-id><article-categories><subj-group subj-group-type="heading"><subject>Research Article</subject></subj-group><subj-group subj-group-type="section-heading" xml:lang="ru"><subject>КАТАЛИЗ В НЕФТЕПЕРЕРАБАТЫВАЮЩЕЙ ПРОМЫШЛЕННОСТИ</subject></subj-group><subj-group subj-group-type="section-heading" xml:lang="en"><subject>СATALYSIS IN PETROLEUM REFINING INDUSTRY</subject></subj-group></article-categories><title-group><article-title>Защита катализаторов гидроочистки нефтяных фракций от механических примесей: экспериментальные исследования и расчет</article-title><trans-title-group xml:lang="en"><trans-title>Guard of hydrotreating catalysts of oil fractions from solid particulates: experimental studies and calculation</trans-title></trans-title-group></title-group><contrib-group><contrib contrib-type="author" corresp="yes"><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Мик</surname><given-names>И. А.</given-names></name><name name-style="western" xml:lang="en"><surname>Mik</surname><given-names>I. A.</given-names></name></name-alternatives><email xlink:type="simple">ctls@kalvis.ru</email><xref ref-type="aff" rid="aff-1"/></contrib><contrib contrib-type="author" corresp="yes"><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Кленов</surname><given-names>О. П.</given-names></name><name name-style="western" xml:lang="en"><surname>Klenov</surname><given-names>O. P.</given-names></name></name-alternatives><email xlink:type="simple">ctls@kalvis.ru</email><xref ref-type="aff" rid="aff-1"/></contrib><contrib contrib-type="author" corresp="yes"><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Казаков</surname><given-names>M. O.</given-names></name><name name-style="western" xml:lang="en"><surname>Kazakov</surname><given-names>M. O.</given-names></name></name-alternatives><email xlink:type="simple">ctls@kalvis.ru</email><xref ref-type="aff" rid="aff-1"/></contrib><contrib contrib-type="author" corresp="yes"><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Надеина</surname><given-names>К. А.</given-names></name><name name-style="western" xml:lang="en"><surname>Nadeina</surname><given-names>K. A.</given-names></name></name-alternatives><email xlink:type="simple">ctls@kalvis.ru</email><xref ref-type="aff" rid="aff-1"/></contrib><contrib contrib-type="author" corresp="yes"><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Климов</surname><given-names>О. В.</given-names></name><name name-style="western" xml:lang="en"><surname>Klimov</surname><given-names>O. V.</given-names></name></name-alternatives><email xlink:type="simple">ctls@kalvis.ru</email><xref ref-type="aff" rid="aff-1"/></contrib><contrib contrib-type="author" corresp="yes"><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Решетников</surname><given-names>С. И.</given-names></name><name name-style="western" xml:lang="en"><surname>Reshetnikov</surname><given-names>S. I.</given-names></name></name-alternatives><email xlink:type="simple">ctls@kalvis.ru</email><xref ref-type="aff" rid="aff-1"/></contrib><contrib contrib-type="author" corresp="yes"><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Носков</surname><given-names>А. С.</given-names></name><name name-style="western" xml:lang="en"><surname>Noskov</surname><given-names>A. S.</given-names></name></name-alternatives><email xlink:type="simple">ctls@kalvis.ru</email><xref ref-type="aff" rid="aff-1"/></contrib></contrib-group><aff-alternatives id="aff-1"><aff xml:lang="ru"><institution>Институт катализа им. Г.