Pub Date : 2023-10-23DOI: 10.3103/S1068364X23700989
Yu. V. Gavrilov, A. Yu. Naletov, E. N. Mikhailova, G. S. Savin
This article is devoted to exergetic analysis of the pyrolysis of propane–butane mixture, with the production of hydrogen and carbon nanofiber. The process is studied on laboratory equipment, with subsequent assessment of the prospects for its adoption on an industrial scale. The exergy balance is calculated for each stage of the process on the basis of laboratory data. The exergy losses for the stages of periodic pyrolysis of propane–butane mixture are found to be very high. That corresponds to low efficiency of the experimental apparatus. The results may be used to study the kinetic laws of the process, so as to assess the options for its larger-scale introduction (the scalability of the process). It is expedient to develop practical methods for the process itself and for each stage on an industrial scale.
{"title":"Production of Hydrogen and Carbon Nanofiber by Catalytic Pyrolysis of Propane–Butane Mixture: Prospects for Large-Scale Introduction","authors":"Yu. V. Gavrilov, A. Yu. Naletov, E. N. Mikhailova, G. S. Savin","doi":"10.3103/S1068364X23700989","DOIUrl":"10.3103/S1068364X23700989","url":null,"abstract":"<div><p>This article is devoted to exergetic analysis of the pyrolysis of propane–butane mixture, with the production of hydrogen and carbon nanofiber. The process is studied on laboratory equipment, with subsequent assessment of the prospects for its adoption on an industrial scale. The exergy balance is calculated for each stage of the process on the basis of laboratory data. The exergy losses for the stages of periodic pyrolysis of propane–butane mixture are found to be very high. That corresponds to low efficiency of the experimental apparatus. The results may be used to study the kinetic laws of the process, so as to assess the options for its larger-scale introduction (the scalability of the process). It is expedient to develop practical methods for the process itself and for each stage on an industrial scale.</p></div>","PeriodicalId":519,"journal":{"name":"Coke and Chemistry","volume":null,"pages":null},"PeriodicalIF":0.4,"publicationDate":"2023-10-23","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"71909866","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}
Pub Date : 2023-10-23DOI: 10.3103/S1068364X23700953
Nurlan Dosmukhamedov, Erzhan Zholdasbay, Maksut Egizekov, Murat Kurmanseitov
The paper highlights the issues of thermal decomposition of aluminum chloride hexahydrate which is applied to the integrated technology of ash processing from the combustion of Ekibastuz coal. To solve this problem the possibility of using thermal decomposition of AlCl3·6H2O crystals in a static state and in a fluidized bed is considered. This approach allowed conducting a comparative assessment and selection of the most rational method for the thermal decomposition of ACH from a technological and economic point of view. It was found that under the conditions of thermal decomposition of ACH in a static state, its maximum decomposition to Al2O3 is achieved at a temperature of 400°C. The residual chlorine content in alumina is 1.09%, and aluminum in the form of AlCl3 is 0.5% of the total aluminum content. At a temperature of 500°C, the residual chlorine content in alumina is 0.71%, and AlCl3 is practically not detected. It was found that crystals of AlCl3·6H2O almost completely decompose in a fluidized bed at a temperature of 500°C (residual chlorine content 0.75%). In this case, the degree of decomposition of AlCl3·6H2O crystals was 87% at 300°C and 95% at 400°C. After calcining the samples obtained at 900°C, the residual chlorine content in them decreased to 0.27%, and after calcining at temperatures above 1000°C, no chlorine was detected in the samples at all. The specific surface area of alumina obtained after thermal decomposition at 400°C was 169.6 m2/g. After additional roasting of the sample at a temperature of 1200°C, the specific surface area of alumina decreased to 7.8 m2/g.
