D. V. Avramov, M. M. Rodionov, V. V. Vasilyev, E. V. Salamatova
{"title":"燃油的等离子化学处理","authors":"D. V. Avramov, M. M. Rodionov, V. V. Vasilyev, E. V. Salamatova","doi":"10.3103/S1068364X24600489","DOIUrl":null,"url":null,"abstract":"<div><p>A plasma-chemical method is proposed for processing fuel oil, at a rate of 1000 kg/h. Mild plasma-chemical treatment results in considerable cracking of the high-boiling fuel-oil component. In plasma-chemical processing of fuel oil and subsequent distillation of the liquid components, the products are 6.7% gas, 48.0% residue, 11.2% solvent (from the onset of boiling to 250°C), and 34.1% heating oil (251–360°C). Distillation of the heating oil yields the following: 0.3% gas, 30.2% SMT low-viscosity marine fuel (251–330°C); and 3.6% number 5 fuel oil (331–360°C). The residue is characterized by penetration 150 dmm and softening temperature (by the ring and ball method) 73°C. It may be used in highway bitumen and as a raw material for delayed coking. The total power consumption in the plasma-chemical processing of 1000 kg of fuel oil is around 30–40 kW (including 6–8 kW in operation of the plasma-chemical reactor).</p></div>","PeriodicalId":519,"journal":{"name":"Coke and Chemistry","volume":"67 5","pages":"301 - 308"},"PeriodicalIF":0.4000,"publicationDate":"2024-08-18","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Plasma-Chemical Processing of Fuel Oil\",\"authors\":\"D. V. Avramov, M. M. Rodionov, V. V. Vasilyev, E. V. Salamatova\",\"doi\":\"10.3103/S1068364X24600489\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><p>A plasma-chemical method is proposed for processing fuel oil, at a rate of 1000 kg/h. Mild plasma-chemical treatment results in considerable cracking of the high-boiling fuel-oil component. In plasma-chemical processing of fuel oil and subsequent distillation of the liquid components, the products are 6.7% gas, 48.0% residue, 11.2% solvent (from the onset of boiling to 250°C), and 34.1% heating oil (251–360°C). Distillation of the heating oil yields the following: 0.3% gas, 30.2% SMT low-viscosity marine fuel (251–330°C); and 3.6% number 5 fuel oil (331–360°C). The residue is characterized by penetration 150 dmm and softening temperature (by the ring and ball method) 73°C. It may be used in highway bitumen and as a raw material for delayed coking. The total power consumption in the plasma-chemical processing of 1000 kg of fuel oil is around 30–40 kW (including 6–8 kW in operation of the plasma-chemical reactor).</p></div>\",\"PeriodicalId\":519,\"journal\":{\"name\":\"Coke and Chemistry\",\"volume\":\"67 5\",\"pages\":\"301 - 308\"},\"PeriodicalIF\":0.4000,\"publicationDate\":\"2024-08-18\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Coke and Chemistry\",\"FirstCategoryId\":\"1085\",\"ListUrlMain\":\"https://link.springer.com/article/10.3103/S1068364X24600489\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q4\",\"JCRName\":\"ENGINEERING, CHEMICAL\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Coke and Chemistry","FirstCategoryId":"1085","ListUrlMain":"https://link.springer.com/article/10.3103/S1068364X24600489","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q4","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
A plasma-chemical method is proposed for processing fuel oil, at a rate of 1000 kg/h. Mild plasma-chemical treatment results in considerable cracking of the high-boiling fuel-oil component. In plasma-chemical processing of fuel oil and subsequent distillation of the liquid components, the products are 6.7% gas, 48.0% residue, 11.2% solvent (from the onset of boiling to 250°C), and 34.1% heating oil (251–360°C). Distillation of the heating oil yields the following: 0.3% gas, 30.2% SMT low-viscosity marine fuel (251–330°C); and 3.6% number 5 fuel oil (331–360°C). The residue is characterized by penetration 150 dmm and softening temperature (by the ring and ball method) 73°C. It may be used in highway bitumen and as a raw material for delayed coking. The total power consumption in the plasma-chemical processing of 1000 kg of fuel oil is around 30–40 kW (including 6–8 kW in operation of the plasma-chemical reactor).
期刊介绍：
The journal publishes scientific developments and applications in the field of coal beneficiation and preparation for coking, coking processes, design of coking ovens and equipment, by-product recovery, automation of technological processes, ecology and economics. It also presents indispensable information on the scientific events devoted to thermal rectification, use of smokeless coal as an energy source, and manufacture of different liquid and solid chemical products.
求助内容：
应助结果提醒方式：
京公网安备 11010802042870号