К. Борескова СО РАН, Новосибирск</institution><country>Россия</country></aff><aff xml:lang="en"><institution>Boreskov Institute of Catalysis SB RAS, Novosibirsk</institution><country>Russian Federation</country></aff></aff-alternatives><pub-date pub-type="collection"><year>2023</year></pub-date><pub-date pub-type="epub"><day>23</day><month>11</month><year>2023</year></pub-date><volume>23</volume><issue>6</issue><fpage>70</fpage><lpage>79</lpage><permissions><copyright-statement>Copyright &amp;#x00A9; LLC "KALVIS", 2023</copyright-statement><copyright-year>2023</copyright-year><copyright-holder xml:lang="ru">LLC "KALVIS"</copyright-holder><copyright-holder xml:lang="en">LLC "KALVIS"</copyright-holder><license xlink:href="https://www.catalysis-kalvis.ru/jour/about/submissions#copyrightNotice" xlink:type="simple"><license-p>https://www.catalysis-kalvis.ru/jour/about/submissions#copyrightNotice</license-p></license></permissions><self-uri xlink:href="https://www.catalysis-kalvis.ru/jour/article/view/978">https://www.catalysis-kalvis.ru/jour/article/view/978</self-uri><abstract><p>Проведено исследование эффективности улавливания микрочастиц механических примесей, содержащихся в дизельном топливе, для пакетной загрузки катализаторов – аналога промышленного пакета защитных слоев гидропроцессов. Пакет катализаторов состоял из ранжированных по форме и размеру зерен катализатора: сегментные кольца, полые цилиндры двух типоразмеров и зерна с сечением в форме трилистника. Эксперименты проводились в режиме струйного течения с неизменным ансамблем микрочастиц – железной окалины размером от 5 до 150 мкм на входе пакетной загрузки. Получено, что коэффициент проскока пакетной загрузки катализаторов защитного слоя существенно не менялся (K ≈ 0,985) в ходе эксперимента. При этом наблюдался линейный рост перепада давления на пакетной загрузке катализаторов защитного слоя высотой 17 см – с 220 до 408 Па, который происходил в результате улавливания зернами катализатора микрочастиц механических примесей. Теоретическая оценка начального перепада давления (228 Па) с хорошей точностью совпадает с экспериментальными данными (220 Па).</p></abstract><trans-abstract xml:lang="en"><p>A study was made of the efficiency of trapping solid microparticulates contained in diesel fuel for catalyst loading – an analogue of an industrial package of guard beds of hydroprocesses. The package of catalysts consisted of catalyst granules ranked by shape and size: segmented rings, hollow cylinders of two standard sizes and trilobe shape. The experiments were carried out in the trickle flow regime with a constant ensemble of microparticulates – iron scale with a size of 5 to 150 μm at the inlet of the catalysts loading. It was found that the penetration coefficient of the catalysts loading of the guard beds did not change significantly (K ≈ 0.985) during the experiment. At the same time, a linear increase in the pressure drop on the catalysts loading of the guard beds with a height of 17 cm from 220 to 408 Pa was observed which occurred as a result of the trapping of solid microparticulates by the catalyst granules. The theoretical estimate of the initial pressure drop (228 Pa) coincides with the experimental data (220 Pa) with good accuracy.</p></trans-abstract><kwd-group xml:lang="ru"><kwd>гидроочистка</kwd><kwd>защитные слои</kwd><kwd>механические примеси</kwd><kwd>перепад давления</kwd></kwd-group><kwd-group xml:lang="en"><kwd>hydrotreating</kwd><kwd>guard beds microparticulates</kwd><kwd>pressure drop</kwd></kwd-group></article-meta></front><back><ref-list><title>References</title><ref id="cit1"><label>1</label><citation-alternatives><mixed-citation xml:lang="ru">Speight J.G. Fouling in refineries // Fouling in Refineries. 2015. P. 1–538. https://doi.org/10.1016/C2013-0-19044-7</mixed-citation><mixed-citation xml:lang="en">Speight J.G. Fouling in refineries // Fouling in Refineries. 2015. P. 1–538. https://doi.org/10.1016/C2013-0-19044-7</mixed-citation></citation-alternatives></ref><ref id="cit2"><label>2</label><citation-alternatives><mixed-citation xml:lang="ru">Будуква С. В. и др. Дезактивация катализаторов гидроочистки (обзор) // Катализ в промышленности.. 