Petroleum Chemistry最新文献

筛选
英文 中文
Kinetic Features of Cumene Dehydrogenation over Porous Catalytic Converters 多孔催化转化器上异丙烯脱氢的动力学特征
IF 1.1 4区 工程技术
Petroleum Chemistry Pub Date : 2026-03-16 DOI: 10.1134/S0965544125601620
Alexey S. Fedotov, Danil Yu. Grachev, Roman D. Kapustin
{"title":"Kinetic Features of Cumene Dehydrogenation over Porous Catalytic Converters","authors":"Alexey S. Fedotov,&nbsp;Danil Yu. Grachev,&nbsp;Roman D. Kapustin","doi":"10.1134/S0965544125601620","DOIUrl":"10.1134/S0965544125601620","url":null,"abstract":"<p>The kinetics of cumene dehydrogenation in the channels of porous ceramic converters modified with tungsten oxide were investigated. It was shown that, under the reaction conditions studied, this process occurs far from thermodynamic equilibrium in an open system and follows a first-order kinetic equation with respect to cumene. Based on the effective activation energy (161 kJ/mol) and an analysis of the reaction rate–temperature relationship, a stepwise sequence of surface dehydrogenation reactions over WO<sub>3</sub> is proposed: adsorption of cumene on W<sup>6+</sup> acid sites, hydrogen abstraction leading to the formation of metastable carbenium ions, and hydrogen recombination on the catalyst surface. The resulting activation energy and pre-exponential factor (1.85 × 10<sup>8</sup>) are consistent with values previously reported for the dehydrogenation of alkylbenzenes over oxide catalysts, thereby supporting the validity of the proposed kinetic model.</p>","PeriodicalId":725,"journal":{"name":"Petroleum Chemistry","volume":"66 1","pages":"14 - 27"},"PeriodicalIF":1.1,"publicationDate":"2026-03-16","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"147559692","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":4,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
引用次数: 0
Selective Alkylation of Toluene with Diethyl Carbonate over MgO- and Pd-Modified ZSM-5 Catalysts MgO和pd改性ZSM-5催化剂上甲苯与碳酸二乙酯的选择性烷基化反应
IF 1.1 4区 工程技术
Petroleum Chemistry Pub Date : 2026-03-05 DOI: 10.1134/S0965544126600256
Michail D. Kryuchkov, Leonid A. Kulikov, Ivan S. Levin, Eduard A. Karakhanov, Anton L. Maximov
{"title":"Selective Alkylation of Toluene with Diethyl Carbonate over MgO- and Pd-Modified ZSM-5 Catalysts","authors":"Michail D. Kryuchkov,&nbsp;Leonid A. Kulikov,&nbsp;Ivan S. Levin,&nbsp;Eduard A. Karakhanov,&nbsp;Anton L. Maximov","doi":"10.1134/S0965544126600256","DOIUrl":"10.1134/S0965544126600256","url":null,"abstract":"<p>The alkylation of toluene with diethyl carbonate (DEC) was studied over ZSM-5 (MFI) zeolite catalysts modified with magnesium oxide and palladium. MgO modification effectively suppressed strong Brønsted acid sites, leading to enhanced para-selectivity by inhibiting disproportionation, isomerization, and deep alkylation reactions. The introduction of palladium provided hydrogenation–dehydrogenation functionality, markedly improving catalyst stability by suppressing olefin oligomerization and coke formation. As a result, high selectivity toward <i>p</i>-ethyltoluene was achieved at moderate toluene conversion under optimized conditions. The influence of reaction temperature, space velocity, and toluene/DEC molar ratio on catalytic performance was systematically investigated. Toluene conversion exhibited non-monotonic behavior with respect to these parameters, reflecting a balance between DEC activation, reactant contact time, and catalyst deactivation. Optimal operating conditions provided high para-selectivity while limiting secondary isomerization and polyalkylation reactions. Fresh and spent catalysts were characterized by XRD, N<sub>2</sub> physisorption, NH<sub>3</sub>-TPD, Py-IR, TEM, TGA, and DSC. These analyses revealed that MgO modification alone leads to the formation of condensed, pore-blocking coke, whereas palladium alters the nature of carbonaceous deposits toward less condensed species, thereby enhancing catalyst stability. Compared with literature systems based on alcohols and other carbonates, the developed catalysts operate at lower alkylating-agent excess and higher space velocities while maintaining competitive conversion and para-selectivity.