K. S. Votolin, S. I. Zherebtsov, K. M. Shpakodraev, N. V. Malyshenko
{"title":"Structural-Group Composition and Biological Activity of Humic, Hymatomelanic, Humous, and Fulvic Acids from Lignite","authors":"K. S. Votolin, S. I. Zherebtsov, K. M. Shpakodraev, N. V. Malyshenko","doi":"10.3103/S1068364X26600429","DOIUrl":"10.3103/S1068364X26600429","url":null,"abstract":"<p>Fractions of humic materials, including humic, hymatomelanic, humous, and fulvic acids, are derived from Kansk-Achinsk and South Ural lignite. The yield of humic materials is greatest for naturally oxidized lignite from the Tisul field in the Kansk-Achinsk Basin: 60.9% humic acids (including 11.3% hymatomelanic acids and 49.6% humous acids) and 9.6% fulvic acids). The fractions are studied by means of <sup>13</sup>С NMR (CPMAS) spectroscopy, technical analysis, and elemental analysis. Each fraction is found to have a specific elemental composition and also structural-group composition. The biological activity of the fractions is assessed for wheat seeds of the Aphrodite variety. For all the humic materials, the biological activity is relatively high; they may be recommended as growth stimulators for plants. The phytoactivity index of humic acids is found to depend on the structural-group parameters calculated from the <sup>13</sup>C NMR (CPMAS) spectroscopic data: the aromatic content <i>f</i><sub>a</sub> (<i>R</i><sup>2</sup> = 0.86–0.96) and the aromatic/aliphatic ratio <i>f</i><sub>a/al</sub> (<i>R</i><sup>2</sup> = 0.88–0.98). The fulvic acids have the greatest biological activity with respect to the wheat seeds. Their phytoactivity index is relatively high in solutions whose concentration is an order of magnitude lower: the most effective concentration is 0.00025% for fulvic acids and 0.0050% for humic, hymatomelanic, and humous acids.</p>","PeriodicalId":519,"journal":{"name":"Coke and Chemistry","volume":"69 5","pages":"261 - 270"},"PeriodicalIF":0.6,"publicationDate":"2026-08-28","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"148823123","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
N. S. Cheglakova, E. E. Sokolovskaya, D. R. Izmaylov, E. V. Karunova, O. A. Kalko
{"title":"Influence of the Iron and Calcium Content of Coking Batch on the Hot Strength of Coke at Severstal","authors":"N. S. Cheglakova, E. E. Sokolovskaya, D. R. Izmaylov, E. V. Karunova, O. A. Kalko","doi":"10.3103/S1068364X26600442","DOIUrl":"10.3103/S1068364X26600442","url":null,"abstract":"<p>The influence of the iron and calcium content in coking batch on the reactivity (<i>CRI</i>) and strength after reaction with carbon dioxide (<i>CSR</i>) of laboratory coke is studied by adding components to the batch. Increasing the content of calcium oxide and ferric oxide in the batch’s ash impairs the properties of the laboratory coke produced. The influence of additional iron oxide is stronger and more specific than the influence of extra calcium oxide.</p>","PeriodicalId":519,"journal":{"name":"Coke and Chemistry","volume":"69 5","pages":"276 - 280"},"PeriodicalIF":0.6,"publicationDate":"2026-08-28","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"148823124","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
A. A. Leifrid, A. V. Sidorov, D. A. Reznik, A. E. Reznik, A. V. Chertenkov, V. S. Frolov, A. A. Bobrovnikova
{"title":"Polyacrylates in the Coal Industry: Their Antifreeze Action and Potential Application","authors":"A. A. Leifrid, A. V. Sidorov, D. A. Reznik, A. E. Reznik, A. V. Chertenkov, V. S. Frolov, A. A. Bobrovnikova","doi":"10.3103/S1068364X26600454","DOIUrl":"10.3103/S1068364X26600454","url":null,"abstract":"<p>In cold climates, the freezing of coal and coal concentrates on transportation in winter is a serious problem. In that context, the properties of polyacrylates—in particular, sodium polyacrylate—and the basis of their antifreeze action—essentially, high water absorption and the formation of a gel structure—are studied in detail in the present work. The sorbent Minex B95, which absorbs and binds free moisture and prevents the formation of a monolithic ice structure in the coal mass, is recommended. The technology for dosing the polymer and its consumption standards are described, and its minimal environmental impact and influence on coal quality are confirmed. Comparison with traditional antifreeze methods shows the economic and operational benefits of the proposed sorbent. The introduction of polyacrylates to ensure uninterrupted operation of the coal industry in severe climates is highly effective and of great strategic importance.</p>","PeriodicalId":519,"journal":{"name":"Coke and Chemistry","volume":"69 5","pages":"281 - 285"},"PeriodicalIF":0.6,"publicationDate":"2026-08-28","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"148823068","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