2022. Т. 22, № 3. С. 38–65. https://doi.org/10.18412/1816-0387-2022-3-38-65</mixed-citation><mixed-citation xml:lang="en">Будуква С. В. и др. Дезактивация катализаторов гидроочистки (обзор) // Катализ в промышленности.. 2022. Т. 22, № 3. С. 38–65. https://doi.org/10.18412/1816-0387-2022-3-38-65</mixed-citation></citation-alternatives></ref><ref id="cit3"><label>3</label><citation-alternatives><mixed-citation xml:lang="ru">Polischuk C. et al. A review of foulant sources, operational issues, and remedies during the processing of oil sand derived bitumen fractions // Fuel. 2023. Vol. 340. https://doi.org/10.1016/j.fuel.2023.127516</mixed-citation><mixed-citation xml:lang="en">Polischuk C. et al. A review of foulant sources, operational issues, and remedies during the processing of oil sand derived bitumen fractions // Fuel. 2023. Vol. 340. https://doi.org/10.1016/j.fuel.2023.127516</mixed-citation></citation-alternatives></ref><ref id="cit4"><label>4</label><citation-alternatives><mixed-citation xml:lang="ru">Marafi M., Stanislaus A., Furimsky E. Handbook of Spent Hydroprocessing Catalysts: Second Edition // Handbook of Spent Hydroprocessing Catalysts: Second Edition. Amsterdam: Elsevier, 2017.</mixed-citation><mixed-citation xml:lang="en">Marafi M., Stanislaus A., Furimsky E. Handbook of Spent Hydroprocessing Catalysts: Second Edition // Handbook of Spent Hydroprocessing Catalysts: Second Edition. Amsterdam: Elsevier, 2017.</mixed-citation></citation-alternatives></ref><ref id="cit5"><label>5</label><citation-alternatives><mixed-citation xml:lang="ru">Toulhoat H., Raybaud P. Catalysis by transition metal sulphides: From molecular theory to industrial applications. Paris: Technip, 2013.</mixed-citation><mixed-citation xml:lang="en">Toulhoat H., Raybaud P. Catalysis by transition metal sulphides: From molecular theory to industrial applications. Paris: Technip, 2013.</mixed-citation></citation-alternatives></ref><ref id="cit6"><label>6</label><citation-alternatives><mixed-citation xml:lang="ru">Nadeina K.A. et al. Guard bed catalysts for silicon removal during hydrotreating of middle distillates // Catal. Today. 2019. Vol. 329. P. 53–62. https://doi.org/10.1016/j.cattod.2018.11.075</mixed-citation><mixed-citation xml:lang="en">Nadeina K.A. et al. Guard bed catalysts for silicon removal during hydrotreating of middle distillates // Catal. Today. 2019. Vol. 329. P. 53–62. https://doi.org/10.1016/j.cattod.2018.11.075</mixed-citation></citation-alternatives></ref><ref id="cit7"><label>7</label><citation-alternatives><mixed-citation xml:lang="ru">Nadeina K.A. et al. Influence of alumina precursor on silicon capacity of NiMo/γ-Al2O3 guard bed catalysts for gas oil hydrotreating // Catal. Today. 2020. Vol. 353. P. 53–62. https://doi.org/10.1016/j.cattod.2019.10.028</mixed-citation><mixed-citation xml:lang="en">Nadeina K.A. et al. Influence of alumina precursor on silicon capacity of NiMo/γ-Al2O3 guard bed catalysts for gas oil hydrotreating // Catal. Today. 2020. Vol. 353. P. 53–62. https://doi.org/10.1016/j.cattod.2019.10.028</mixed-citation></citation-alternatives></ref><ref id="cit8"><label>8</label><citation-alternatives><mixed-citation xml:lang="ru">Mik I.A. et al. Optimization of grading guard systems for trapping of particulates to prevent pressure drop buildup in gas oil hydrotreater // Fuel. 2021. Vol. 285. https://doi.org/10.1016/j.fuel.2020.119149</mixed-citation><mixed-citation xml:lang="en">Mik I.A. et al. Optimization of grading guard systems for trapping of particulates to prevent pressure drop buildup in gas oil hydrotreater // Fuel. 2021. Vol. 285. https://doi.org/10.1016/j.fuel.2020.119149</mixed-citation></citation-alternatives></ref><ref