</p>","PeriodicalId":725,"journal":{"name":"Petroleum Chemistry","volume":"66 1","pages":"28 - 48"},"PeriodicalIF":1.1,"publicationDate":"2026-03-05","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"147559083","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":4,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
引用次数: 0
High-Pressure Non-Catalytic Partial Oxidation of Methane 甲烷高压非催化部分氧化
IF 1.1 4区 工程技术
Petroleum Chemistry Pub Date : 2026-03-05 DOI: 10.1134/S0965544125601292
Valery I. Savchenko, Alexey V. Ozerskii, Emmanuel Busillo, Alexey V. Nikitin, Igor V. Sedov, Vladimir S. Arutyunov
{"title":"High-Pressure Non-Catalytic Partial Oxidation of Methane","authors":"Valery I. Savchenko,&nbsp;Alexey V. Ozerskii,&nbsp;Emmanuel Busillo,&nbsp;Alexey V. Nikitin,&nbsp;Igor V. Sedov,&nbsp;Vladimir S. Arutyunov","doi":"10.1134/S0965544125601292","DOIUrl":"10.1134/S0965544125601292","url":null,"abstract":"<p>This study presents the results of detailed kinetic modeling for the high-pressure, non-catalytic partial oxidation of natural gas. The findings demonstrate the critical importance of reaction kinetics in determining the actual product distribution, particularly given the extended time required for reach equilibrium under these conditions. The influence of kinetics was evaluated across a pressure range of 1 to 100 bar. Although near-complete O<sub>2</sub> conversion (&gt;99.99%) is achieved very rapidly at high pressures, a significant amount of unreacted methane remains at this point. Attaining high methane conversion in the post-flame zone requires a time frame that is several orders of magnitude longer. This is attributed to the increasing impact of the partial pressure of H<sub>2</sub> produced in this zone, which shifts the equilibrium in the reaction system (2CH<sub>4</sub> ↔ C<sub>2</sub>H<sub>4</sub> + 2H<sub>2</sub> ↔ C<sub>2</sub>H<sub>2</sub> + 3H<sub>2</sub>) to the left. This shift, in turn, reduces both the acetylene content in the gas mixture and its consumption via reaction with OH<sup>•</sup> radicals. Furthermore, an increase in pressure promotes the influence of CO methanation, thereby limiting the maximum achievable CH<sub>4</sub> conversion.</p>","PeriodicalId":725,"journal":{"name":"Petroleum Chemistry","volume":"66 1","pages":"73 - 87"},"PeriodicalIF":1.1,"publicationDate":"2026-03-05","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"147558837","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":4,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
引用次数: 0
Study on the Hydrogen Production Characteristics of Sorption-Enhanced Steam Reforming of Shale Gas Using Calcium-Based Adsorbents 钙基吸附剂吸附强化页岩气蒸汽重整制氢特性研究
IF 1.1 4区 工程技术
Petroleum Chemistry Pub Date : 2026-03-05 DOI: 10.1134/S0965544125600298
Lipei Qiu, Sha Wang, Bin Hu, Junyin Wang, Ziru Wang, Tingting Zhang, Cong Shi