{"title":"Production, Characterization and Application of Mesophase Pitches Based on Residual Hydrocarbon Fractions: A Review of Modern Concepts","authors":"R. R. Gabdulkhakov, P. V. Spasiuk, T. G. Utenkova","doi":"10.3103/S1068364X26600314","DOIUrl":"10.3103/S1068364X26600314","url":null,"abstract":"<p>Mesophase pitch is a complex hydrocarbon dispersion system dominated by a liquid-crystalline phase, which forms during the thermolysis of polycyclic aromatic compounds at temperatures above 380°C. The properties of the mesophase vary significantly depending on the composition of the feedstock, the parameters of the pitch production process, and other factors. The mesophase optical texture, its proportion in the pitch determine the performance characteristics of the material, which necessitates reliable differentiation between different types of mesophase. Mesophase pitch is widely used to produce high-tech carbon materials, whereby the requirements for it depends on resulting material. Systematic approaches to differentiating types of mesophase pitch based on their properties remain insufficiently developed. In this regard, this study proposes a comprehensive methodological approach aimed at identifying and differentiating various types of mesophase, establishing a relationship between feedstock composition, the mechanism of mesophase formation, and the properties of pitches. The role of different classes of compounds in the feedstock and their influence on the mesophase formation mechanism are evaluated, which in the long term enables the adaptation of various feedstock types for producing pitches with different intended uses. The optimal feedstock composition for producing mesophase pitch is determined, and quantitative and qualitative evaluation criteria are developed to enable the differentiation of mesophase pitches by their fields of practical application. Requirements for mesophase pitch depending on the target product are compiled and systematized. This form a scientific foundation for characterizing mesophase pitches as an intermediate stage in the production of carbon materials from hydrocarbon residues.</p>","PeriodicalId":519,"journal":{"name":"Coke and Chemistry","volume":"69 4","pages":"229 - 260"},"PeriodicalIF":0.6,"publicationDate":"2026-07-21","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"148519520","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
N. S. Zakharov, G. Yu. Simenyuk, T. S. Nechaeva, T. O. Sergina, V. I. Krasheninin
{"title":"Charge Storage in Activated Sapropelic Coal with KOH and H2SO4 Electrolytes","authors":"N. S. Zakharov, G. Yu. Simenyuk, T. S. Nechaeva, T. O. Sergina, V. I. Krasheninin","doi":"10.3103/S1068364X2660034X","DOIUrl":"10.3103/S1068364X2660034X","url":null,"abstract":"<p>The electrochemical characteristics and charge storage mechanisms of activated sapropelic coal in alkaline (6 M KOH) and acidic (4 M H<sub>2</sub>SO<sub>4</sub>) electrolytes are compared. The type of electrolyte determines the dominant energy storage mechanism, as established by cyclic voltammetry, galvanostatic charging and discharging (at a current density of 35.7 mA/cm<sup>2</sup>), and electrochemical impedance spectroscopy. The maximum unit capacitance (164.8 F/g) and energy (5.72 W h/kg) are recorded in sulfuric acid; that may be attributed to synergy between the capacitance of the double electric layer and the contribution of the fast pseudocapacitance of surface functional groups. Analysis of the impedance spectra reveals no significant diffusional constraints for protons in the coal’s pore structure, whereas substantial Warburg impedance is observed in the alkaline medium on account of the hindered migration of hydrated potassium ions. Despite lower unit capacitance in KOH electrolyte (98.7 F/g), the power density obtained (250 kW/kg) is comparable with that in sulfuric acid. We conclude that, for the chosen current density, the surface of the material is characterized by high kinetic accessibility for ions of both types. It follows from the low internal resistance (1.2 Ω) and high electronic conductivity of the material in both media that activated sapropelic coal is promising as a versatile basis for highly efficient supercapacitors.