{"title":"Thermal Decomposition of Aluminum Chloride Hexahydrate to Produce Aluminum Oxide","authors":"Nurlan Dosmukhamedov, Erzhan Zholdasbay, Maksut Egizekov, Murat Kurmanseitov","doi":"10.3103/S1068364X23700953","DOIUrl":"10.3103/S1068364X23700953","url":null,"abstract":"<p>The paper highlights the issues of thermal decomposition of aluminum chloride hexahydrate which is applied to the integrated technology of ash processing from the combustion of Ekibastuz coal. To solve this problem the possibility of using thermal decomposition of AlCl<sub>3</sub>·6H<sub>2</sub>O crystals in a static state and in a fluidized bed is considered. This approach allowed conducting a comparative assessment and selection of the most rational method for the thermal decomposition of ACH from a technological and economic point of view. It was found that under the conditions of thermal decomposition of ACH in a static state, its maximum decomposition to Al<sub>2</sub>O<sub>3</sub> is achieved at a temperature of 400°C. The residual chlorine content in alumina is 1.09%, and aluminum in the form of AlCl<sub>3</sub> is 0.5% of the total aluminum content. At a temperature of 500°C, the residual chlorine content in alumina is 0.71%, and AlCl<sub>3</sub> is practically not detected. It was found that crystals of AlCl<sub>3</sub>·6H<sub>2</sub>O almost completely decompose in a fluidized bed at a temperature of 500°C (residual chlorine content 0.75%). In this case, the degree of decomposition of AlCl<sub>3</sub>·6H<sub>2</sub>O crystals was 87% at 300°C and 95% at 400°C. After calcining the samples obtained at 900°C, the residual chlorine content in them decreased to 0.27%, and after calcining at temperatures above 1000°C, no chlorine was detected in the samples at all. The specific surface area of alumina obtained after thermal decomposition at 400°C was 169.6 m<sup>2</sup>/g. After additional roasting of the sample at a temperature of 1200°C, the specific surface area of alumina decreased to 7.8 m<sup>2</sup>/g.</p>","PeriodicalId":519,"journal":{"name":"Coke and Chemistry","volume":null,"pages":null},"PeriodicalIF":0.4,"publicationDate":"2023-10-23","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"71909867","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}
Pub Date : 2023-10-01DOI: 10.3103/s1068364x23701193
Abstract
The possibility of extracting vanadium from various carbon materials (petroleum coke, bitumen, fuel-oil ash and slag, ash from foundry graphite, black shale, and lignite) is investigated. Systems for producing vanadium slag from ash and from titanomagnetite ore are compared. The two types of slag are compared in terms of phase composition, chemical composition, and content of soluble forms of vanadium. In experimental melts, a vanadium alloy and vanadium slag are obtained. The potential for extracting vanadium from carbon materials is demonstrated.
{"title":"Carbon Materials as a Source of Vanadium","authors":"","doi":"10.3103/s1068364x23701193","DOIUrl":"https://doi.org/10.3103/s1068364x23701193","url":null,"abstract":"<h3>Abstract</h3> <p>The possibility of extracting vanadium from various carbon materials (petroleum coke, bitumen, fuel-oil ash and slag, ash from foundry graphite, black shale, and lignite) is investigated. Systems for producing vanadium slag from ash and from titanomagnetite ore are compared. The two types of slag are compared in terms of phase composition, chemical composition, and content of soluble forms of vanadium. In experimental melts, a vanadium alloy and vanadium slag are obtained. The potential for extracting vanadium from carbon materials is demonstrated.</p>","PeriodicalId":519,"journal":{"name":"Coke and Chemistry","volume":null,"pages":null},"PeriodicalIF":0.4,"publicationDate":"2023-10-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"139769724","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}
Pub Date : 2023-09-13DOI: 10.3103/S1068364X23700886
I. S. Bersenev, S. I. Pokolenko, A. D. Nikitin, N. A. Spirin
The objective of this paper is to learn the possibilities of using biofuel to ensure the heating of indurating machines and assess its impact on the volume of emissions. The main source of fuel was sunflower husk, which can be used in pellet production by the following means: the firing and utilization of fume laden gas as a heat carrier during drying of blend materials and the gasification and utilization of syngas as the fuel in order to heat the indurating machines while thermally treating the pellets. Mathematical simulation was adopted as the research methodology. The results reveal that using biofuel to heat indurating machines during the pelletizing process is technologically feasible. However, there are numerous constraints that are mainly related to environmental issues and logistics. In the course of firing, husk generates additional solid waste and sulfur oxide, although, from the perspective of ESG statistics, it leads to a reduction in the carbon footprint of the end products. Issues related to the handling and storage of biofuel are caused by its aggregate state (solid), low bulk weight, and relatively low calorific value. The abovementioned parameters make biofuel a less favorable source of fuel when compared with natural gas. The aspects of biofuel application shall be considered when planning “energy transition” activities, since they affect economic viability, along with the environment of industrial regions (and the quality of life of inhabitants as well).