id="cit9"><label>9</label><citation-alternatives><mixed-citation xml:lang="ru">Moyse B.M. Raschig ring hds catalysts reduce pressure drop // Oil Gas J. 1984. Vol. 82, № 53. P. 164–166, 168</mixed-citation><mixed-citation xml:lang="en">Moyse B.M. Raschig ring hds catalysts reduce pressure drop // Oil Gas J. 1984. Vol. 82, № 53. P. 164–166, 168</mixed-citation></citation-alternatives></ref><ref id="cit10"><label>10</label><citation-alternatives><mixed-citation xml:lang="ru">Wang S. et al. Deposition of Fine Particles in Packed Beds at Hydrotreating Conditions: Role of Surface Chemistry // Ind. Eng. Chem. Res. 1999. Vol. 38, № 12. P. 4878–4888. https://doi.org/10.1021/ie990257+</mixed-citation><mixed-citation xml:lang="en">Wang S. et al. Deposition of Fine Particles in Packed Beds at Hydrotreating Conditions: Role of Surface Chemistry // Ind. Eng. Chem. Res. 1999. Vol. 38, № 12. P. 4878–4888. https://doi.org/10.1021/ie990257+</mixed-citation></citation-alternatives></ref><ref id="cit11"><label>11</label><citation-alternatives><mixed-citation xml:lang="ru">Polischuk C. et al. Impact of Fine Solids on Hydrotreating of Bitumen-Derived Gas Oil // Ind. Eng. Chem. Res. 2023. Vol. 62, № 2. P. 936–948. https://doi.org/10.1021/acs.iecr.2c04241</mixed-citation><mixed-citation xml:lang="en">Polischuk C. et al. Impact of Fine Solids on Hydrotreating of Bitumen-Derived Gas Oil // Ind. Eng. Chem. Res. 2023. Vol. 62, № 2. P. 936–948. https://doi.org/10.1021/acs.iecr.2c04241</mixed-citation></citation-alternatives></ref><ref id="cit12"><label>12</label><citation-alternatives><mixed-citation xml:lang="ru">Hamidipour M., Larachi F., Ring Z. Monitoring filtration in trickle beds using electrical capacitance tomography // Ind. Eng. Chem. Res. 2009. https://doi.org/10.1021/ie800810t</mixed-citation><mixed-citation xml:lang="en">Hamidipour M., Larachi F., Ring Z. Monitoring filtration in trickle beds using electrical capacitance tomography // Ind. Eng. Chem. Res. 2009. https://doi.org/10.1021/ie800810t</mixed-citation></citation-alternatives></ref><ref id="cit13"><label>13</label><citation-alternatives><mixed-citation xml:lang="ru">Robinson P.R., Dolbear G.E. Hydrotreating and Hydrocracking: Fundamentals // Practical Advances in Petroleum Processing. Springer New York, 2007. P. 177–218. https://doi.org/10.1007/978-0-387-25789-1_7</mixed-citation><mixed-citation xml:lang="en">Robinson P.R., Dolbear G.E. Hydrotreating and Hydrocracking: Fundamentals // Practical Advances in Petroleum Processing. Springer New York, 2007. P. 177–218. https://doi.org/10.1007/978-0-387-25789-1_7</mixed-citation></citation-alternatives></ref><ref id="cit14"><label>14</label><citation-alternatives><mixed-citation xml:lang="ru">Dalai A.K. et al. Deposition of fine particles during hydrotreating of oil sands bitumen-derived heavy gas oil in a packed bed reactor: Impact of process parameters and surface charge // Ind. Eng. Chem. Res. 2021. Vol. 60, № 43. P. 15464–15471. https://doi.org/10.1021/acs.iecr.1c03000</mixed-citation><mixed-citation xml:lang="en">Dalai A.K. et al. Deposition of fine particles during hydrotreating of oil sands bitumen-derived heavy gas oil in a packed bed reactor: Impact of process parameters and surface charge // Ind. Eng. Chem. Res. 2021. Vol. 60, № 43. P. 15464–15471. https://doi.org/10.1021/acs.iecr.1c03000</mixed-citation></citation-alternatives></ref><ref id="cit15"><label>15</label><citation-alternatives><mixed-citation xml:lang="ru">Ancheyta J. Modeling and Simulation of Catalytic Reactors for Petroleum Refining // Modeling and Simulation of Catalytic Reactors for Petroleum Refining. Hoboken: John Wiley &amp; Sons, Inc., 2011. https://doi.org/10.1002/9780470933565</mixed-citation><mixed-citation xml:lang="en">Ancheyta J. Modeling and Simulation of Catalytic