</p>","PeriodicalId":519,"journal":{"name":"Coke and Chemistry","volume":"69 4","pages":"194 - 198"},"PeriodicalIF":0.6,"publicationDate":"2026-07-21","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"148519521","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
{"title":"Synchronous Thermal Analysis of Commercial Petroleum Coke Samples","authors":"S. A. Sozinov, A. N. Prigorodova, N. S. Zakharov","doi":"10.3103/S1068364X26600375","DOIUrl":"10.3103/S1068364X26600375","url":null,"abstract":"<p>The pyrolysis of two series of commercial petroleum coke samples that differ significantly in microstructure—isotropic coke and needle coke—is studied by synchronous thermal analysis in combination with mass spectrometry of the gases produced. The particle size (1–2 mm) has the key influence on the thermolysis in a thermogravimetric experiment; on that basis, the structure-dependent aspects of the process may be identified. Isotropic coke is characterized by intense decomposition at lower temperatures (beginning at ~521°C) and considerable total mass loss (14.9%), whereas the thermal stability of needle coke is higher, with maximum losses at ~767°C and total mass losses of around 5%. Mass spectroscopy shows that isotropic coke is less aromatic, as indicated by the more intense CH<sub>4</sub> and H<sub>2</sub> liberation at low temperatures. Clear differences in the temperature profiles of gas liberation (CO<sub>2</sub>, CH<sub>4</sub>, H<sub>2</sub>) in pyrolysis correlate with the chemical composition and morphology of the coke. Thus, by thermogravimetric analysis and mass spectrometry of the gases produced, a direct relationship may be established between the microstructure of the petroleum coke and the kinetics of thermal decomposition. That permits prediction of its behavior in subsequent heat treatment.</p>","PeriodicalId":519,"journal":{"name":"Coke and Chemistry","volume":"69 4","pages":"209 - 216"},"PeriodicalIF":0.6,"publicationDate":"2026-07-21","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"148519517","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
A. T. Ordabaeva, Z. M. Muldakhmetov, M. G. Meiramov, S. V. Kim, Ya. A. Visurkhanova
{"title":"Catalytic Processing of a Phenolic Concentrate of Recycled Coke Plant Water","authors":"A. T. Ordabaeva, Z. M. Muldakhmetov, M. G. Meiramov, S. V. Kim, Ya. A. Visurkhanova","doi":"10.3103/S1068364X26600387","DOIUrl":"10.3103/S1068364X26600387","url":null,"abstract":"<p>The composition of a phenolic concentrate of recycled water from Shubarkol Kumir coke plant formed when water is exposed to gases produced in coking is studied. Gas–liquid chromatography permits the identification of 17 phenolic compounds (91.82 wt % of the total phenolic concentrate). The phenolic extract is obtained using a mixture of benzene and ethyl acetate. In hydration of the phenolic extract, the synthetic catalysts Co/C, Fe<sub>2</sub>O<sub>3</sub>/C, Fe–Co/C, and NiO/C are employed. Of these, Co/C ensures the greatest yield of benzene (10.24%), methyl cyclohexane (11.9%), toluene (5.73%), and mixed xylene isomers (3.84%). Thus, the catalytic hydration of a phenolic extract containing phenol and its alkyl-substituted derivatives to obtain aromatic hydrocarbons (benzene, toluene, and xylenes) and methyl cyclohexane is a promising disposal method: it reduces the plant’s environmental impact and yields materials that are in demand for the petrochemical and polymer industries.</p>","PeriodicalId":519,"journal":{"name":"Coke and Chemistry","volume":"69 4","pages":"217 - 222"},"PeriodicalIF":0.6,"publicationDate":"2026-07-21","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"148519524","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