{"title":"The Use of Biofuel in Pellet Production","authors":"I. S. Bersenev, S. I. Pokolenko, A. D. Nikitin, N. A. Spirin","doi":"10.3103/S1068364X23700886","DOIUrl":"10.3103/S1068364X23700886","url":null,"abstract":"<p>The objective of this paper is to learn the possibilities of using biofuel to ensure the heating of indurating machines and assess its impact on the volume of emissions. The main source of fuel was sunflower husk, which can be used in pellet production by the following means: the firing and utilization of fume laden gas as a heat carrier during drying of blend materials and the gasification and utilization of syngas as the fuel in order to heat the indurating machines while thermally treating the pellets. Mathematical simulation was adopted as the research methodology. The results reveal that using biofuel to heat indurating machines during the pelletizing process is technologically feasible. However, there are numerous constraints that are mainly related to environmental issues and logistics. In the course of firing, husk generates additional solid waste and sulfur oxide, although, from the perspective of ESG statistics, it leads to a reduction in the carbon footprint of the end products. Issues related to the handling and storage of biofuel are caused by its aggregate state (solid), low bulk weight, and relatively low calorific value. The abovementioned parameters make biofuel a less favorable source of fuel when compared with natural gas. The aspects of biofuel application shall be considered when planning “energy transition” activities, since they affect economic viability, along with the environment of industrial regions (and the quality of life of inhabitants as well).</p>","PeriodicalId":519,"journal":{"name":"Coke and Chemistry","volume":null,"pages":null},"PeriodicalIF":0.4,"publicationDate":"2023-09-13","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"6713745","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}
The combustion behaviors of semi-coke, anthracite, bituminous coal and their blends were studied using a thermogravimetric analyzer. Compared with anthracite, the experiments showed that semi-coke had low ignition temperature, good comprehensive combustion characteristics and high burnout rate. In compound samples, with the increase of SC1 semi-coke content, the ignition temperature of BC bituminous coal, IC mixed sample and SC1 compound samples gradually decreased, and the comprehensive combustion characteristic index S increased, and the TG curves of the compound samples moved to the low temperature. In the BC and IC compound sample, the ignition temperature and comprehensive combustion characteristic index of compound samples also improved with the addition of SC2 semi-coke and SC3 semi-coke. Furthermore, By means of the universal integral method, the results indicated that the shrinkage cylinder model of phase boundary reaction was the most probable mechanism function of semi-coke, anthracite and bituminous coal combustion. The kinetic parameters of the samples are obtained that the activation energy of semi-coke was lower than that of anthracite. In summary, mixing semi-coke with pulverized coal into blast furnace was beneficial to fuel combustion.
{"title":"Study on Combustion Characteristics and Kinetics of Coal and Semi-Coke Injected by Blast Furnace","authors":"Huining Wei, Shijie Wang, Hongming Fang, Zichun Guo, Weijing Guo, Bihan Gu","doi":"10.3103/S1068364X23700837","DOIUrl":"10.3103/S1068364X23700837","url":null,"abstract":"<p>The combustion behaviors of semi-coke, anthracite, bituminous coal and their blends were studied using a thermogravimetric analyzer. Compared with anthracite, the experiments showed that semi-coke had low ignition temperature, good comprehensive combustion characteristics and high burnout rate. In compound samples, with the increase of SC1 semi-coke content, the ignition temperature of BC bituminous coal, IC mixed sample and SC1 compound samples gradually decreased, and the comprehensive combustion characteristic index S increased, and the TG curves of the compound samples moved to the low temperature. In the BC and IC compound sample, the ignition temperature and comprehensive combustion characteristic index of compound samples also improved with the addition of SC2 semi-coke and SC3 semi-coke. Furthermore, By means of the universal integral method, the results indicated that the shrinkage cylinder model of phase boundary reaction was the most probable mechanism function of semi-coke, anthracite and bituminous coal combustion. The kinetic parameters of the samples are obtained that the activation energy of semi-coke was lower than that of anthracite. In summary, mixing semi-coke with pulverized coal into blast furnace was beneficial to fuel combustion.</p>","PeriodicalId":519,"journal":{"name":"Coke and Chemistry","volume":null,"pages":null},"PeriodicalIF":0.4,"publicationDate":"2023-09-13","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"6713692","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}
An increasing number of coking enterprises are challenged by excessive sulfur content in their crude benzene products, which hinders sales and revenue. In this work, microcrystalline adsorbent was used to remove carbon disulfide and thiophene in crude benzene. BET, XRD, XRF and SEM characterization showed that the microcrystalline adsorbent has a large specific surface area, high crystallinity morphology, Si/Al ratio and regeneration stability. By investigating the effects of adsorption time, temperature, adsorbent dosage and regeneration times on the desulfurization performance of microcrystalline adsorbent W1, it was found that the desulfurization effect was mainly affected by time and temperature. When the experimental conditions at 20°C, 7 h, the amount of adsorbent was 4.5 g, the volume of crude benzene was 10 mL, resulting in desulfurization rate of 67% for thiophene, 52% for carbon disulfide, and 62% for total desulfurization, approximately 26% for crude benzene loss rate. The overall desulfurization rate remained stable around 55% after three regenerations, while the rate for rude benzene loss increased to roughly 30%. The results indicate that the microcrystalline adsorbent exhibits significant potential for desulfurization of crude benzene, providing valuable guidance and reference for coking enterprises.