Reactors for Petroleum Refining // Modeling and Simulation of Catalytic Reactors for Petroleum Refining. Hoboken: John Wiley &amp; Sons, Inc., 2011. https://doi.org/10.1002/9780470933565</mixed-citation></citation-alternatives></ref><ref id="cit16"><label>16</label><citation-alternatives><mixed-citation xml:lang="ru">Vogelaar B.M. et al. Hydroprocessing catalyst deactivation in commercial practice // Catalysis Today. Elsevier, 2010. Vol. 154, № 3–4. P. 256–263. https://doi.org/10.1016/j.cattod.2010.03.039</mixed-citation><mixed-citation xml:lang="en">Vogelaar B.M. et al. Hydroprocessing catalyst deactivation in commercial practice // Catalysis Today. Elsevier, 2010. Vol. 154, № 3–4. P. 256–263. https://doi.org/10.1016/j.cattod.2010.03.039</mixed-citation></citation-alternatives></ref><ref id="cit17"><label>17</label><citation-alternatives><mixed-citation xml:lang="ru">Kam E.K.T. et al. A hydroprocessing multicatalyst deactivation and reactor performance model-pilot-plant life test applications // Energy and Fuels. American Chemical Society, 2005. Vol. 19, № 3. P. 753–764. https://doi.org/10.1021/ef049843s</mixed-citation><mixed-citation xml:lang="en">Kam E.K.T. et al. A hydroprocessing multicatalyst deactivation and reactor performance model-pilot-plant life test applications // Energy and Fuels. American Chemical Society, 2005. Vol. 19, № 3. P. 753–764. https://doi.org/10.1021/ef049843s</mixed-citation></citation-alternatives></ref><ref id="cit18"><label>18</label><citation-alternatives><mixed-citation xml:lang="ru">Toulhoat H. et al. THERMIDOR: A new model for combined simulation of operations and optimization of catalysts in residues hydroprocessing units // Catal. Today. 2005. https://doi.org/10.1016/j.cattod.2005.08.023</mixed-citation><mixed-citation xml:lang="en">Toulhoat H. et al. THERMIDOR: A new model for combined simulation of operations and optimization of catalysts in residues hydroprocessing units // Catal. Today. 2005. https://doi.org/10.1016/j.cattod.2005.08.023</mixed-citation></citation-alternatives></ref><ref id="cit19"><label>19</label><citation-alternatives><mixed-citation xml:lang="ru">Rodríguez E. et al. Modeling of hydrotreating catalyst deactivation for heavy oil hydrocarbons // Fuel. 2018. https://doi.org/10.1016/j.fuel.2018.02.085</mixed-citation><mixed-citation xml:lang="en">Rodríguez E. et al. Modeling of hydrotreating catalyst deactivation for heavy oil hydrocarbons // Fuel. 2018. https://doi.org/10.1016/j.fuel.2018.02.085</mixed-citation></citation-alternatives></ref><ref id="cit20"><label>20</label><citation-alternatives><mixed-citation xml:lang="ru">Wang S., Chung K., Gray M.R. Role of hydrotreating products in deposition of fine particles in reactors // Fuel. 2001. https://doi.org/10.1016/S0016-2361(00)00173-3</mixed-citation><mixed-citation xml:lang="en">Wang S., Chung K., Gray M.R. Role of hydrotreating products in deposition of fine particles in reactors // Fuel. 2001. https://doi.org/10.1016/S0016-2361(00)00173-3</mixed-citation></citation-alternatives></ref><ref id="cit21"><label>21</label><citation-alternatives><mixed-citation xml:lang="ru">Ortiz-Arroyo A., Larachi F. Lagrange-Euler-Euler CFD approach for modeling deep-bed filtration in trickle flow reactors // Sep. Purif. Technol. Elsevier, 2005. Vol. 41, № 2. P. 155–172. https://doi.org/10.1016/j.seppur.2004.05.008</mixed-citation><mixed-citation xml:lang="en">Ortiz-Arroyo A., Larachi F. Lagrange-Euler-Euler CFD approach for modeling deep-bed filtration in trickle flow reactors // Sep. Purif. Technol. Elsevier, 2005. Vol. 41, № 2. P. 155–172. https://doi.org/10.1016/j.seppur.2004.05.008</mixed-citation></citation-alternatives></ref><ref id="cit22"><label>22</label><citation-alternatives><mixed-citation xml:lang="ru">Edouard D., Iliuta I., Larachi