Petroleum Chemistry最新文献_第9页

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, Alexey V. Ozerskii, Emmanuel Busillo, Alexey V. Nikitin, Igor V. Sedov, Vladimir S. Arutyunov","doi":"10.1134/S0965544125601292","DOIUrl":"10.1134/S0965544125601292","url":null,"abstract":"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 O2 conversion (>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 H2 produced in this zone, which shifts the equilibrium in the reaction system (2CH4 ↔ C2H4 + 2H2 ↔ C2H2 + 3H2) to the left. This shift, in turn, reduces both the acetylene content in the gas mixture and its consumption via reaction with OH• radicals. Furthermore, an increase in pressure promotes the influence of CO methanation, thereby limiting the maximum achievable CH4 conversion.","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, Sha Wang, Bin Hu, Junyin Wang, Ziru Wang, Tingting Zhang, Cong Shi","doi":"10.1134/S0965544125600298","DOIUrl":"10.1134/S0965544125600298","url":null,"abstract":"This study presents a thermodynamic analysis of hydrogen (H2) 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 H2 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 H2 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 H2 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.","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, Rongxiang Zhao, Xiuping Li, Liangpei Hou","doi":"10.1134/S0965544124601923","DOIUrl":"10.1134/S0965544124601923","url":null,"abstract":"A deep eutectic solvents (DES) was synthesized by stirring mixture of 1-butyl-pyridinehydrochloride ([C4pyr]Cl) and oxalic acid (C2H2O4) at 100°C. The [C4pyr]Cl/C2H2O4 DES was characterized by FT-IR and 1H 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 [C4pyr]Cl/C2H2O4 DES are readily oxidized to ‒COOOH by H2O2, 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, T = 50°C, and O/S = 6, the DBT removal rate reached 98.6% within 80 min. The catalytic activity of [C4pyr]Cl/C2H2O4 exhibited only a slight decrease after nine regeneration cycles. The apparent activation energy for DBT removal using [C4pyr]Cl/C2H2O4 was 33.3 kJ/mol. Experimental results indicate that the low apparent activation energy contributes to the high desulfurization efficiency.","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

Seed-Assisted Synthesis of Mordenite and Its Physicochemical and Catalytic Properties in Toluene Disproportionation 丝光沸石的种子辅助合成及其甲苯歧化的理化和催化性能

IF 1.1 4区工程技术

Petroleum Chemistry Pub Date : 2026-02-25 DOI: 10.1134/S0965544125602054

Anastasiia P. Dubtsova, Egor P. Andriako, Tatiana O. Bok, Olga A. Ponomareva, Irina I. Ivanova

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

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

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, Qahtan A. Mahmood, Amer T. Nawaf, Mohamed A. Habila, Ali A. Hassan, Rajesh Haldhar","doi":"10.1134/S0965544124602850","DOIUrl":"10.1134/S0965544124602850","url":null,"abstract":"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 (Co3O4) 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 (Co3O4/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 in situ from acetic acid and hydrogen peroxide (H2O2), 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.","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, G. B. Narochnyi, I. N. Zubkov, D. A. Ponomarev, M. A. Zubkova, A. P. Savost’yanov, R. E. Yakovenko","doi":"10.1134/S0965544125600195","DOIUrl":"10.1134/S0965544125600195","url":null,"abstract":"This study investigates a silica-gel-supported cobalt catalyst for synthesizing long-chain hydrocarbons (C19+) from CO and H2. The process conditions were varied within the following ranges: pressure, 1.5–3.5 MPa; gas hourly space velocity (GHSV), 300–830 h–1; H2/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 C19+ hydrocarbons in the products. When the C19+ content increased from approximately 40 to 55 wt %, the deactivation rate increased more than tenfold. Under optimized conditions (H2/CO = 2.3, P = 2.0 MPa, T = 193°C), the C19+ 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.","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

引用次数: 0

Effects of Pressure on the Non-Catalytic Thermal Conversion of Methane in Various Gases 压力对不同气体中甲烷非催化热转化的影响

IF 1.1 4区工程技术

Petroleum Chemistry Pub Date : 2026-01-18 DOI: 10.1134/S0965544125601127

V. I. Savchenko, A. V. Ozerskii, E. Busillo, A. V. Nikitin, I. V. Sedov, V. S. Arutyunov

{"title":"Effects of Pressure on the Non-Catalytic Thermal Conversion of Methane in Various Gases","authors":"V. I. Savchenko, A. V. Ozerskii, E. Busillo, A. V. Nikitin, I. V. Sedov, V. S. Arutyunov","doi":"10.1134/S0965544125601127","DOIUrl":"10.1134/S0965544125601127","url":null,"abstract":"A detailed kinetic model based on the NUI Galway mechanism for light hydrocarbon oxidation was used to investigate the effects of pressure on the non-catalytic conversion of methane in various gas atmospheres (Ar, H2, CO, CO2, H2O). The study also evaluated the impact of H2O addition on the conversion of CH4 in mixtures with H2 and CO. For CH4 mixed with Ar, CO, or H2, the methane pyrolysis rate exhibits a power-law dependence on pressure (W = APn), with the exponent n ranging from ~0.4 to ~0.65 in the 1400–1800 K temperature range. The achievable CH4 conversion decreases significantly with rising pressure, particularly for CH4–H2 mixtures. For the non-catalytic conversion of CH4 in mixtures with H2O and CO2, the initial pyrolysis rate is similar to that in an argon atmosphere. At high pressures, however, the CH4 concentration profile subsequently passes through a rising region. This is attributed to the interaction of C2H2 and CO products with H2O, which generates additional H2 and consequently shifts the equilibrium of the reaction system (2CH4 ↔ C2H4 + 2H2 ↔ C2H2 + H2) to the left.","PeriodicalId":725,"journal":{"name":"Petroleum Chemistry","volume":"65 11","pages":"1317 - 1328"},"PeriodicalIF":1.1,"publicationDate":"2026-01-18","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"147340235","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