{"title":"Study on Desulfurization of Crude Benzene with Microcrystalline Adsorbent","authors":"Zichun Guo, Shijie Wang, Hongming Fang, Huining Wei, Hui Li, Jiaqi Yan","doi":"10.3103/S1068364X23700916","DOIUrl":"10.3103/S1068364X23700916","url":null,"abstract":"<p>An increasing number of coking enterprises are challenged by excessive sulfur content in their crude benzene products, which hinders sales and revenue. In this work, microcrystalline adsorbent was used to remove carbon disulfide and thiophene in crude benzene. BET, XRD, XRF and SEM characterization showed that the microcrystalline adsorbent has a large specific surface area, high crystallinity morphology, Si/Al ratio and regeneration stability. By investigating the effects of adsorption time, temperature, adsorbent dosage and regeneration times on the desulfurization performance of microcrystalline adsorbent W1, it was found that the desulfurization effect was mainly affected by time and temperature. When the experimental conditions at 20°C, 7 h, the amount of adsorbent was 4.5 g, the volume of crude benzene was 10 mL, resulting in desulfurization rate of 67% for thiophene, 52% for carbon disulfide, and 62% for total desulfurization, approximately 26% for crude benzene loss rate. The overall desulfurization rate remained stable around 55% after three regenerations, while the rate for rude benzene loss increased to roughly 30%. The results indicate that the microcrystalline adsorbent exhibits significant potential for desulfurization of crude benzene, providing valuable guidance and reference for coking enterprises.</p>","PeriodicalId":519,"journal":{"name":"Coke and Chemistry","volume":null,"pages":null},"PeriodicalIF":0.4,"publicationDate":"2023-09-13","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"6713691","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}
Pub Date : 2023-09-13DOI: 10.3103/S1068364X23700862
V. I. Ekgauz, K. V. Pokrishkin, N. V. Dementeva
The literature regarding deposits formed during the transportation and processing of coke oven gas in byproduct capture shops at coke plants is reviewed. The development of deposits is described, and methods of preventing their formation in gas lines and equipment are discussed.
{"title":"Deposits in Coke Oven Gas Lines and Equipment at Coke Plants: A Review","authors":"V. I. Ekgauz, K. V. Pokrishkin, N. V. Dementeva","doi":"10.3103/S1068364X23700862","DOIUrl":"10.3103/S1068364X23700862","url":null,"abstract":"<div><p>The literature regarding deposits formed during the transportation and processing of coke oven gas in byproduct capture shops at coke plants is reviewed. The development of deposits is described, and methods of preventing their formation in gas lines and equipment are discussed.</p></div>","PeriodicalId":519,"journal":{"name":"Coke and Chemistry","volume":null,"pages":null},"PeriodicalIF":0.4,"publicationDate":"2023-09-13","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"6713743","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}
Pub Date : 2023-09-13DOI: 10.3103/S1068364X23700898
N. A. Krasulin, T. G. Cherkasova, V. S. Solodov, V. A. Klimchuk, S. P. Subbotin
In coal coking, volatile products are liberated. As a result, deposits of pyrocarbon (graphite) are formed on the walls and roof of the coke ovens. Those deposits may obstruct the extraction of coke cake. By identifying the parameters with the greatest effect on the formation of pyrocarbon, its growth in the coke ovens may be more accurately monitored, and hence the coke plant’s stock of coke ovens may be better maintained. The influence of the following factors on the rate of pyrocarbon formation is investigated: the metamorphic development of the coal; its moisture content; and its granulometric composition.