F. Role of gas phase in the deposition dynamics of fine particles in trickle-bed reactors // Chem. Eng. Sci. Pergamon, 2006. Vol. 61, № 12. P. 3875–3884. https://doi.org/10.1016/j.ces.2006.01.031</mixed-citation><mixed-citation xml:lang="en">Edouard D., Iliuta I., Larachi F. Role of gas phase in the deposition dynamics of fine particles in trickle-bed reactors // Chem. Eng. Sci. Pergamon, 2006. Vol. 61, № 12. P. 3875–3884. https://doi.org/10.1016/j.ces.2006.01.031</mixed-citation></citation-alternatives></ref><ref id="cit23"><label>23</label><citation-alternatives><mixed-citation xml:lang="ru">Iliuta I., Larachi F. Three-phase fixed-bed reactors // Multiphase Catalytic Reactors: Theory, Design, Manufacturing, and Applications. 2016. https://doi.org/10.1007/s11242-013-0199-x</mixed-citation><mixed-citation xml:lang="en">Iliuta I., Larachi F. Three-phase fixed-bed reactors // Multiphase Catalytic Reactors: Theory, Design, Manufacturing, and Applications. 2016. https://doi.org/10.1007/s11242-013-0199-x</mixed-citation></citation-alternatives></ref><ref id="cit24"><label>24</label><citation-alternatives><mixed-citation xml:lang="ru">Rana R. et al. The Impact of Process Parameters on the Deposition of Fines Present in Bitumen-Derived Gas Oil on Hydrotreating Catalyst // Energy and Fuels. 2017. https://doi.org/10.1021/acs.energyfuels.7b00554</mixed-citation><mixed-citation xml:lang="en">Rana R. et al. The Impact of Process Parameters on the Deposition of Fines Present in Bitumen-Derived Gas Oil on Hydrotreating Catalyst // Energy and Fuels. 2017. https://doi.org/10.1021/acs.energyfuels.7b00554</mixed-citation></citation-alternatives></ref><ref id="cit25"><label>25</label><citation-alternatives><mixed-citation xml:lang="ru">Rana R. et al. Deposition of fine particles of gas oil on hydrotreating catalyst: Impact of process parameters and filtration trends // Fuel Process. Technol. Elsevier B.V., 2018. Vol. 171. P. 223–231. https://doi.org/10.1016/j.fuproc.2017.09.019</mixed-citation><mixed-citation xml:lang="en">Rana R. et al. Deposition of fine particles of gas oil on hydrotreating catalyst: Impact of process parameters and filtration trends // Fuel Process. Technol. Elsevier B.V., 2018. Vol. 171. P. 223–231. https://doi.org/10.1016/j.fuproc.2017.09.019</mixed-citation></citation-alternatives></ref><ref id="cit26"><label>26</label><citation-alternatives><mixed-citation xml:lang="ru">Iliuta I., Larachi F. Three-phase fixed-bed reactors // Multiphase Catalytic Reactors: Theory, Design, Manufacturing, and Applications. 2016. https://doi.org/10.1007/s11242-013-0199-x</mixed-citation><mixed-citation xml:lang="en">Iliuta I., Larachi F. Three-phase fixed-bed reactors // Multiphase Catalytic Reactors: Theory, Design, Manufacturing, and Applications. 2016. https://doi.org/10.1007/s11242-013-0199-x</mixed-citation></citation-alternatives></ref><ref id="cit27"><label>27</label><citation-alternatives><mixed-citation xml:lang="ru">Gray M.R., Srinivasan N., Masliyah J.H. Pressure buildup in gas-liquid flow through packed beds due to deposition of fine particles // Can. J. Chem. Eng. 2002.</mixed-citation><mixed-citation xml:lang="en">Gray M.R., Srinivasan N., Masliyah J.H. Pressure buildup in gas-liquid flow through packed beds due to deposition of fine particles // Can. J. Chem. Eng. 2002.</mixed-citation></citation-alternatives></ref><ref id="cit28"><label>28</label><citation-alternatives><mixed-citation xml:lang="ru">Hamidipour M., Larachi F., Ring Z. Hydrodynamic observations of trickle beds under filtration conditions // Industrial and Engineering Chemistry Research. 2007. https://doi.org/10.1021/ie061360j</mixed-citation><mixed-citation xml:lang="en">Hamidipour M., Larachi F., Ring Z. Hydrodynamic observations of trickle beds under filtration conditions // Industrial and Engineering Chemistry Research. 