{"title":"Semicoking of Lignite under Pressure","authors":"S. R. Islamov, D. A. Loginov, A. P. Chernykh","doi":"10.3103/S1068364X26600363","DOIUrl":"10.3103/S1068364X26600363","url":null,"abstract":"<p>Quality requirements on coal for power generation and for industry are increasing rapidly at present, with rise in calorific value to 7000 kcal/kg. In most cases, classical coal enrichment cannot affordably meet those standards. A possible alternative is thermal processing of low-ash lignite under pressure. The target products are high-pressure semicoke and combustible gas. This technology is economical and has low environmental impact. Semicoke is primarily used as a highly reactive reducing agent for steelmaking.</p>","PeriodicalId":519,"journal":{"name":"Coke and Chemistry","volume":"69 4","pages":"205 - 208"},"PeriodicalIF":0.6,"publicationDate":"2026-07-21","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"148519522","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
{"title":"World Market for Metallurgical Coal: 2025 Data and 2026 Prospects","authors":"S. V. Nedelin, S. V. Myasoyedov, P. I. Chernousov","doi":"10.3103/S1068364X26600326","DOIUrl":"10.3103/S1068364X26600326","url":null,"abstract":"<p>According to 2025 data, world exports of metallurgical coal amounted to 325 million t. Australia was the largest exporter, although its share of the total was no more than 45%. Recently, exports from Mongolia have grown most rapidly, thanks to the development of rail lines in collaboration with China. According to estimates, the top five exporters—China, India, Japan, the European Community, and South Korea—account for about 85–90% of the world trade in metallurgical coal. Supplies in China may remain unchanged in 2026. The lack of a free trade agreement between Russia and China puts Russia at a competitive disadvantage to Australia and Indonesia in terms of coal supplies to China because of import duties. Crude steel production in India increased by 10% between 2024 and 2025, reaching 164 million t. Australia contributes 54% of India’s imports, although its share has fallen as imports from Russia and the United States have increased. In Russia, the cost of average coking batch (in rubles) fell by 25% on account of weak internal and export markets for steel and the drop in coke production. The strong ruble reduces the ruble netback of Russian exporters—that is, the portion of export revenue that remains in rubles after accounting for foreign exchange sales and export duties. Despite the growth in world prices for high-quality coking coal, the strong ruble and expanding logistics often reduce export parity below producers’ costs.</p>","PeriodicalId":519,"journal":{"name":"Coke and Chemistry","volume":"69 4","pages":"183 - 187"},"PeriodicalIF":0.6,"publicationDate":"2026-07-21","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"148519518","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
V. A. Naletov, M. B. Glebov, A. Yu. Naletov, N. N. Karzaeva, V. A. Vasilenko
{"title":"Optimization of Coke Plant Heating System To Ensure More Intense Heat Transfer and Smaller Temperature Gradients in Coke Oven Walls","authors":"V. A. Naletov, M. B. Glebov, A. Yu. Naletov, N. N. Karzaeva, V. A. Vasilenko","doi":"10.3103/S1068364X26600399","DOIUrl":"10.3103/S1068364X26600399","url":null,"abstract":"<div><p>Optimal organization of heating systems at coke plants is considered, for the example of the coke ovens at Moskoks. In the proposed approach, the heat transfer is intensified, and the temperature gradient over the height of the heating walls in the furnace chamber is increased. To that end, superheated steam is supplied together with air to the regenerator in the ascending line and then to the fuel combustion zone. Computational experiments show that, on supplying steam in different quantities, more heat is transferred from the gas to the wall adjacent to the coke cake, and the temperature gradient over the height of the heating channels in the chamber wall decreases. To ensure optimal organization of the heating system, the supply of steam to the heating channels at a rate of 122.70 m<sup>3</sup>/h is recommended. That corresponds to the greatest heat transfer coefficient.</p></div>","PeriodicalId":519,"journal":{"name":"Coke and Chemistry","volume":"69 4","pages":"223 - 228"},"PeriodicalIF":0.6,"publicationDate":"2026-07-21","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"148519523","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}