{"title":"Formation of Pyrocarbon in the Laboratory Coking of Coal","authors":"N. A. Krasulin, T. G. Cherkasova, V. S. Solodov, V. A. Klimchuk, S. P. Subbotin","doi":"10.3103/S1068364X23700898","DOIUrl":"10.3103/S1068364X23700898","url":null,"abstract":"<div><p>In coal coking, volatile products are liberated. As a result, deposits of pyrocarbon (graphite) are formed on the walls and roof of the coke ovens. Those deposits may obstruct the extraction of coke cake. By identifying the parameters with the greatest effect on the formation of pyrocarbon, its growth in the coke ovens may be more accurately monitored, and hence the coke plant’s stock of coke ovens may be better maintained. The influence of the following factors on the rate of pyrocarbon formation is investigated: the metamorphic development of the coal; its moisture content; and its granulometric composition.</p></div>","PeriodicalId":519,"journal":{"name":"Coke and Chemistry","volume":null,"pages":null},"PeriodicalIF":0.4,"publicationDate":"2023-09-13","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"6713768","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}
Pub Date : 2023-09-13DOI: 10.3103/S1068364X23700874
V. Z. Abdrakhimov
Lightweight brick based on waste from nonferrous metallurgy is produced using slag and ash from power plants, with no traditional raw materials. The nonferrous waste is the clay component of the gravitational tailings from zircon–ilmenite ore. Adding the optimal quantity (40%) of slag and ash (calorific value 2100 kcal/kg; carbon content 7.44%) yields M100 lightweight brick, whose low thermal conductivity means that it provides effective heat insulation. The added slag and ash facilitate the formation of mullite, which improves the mechanical strength, frost resistance, and other characteristic of the brick.
{"title":"Influence of Ash and Slag on the Characteristics of Heat Insulation Based on Metallurgical Waste","authors":"V. Z. Abdrakhimov","doi":"10.3103/S1068364X23700874","DOIUrl":"10.3103/S1068364X23700874","url":null,"abstract":"<div><p>Lightweight brick based on waste from nonferrous metallurgy is produced using slag and ash from power plants, with no traditional raw materials. The nonferrous waste is the clay component of the gravitational tailings from zircon–ilmenite ore. Adding the optimal quantity (40%) of slag and ash (calorific value 2100 kcal/kg; carbon content 7.44%) yields M100 lightweight brick, whose low thermal conductivity means that it provides effective heat insulation. The added slag and ash facilitate the formation of mullite, which improves the mechanical strength, frost resistance, and other characteristic of the brick.</p></div>","PeriodicalId":519,"journal":{"name":"Coke and Chemistry","volume":null,"pages":null},"PeriodicalIF":0.4,"publicationDate":"2023-09-13","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"6713744","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}
Pub Date : 2023-09-13DOI: 10.3103/S1068364X23700850
A. V. Zhuikov, S. G. Stepanov, D. A. Loginov
The reactivity and conditions of nonisothermal heating are investigated for biomass, coal, and semicoke (obtained by partial gasification of coal at 700–800°C) are investigated; specifically, the mean reactive index of the fuels is determined. In addition, their reactivity in convective heating by hot air is studied; the delay time in ignition is determined. Nonisothermal heating is accompanied by synchronous thermal analysis in an air flux (heating rate 20°C/min). In convective heating by an air flux (500–800°C, flow rate ~5 m/s), the experimental system includes a muffle furnace with a built in horizontal quartz tube; fuel ignition is recorded by means of a high-speed video camera. In both types of heating, biomass is the most reactive. In convective heating by hot air, the ignition delay is less for semicoke than for coal, on account of the greater surface area of the particles. In nonisothermal heating, the mean reactive index of the semicoke (1.6 min °C–1) is lower than for the biomass (7.0 min °C–1) and the coal (4.1 min °C–1). That indicates lower reactivity in the given heating conditions.
{"title":"Reactivity of Biomass, Coal, and Semicoke in Different Heating Conditions","authors":"A. V. Zhuikov, S. G. Stepanov, D. A. Loginov","doi":"10.3103/S1068364X23700850","DOIUrl":"10.3103/S1068364X23700850","url":null,"abstract":"<div><p>The reactivity and conditions of nonisothermal heating are investigated for biomass, coal, and semicoke (obtained by partial gasification of coal at 700–800°C) are investigated; specifically, the mean reactive index of the fuels is determined. In addition, their reactivity in convective heating by hot air is studied; the delay time in ignition is determined. Nonisothermal heating is accompanied by synchronous thermal analysis in an air flux (heating rate 20°C/min). In convective heating by an air flux (500–800°C, flow rate ~5 m/s), the experimental system includes a muffle furnace with a built in horizontal quartz tube; fuel ignition is recorded by means of a high-speed video camera. In both types of heating, biomass is the most reactive. In convective heating by hot air, the ignition delay is less for semicoke than for coal, on account of the greater surface area of the particles. In nonisothermal heating, the mean reactive index of the semicoke (1.6 min °C<sup>–1</sup>) is lower than for the biomass (7.0 min °C<sup>–1</sup>) and the coal (4.1 min °C<sup>–1</sup>). That indicates lower reactivity in the given heating conditions.</p></div>","PeriodicalId":519,"journal":{"name":"Coke and Chemistry","volume":null,"pages":null},"PeriodicalIF":0.4,"publicationDate":"2023-09-13","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"6713796","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}