2007. https://doi.org/10.1021/ie061360j</mixed-citation></citation-alternatives></ref><ref id="cit29"><label>29</label><citation-alternatives><mixed-citation xml:lang="ru">Wang S., Chung K., Gray M.R. Role of hydrotreating products in deposition of fine particles in reactors // Fuel. 2001. https://doi.org/10.1016/S0016-2361(00)00173-3</mixed-citation><mixed-citation xml:lang="en">Wang S., Chung K., Gray M.R. Role of hydrotreating products in deposition of fine particles in reactors // Fuel. 2001. https://doi.org/10.1016/S0016-2361(00)00173-3</mixed-citation></citation-alternatives></ref><ref id="cit30"><label>30</label><citation-alternatives><mixed-citation xml:lang="ru">Han S., Kim J., Ko S.H. Advances in air filtration technologies: structure-based and interaction-based approaches // Mater. Today Adv. 2021. Vol. 9. https://doi.org/10.1016/j.mtadv.2021.100134</mixed-citation><mixed-citation xml:lang="en">Han S., Kim J., Ko S.H. Advances in air filtration technologies: structure-based and interaction-based approaches // Mater. Today Adv. 2021. Vol. 9. https://doi.org/10.1016/j.mtadv.2021.100134</mixed-citation></citation-alternatives></ref><ref id="cit31"><label>31</label><citation-alternatives><mixed-citation xml:lang="ru">Felder R.M. Catalytic reactor design, by M. Orhan Tarhan. McGraw-Hill, 1983 // AIChE Journal. 1984. Vol. 30, № 1. 173–173 p. https://doi.org/10.1002/aic.690300127</mixed-citation><mixed-citation xml:lang="en">Felder R.M. Catalytic reactor design, by M. Orhan Tarhan. McGraw-Hill, 1983 // AIChE Journal. 1984. Vol. 30, № 1. 173–173 p. https://doi.org/10.1002/aic.690300127</mixed-citation></citation-alternatives></ref><ref id="cit32"><label>32</label><citation-alternatives><mixed-citation xml:lang="ru">Ancheyta J., Muñoz J.A.D., Macías M.J. Experimental and theoretical determination of the particle size of hydrotreating catalysts of different shapes // Catal. Today. Elsevier, 2005. Vol. 109, № 1–4. P. 120–127. https://doi.org/10.1016/j.cattod.2005.08.009</mixed-citation><mixed-citation xml:lang="en">Ancheyta J., Muñoz J.A.D., Macías M.J. Experimental and theoretical determination of the particle size of hydrotreating catalysts of different shapes // Catal. Today. Elsevier, 2005. Vol. 109, № 1–4. P. 120–127. https://doi.org/10.1016/j.cattod.2005.08.009</mixed-citation></citation-alternatives></ref><ref id="cit33"><label>33</label><citation-alternatives><mixed-citation xml:lang="ru">Macías M.J., Ancheyta J. Simulation of an isothermal hydrodesulfurization small reactor with different catalyst particle shapes // Catal. Today. 2004. Vol. 98, № 1-2 SPEC. ISS. P. 243–252. https://doi.org/10.1016/j.cattod.2004.07.038</mixed-citation><mixed-citation xml:lang="en">Macías M.J., Ancheyta J. Simulation of an isothermal hydrodesulfurization small reactor with different catalyst particle shapes // Catal. Today. 2004. Vol. 98, № 1-2 SPEC. ISS. P. 243–252. https://doi.org/10.1016/j.cattod.2004.07.038</mixed-citation></citation-alternatives></ref><ref id="cit34"><label>34</label><citation-alternatives><mixed-citation xml:lang="ru">Kirsch A.A., Fuchs N.A. Studies on fibrous aerosol filters-iii diffusional deposition of aerosols in fibrous filters // Ann. Occup. Hyg. 1968. Vol. 11, № 4. P. 299–304. https://doi.org/10.1093/annhyg/11.4.299</mixed-citation><mixed-citation xml:lang="en">Kirsch A.A., Fuchs N.A. Studies on fibrous aerosol filters-iii diffusional deposition of aerosols in fibrous filters // Ann. Occup. Hyg. 1968. Vol. 11, № 4. P. 299–304. https://doi.org/10.1093/annhyg/11.4.299</mixed-citation></citation-alternatives></ref></ref-list><fn-group><fn fn-type="conflict"><p>The authors declare that there are no conflicts of interest present.</p></fn></fn-group></back></article>