{"title":"Study on the Hydrogen Production Characteristics of Sorption-Enhanced Steam Reforming of Shale Gas Using Calcium-Based Adsorbents","authors":"Lipei Qiu,&nbsp;Sha Wang,&nbsp;Bin Hu,&nbsp;Junyin Wang,&nbsp;Ziru Wang,&nbsp;Tingting Zhang,&nbsp;Cong Shi","doi":"10.1134/S0965544125600298","DOIUrl":"10.1134/S0965544125600298","url":null,"abstract":"<p>This study presents a thermodynamic analysis of hydrogen (H<sub>2</sub>) production via shale gas steam reforming (SG-SR) and shale gas sorption-enhanced steam reforming (SG-SESR). The analysis was performed using HSC Chemistry software based on the principle of Gibbs free energy minimization. First, the influence of key operating parameters, such as the steam-to-carbon molar ratio (S/C), temperature, and pressure, on the H<sub>2</sub> yield and concentration, carbon-containing gas concentration, and carbon deposition during the SG-SR process was investigated. The results showed that the optimal reaction conditions were 700°C, 0.10 MPa, and S/C = 4. Under these conditions, the H<sub>2</sub> yield and concentration (on a dry gas basis) were 4.04 mol/mol and 84.05%, respectively. Subsequently, the impact of the CaO-to-carbon molar ratio (CaO/C) on SG-SESR, as well as the synergistic effects of S/C and CaO/C, were explored. The results demonstrated that when the temperature was controlled within 500–600°C with S/C = 6 and CaO/C = 2, the H<sub>2</sub> yield reached 4.30 mol/mol, and the concentration peaked at 99.66%. This thermodynamic analysis of SG-SR and SG-SESR processes not only advances the comprehensive SG utilization and the development of novel clean hydrogen production technologies but also provides theoretical guidance for the practical application of shale gas reforming.</p>","PeriodicalId":725,"journal":{"name":"Petroleum Chemistry","volume":"66 1","pages":"88 - 101"},"PeriodicalIF":1.1,"publicationDate":"2026-03-05","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"147558838","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":4,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
引用次数: 0
Research on a Dual-Function DES [C4pyr]Cl/C2H2O4 as a Desulfurization Catalyst and Extractant 双功能DES [C4pyr]Cl/C2H2O4作为脱硫催化剂和萃取剂的研究
IF 1.1 4区 工程技术
Petroleum Chemistry Pub Date : 2026-02-25 DOI: 10.1134/S0965544124601923
Hongyin Yu, Rongxiang Zhao, Xiuping Li, Liangpei Hou
{"title":"Research on a Dual-Function DES [C4pyr]Cl/C2H2O4 as a Desulfurization Catalyst and Extractant","authors":"Hongyin Yu,&nbsp;Rongxiang Zhao,&nbsp;Xiuping Li,&nbsp;Liangpei Hou","doi":"10.1134/S0965544124601923","DOIUrl":"10.1134/S0965544124601923","url":null,"abstract":"<p>A deep eutectic solvents (DES) was synthesized by stirring mixture of 1-butyl-pyridinehydrochloride ([C<sub>4</sub>pyr]Cl) and oxalic acid (C<sub>2</sub>H<sub>2</sub>O<sub>4</sub>) at 100°C. The [C<sub>4</sub>pyr]Cl/C<sub>2</sub>H<sub>2</sub>O<sub>4</sub> DES was characterized by FT-IR and <sup>1</sup>H NMR spectroscopy. This DES is capable of extracting thiophene-type sulfides due to the similar polarity of 1-butyl-pyridine and DBT. The –COOH groups within the [C<sub>4</sub>pyr]Cl/C<sub>2</sub>H<sub>2</sub>O<sub>4</sub> DES are readily oxidized to ‒COOOH by H<sub>2</sub>O<sub>2</sub>, which susequently catalyzes the thiophene oxidation into sulfone in the model oil. The higher polarity of sulfone compared to that of thiophone enhances their solubility in the solvent. When the V(DES)/V(model oil) = 0.2, <i>T</i> = 50°C, and O/S = 6, the DBT removal rate reached 98.6% within 80 min. The catalytic activity of [C<sub>4</sub>pyr]Cl/C<sub>2</sub>H<sub>2</sub>O<sub>4</sub> exhibited only a slight decrease after nine regeneration cycles. The apparent activation energy for DBT removal using [C<sub>4</sub>pyr]Cl/C<sub>2</sub>H<sub>2</sub>O<sub>4</sub> was 33.3 kJ/mol. Experimental results indicate that the low apparent activation energy contributes to the high desulfurization efficiency.</p>","PeriodicalId":725,"journal":{"name":"Petroleum Chemistry","volume":"66 1","pages":"49 - 56"},"PeriodicalIF":1.1,"publicationDate":"2026-02-25","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"147560860","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":4,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
引用次数: 0
Novel Catalysts Based on Nanosized ZSM-5 and Silicon Carbide for Converting Rapeseed Oil to “Green” Hydrocarbons 基于纳米ZSM-5和碳化硅的新型催化剂将菜籽油转化为“绿色”碳氢化合物
IF 1.1 4区 工程技术
Petroleum Chemistry Pub Date : 2026-02-19 DOI: 10.1134/S0965544125601486
Alexey G. Dedov, Alexey S. Loktev, Malika N. Vagapova, Alexey A. Sadovnikov, Kirill A. Cherednichenko
{"title":"Novel Catalysts Based on Nanosized ZSM-5 and Silicon Carbide for Converting Rapeseed Oil to “Green” Hydrocarbons","authors":"Alexey G. Dedov,&nbsp;Alexey S. Loktev,&nbsp;Malika N. Vagapova,&nbsp;Alexey A. Sadovnikov,&nbsp;Kirill A. Cherednichenko","doi":"10.1134/S0965544125601486","DOIUrl":"10.1134/S0965544125601486","url":null,"abstract":"<p>A nanosized ZSM-5 zeolite and a novel material composed of ZSM-5 nanoparticles and silicon carbide were synthesized directly in the proton form via a microwave-assisted hydrothermal method and tested for the first time as catalysts for rapeseed oil conversion. Both catalysts achieved 100% conversion of rapeseed oil to C<sub>2</sub>–C<sub>4</sub> olefins and aromatic hydrocarbons, which are applicable as “green” components of fuels and intermediates for petrochemical synthesis. The results demonstrate that the composite of silicon carbide and nanosized ZSM-5 modifies the catalytic performance in rapeseed oil conversion.</p>","PeriodicalId":725,"journal":{"name":"Petroleum Chemistry","volume":"66 1","pages":"1 - 13"},"PeriodicalIF":1.1,"publicationDate":"2026-02-19","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://link.springer.com/content/pdf/10.1134/S0965544125601486.pdf","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"147560404","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":4,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"OA","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
引用次数: 0
Novel Catalysts for Producing “Green” Intermediates for Petrochemical Synthesis from Wood Waste 利用木材废料生产“绿色”石油化工中间体的新型催化剂
IF 1.1 4区 工程技术
Petroleum Chemistry Pub Date : 2026-02-13 DOI: 10.1134/S0965544125601334
Alexey G. Dedov, Maya V. Kulikova, Alexey S. Loktev, Alla Yu. Krylova, Albert B. Kulikov, Kristina O. Krysanova, Mark A. Manzhikov
{"title":"Novel Catalysts for Producing “Green” Intermediates for Petrochemical Synthesis from Wood Waste","authors":"Alexey G. Dedov,&nbsp;Maya V. Kulikova,&nbsp;Alexey S. Loktev,&nbsp;Alla Yu. Krylova,&nbsp;Albert B. Kulikov,&nbsp;Kristina O. Krysanova,&nbsp;Mark A. Manzhikov","doi":"10.1134/S0965544125601334","DOIUrl":"10.1134/S0965544125601334","url":null,"abstract":"<p>Co- and Ni-based catalysts derived from aluminum–magnesium hydrotalcites were investigated for the hydrogenation of carbon-rich (up to 66 wt %) biochars prepared by the hydrothermal carbonization of biomass. The biochar was liquefied at 375°C using molecular H<sub>2</sub> generated from tetralin and/or externally supplied molecular H<sub>2</sub> <i>in situ</i>. In all cases, feedstock conversion exceeded 90%. A liquid product yield of 77 wt % was achieved with the Co-based catalyst.</p>","PeriodicalId":725,"journal":{"name":"Petroleum Chemistry","volume":"66 1","pages":"65 - 72"},"PeriodicalIF":1.1,"publicationDate":"2026-02-13","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"147559259","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":4,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
引用次数: 0
Eco-Friendly Reduction of Graphene Oxide-Co3O4 from Waste Material for Rapid Oxidative Desulfurization of Sulfur Compounds Using a Digital Baffle Batch Reactor: Production of Clean Fuel 利用数字挡板间歇式反应器从废料中环保还原氧化石墨烯- co3o4,用于硫化合物的快速氧化脱硫:生产清洁燃料
IF 1.1 4区 工程技术
Petroleum Chemistry Pub Date : 2026-02-13 DOI: 10.1134/S0965544124602850
Jasim I. Humadi, Qahtan A. Mahmood, Amer T. Nawaf, Mohamed A. Habila, Ali A. Hassan, Rajesh Haldhar
{"title":"Eco-Friendly Reduction of Graphene Oxide-Co3O4 from Waste Material for Rapid Oxidative Desulfurization of Sulfur Compounds Using a Digital Baffle Batch Reactor: Production of Clean Fuel","authors":"Jasim I. Humadi,&nbsp;Qahtan A. Mahmood,&nbsp;Amer T. Nawaf,&nbsp;Mohamed A. Habila,&nbsp;Ali A. Hassan,&nbsp;Rajesh Haldhar","doi":"10.1134/S0965544124602850","DOIUrl":"10.1134/S0965544124602850","url":null,"abstract":"<p>The primary objective of this study was reduction of waste materials and their convertation into valuable resources. The secondary objective was to utilize the produced materials for elimination air pollutants. Herein, a novel nanocatalyst, cobalt oxide (Co<sub>3</sub>O<sub>4</sub>) supported on reduced graphene oxide (rGO), was synthesized via an impregnation technology and employed for the oxidative desulfurization (ODS) of heavy naphtha in a Digital Baffle Batch Reactor (DBBR). The rGO nano-support was prepared from waste material through a catalytic reaction. The developed (Co<sub>3</sub>O<sub>4</sub>/rGO) nanocatalyst exhibited outstanding catalytic efficiency attributed to its effective impregnation, favorable pore size distribution, high activity, and large surface area, as confirmed by FESEM, EDX, XRD and BET analyses. The efficacy of the prepared nanocatalyst, combined with novel oxidant, performic acid, produced <i>in situ</i> from acetic acid and hydrogen peroxide (H<sub>2</sub>O<sub>2</sub>), was assessed in the DBBR under various ODS conditions, including reaction times (15, 25, and 35 min), impeller speeds (140, 200, and 260 rpm), and catalyst amounts (0.4, 0.8, and 1.2 g). The experimental results indicated that increasing the oxidation time, impeller speed, and catalyst amount enhanced desulfurization of the oil feedstock, yielding a cleaner fuel. Under optimal conditions (35 min reaction time, 260 rpm impeller speed, and 0.8 g of modified nanocatalyst), a sulfur conversion efficiency of 93.63% was achieved. The developed DBBR design demonstrated a high sulfur removal in only 35 min, a significant improvement compared to previous studies that required longer reaction times for similar or lower efficiencies.</p>","PeriodicalId":725,"journal":{"name":"Petroleum Chemistry","volume":"66 1","pages":"112 - 126"},"PeriodicalIF":1.1,"publicationDate":"2026-02-13","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"147559246","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":4,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
引用次数: 0
Silica-Gel-Supported Cobalt Catalysts for the Selective Synthesis of Long-Chain Hydrocarbons (C19+) 硅-凝胶负载钴催化剂选择性合成长链烃(C19+)
IF 1.1 4区 工程技术
Petroleum Chemistry Pub Date : 2026-02-04 DOI: 10.1134/S0965544125600195
A. A. Chemes, G. B. Narochnyi, I. N. Zubkov, D. A. Ponomarev, M. A. Zubkova, A. P. Savost’yanov, R. E. Yakovenko
{"title":"Silica-Gel-Supported Cobalt Catalysts for the Selective Synthesis of Long-Chain Hydrocarbons (C19+)","authors":"A. A. Chemes,&nbsp;G. B. Narochnyi,&nbsp;I. N. Zubkov,&nbsp;D. A. Ponomarev,&nbsp;M. A. Zubkova,&nbsp;A. P. Savost’yanov,&nbsp;R. E. Yakovenko","doi":"10.1134/S0965544125600195","DOIUrl":"10.1134/S0965544125600195","url":null,"abstract":"<p>This study investigates a silica-gel-supported cobalt catalyst for synthesizing long-chain hydrocarbons (C<sub>19+</sub>) from CO and H<sub>2</sub>. The process conditions were varied within the following ranges: pressure, 1.5–3.5 MPa; gas hourly space velocity (GHSV), 300–830 h<sup>–1</sup>; H<sub>2</sub>/CO ratio, 2.0–2.3; and temperature, 187–213°C. Catalytic testing revealed a correlation between the catalyst deactivation rate and the content of C<sub>19+</sub> hydrocarbons in the products. When the C<sub>19+</sub> content increased from approximately 40 to 55 wt %, the deactivation rate increased more than tenfold. Under optimized conditions (H<sub>2</sub>/CO = 2.3, <i>P</i> = 2.0 MPa, <i>T</i> = 193°C), the C<sub>19+</sub> content reached ~46–50 wt %, and the deactivation rate was minimized. A long-term stability test over 500 h was used to project a catalyst cycle length, which was found to be at least 4000 h. The study results provide a foundation for optimizing Fischer–Tropsch process conditions to maximize catalyst lifetime and selectivity toward heavy hydrocarbons, supporting the recommendation of the proposed catalyst for industrial implementation.</p>","PeriodicalId":725,"journal":{"name":"Petroleum Chemistry","volume":"65 11","pages":"1305 - 1316"},"PeriodicalIF":1.1,"publicationDate":"2026-02-04","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"147336557","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":4,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
引用次数: 0
Potential of Membrane-Based Separation Methods for Producing Low-Carbon Petrochemicals and Renewable Jet Fuels from ABE Fermentation Products (A Review) ABE发酵产物膜分离制备低碳石化产品和可再生航空燃料的研究进展
IF 1.1 4区 工程技术
Petroleum Chemistry Pub Date : 2026-02-04 DOI: 10.1134/S0965544125601760
E. A. Grushevenko, M. V. Magomedova, T. N. Rokhmanka, A. D. Cherepanova, G. S. Golubev, G. I. Konstantinov, I. L. Borisov, K. I. Dement’ev
{"title":"Potential of Membrane-Based Separation Methods for Producing Low-Carbon Petrochemicals and Renewable Jet Fuels from ABE Fermentation Products (A Review)","authors":"E. A. Grushevenko,&nbsp;M. V. Magomedova,&nbsp;T. N. Rokhmanka,&nbsp;A. D. Cherepanova,&nbsp;G. S. Golubev,&nbsp;G. I. Konstantinov,&nbsp;I. L. Borisov,&nbsp;K. I. Dement’ev","doi":"10.1134/S0965544125601760","DOIUrl":"10.1134/S0965544125601760","url":null,"abstract":"<p>This review analyzes existing strategies for intensifying bioalcohol production <i>via</i> acetone–butanol–ethanol (ABE) fermentation focusing on the use of membrane concentration techniques. It also discusses the potential applications of the resulting concentrates as feedstocks for low-carbon fuels and petrochemicals. The review comprises three parts: (1) the current state of ABE fermentation technology, including its fundamental principles as they relate to biomass type; (2) membrane-based separation techniques for concentrating target fermentation products, with a primary focus on pervaporation and promising membrane types and materials; and (3) the downstream processing of ABE concentrates into high-value-added petrochemicals.</p>","PeriodicalId":725,"journal":{"name":"Petroleum Chemistry","volume":"65 11","pages":"1245 - 1279"},"PeriodicalIF":1.1,"publicationDate":"2026-02-04","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"147336556","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":4,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
引用次数: 0
0
×
引用
GB/T 7714-2015
复制
MLA
复制
APA
复制
导出至
BibTeX EndNote RefMan NoteFirst NoteExpress
×
提示
您的信息不完整,为了账户安全,请先补充。
现在去补充
×
提示
您因"违规操作"
具体请查看互助需知
我知道了
×
提示
确定
请完成安全验证×
相关产品
×
本文献相关产品
联系我们:info@booksci.cn Book学术提供免费学术资源搜索服务,方便国内外学者检索中英文文献。致力于提供最便捷和优质的服务体验。 Copyright © 2023 布克学术 All rights reserved.
京ICP备2023020795号-1
ghs 京公网安备 11010802042870号
Book学术文献互助
Book学术文献互助群
群 号:604180095
Book学术官方微信
小红书