Plasma-Chemical Processing of Fuel Oil

IF 0.4 Q4 ENGINEERING, CHEMICAL Coke and Chemistry Pub Date : 2024-08-18 DOI:10.3103/S1068364X24600489
D. V. Avramov, M. M. Rodionov, V. V. Vasilyev, E. V. Salamatova
{"title":"Plasma-Chemical Processing of Fuel Oil","authors":"D. V. Avramov,&nbsp;M. M. Rodionov,&nbsp;V. V. Vasilyev,&nbsp;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}
引用次数: 0

Abstract

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).

Abstract Image

Abstract Image

查看原文
分享 分享
微信好友 朋友圈 QQ好友 复制链接
本刊更多论文
燃油的等离子化学处理
建议采用等离子化学方法处理燃料油,处理量为 1000 公斤/小时。温和的等离子化学处理可使高沸点燃料油成分产生大量裂解。在对燃料油进行等离子化学处理并随后蒸馏液体成分时,产物为 6.7% 的气体、48.0% 的残渣、11.2% 的溶剂(从开始沸腾到 250°C)和 34.1% 的加热油(251-360°C)。加热油的蒸馏结果如下:0.3% 的气体、30.2% 的 SMT 低粘度船用燃料(251-330°C)和 3.6% 的 5 号燃油(331-360°C)。残渣的特点是渗透性为 150 dmm,软化温度(采用环球法)为 73°C。它可用于公路沥青和延迟焦化的原料。等离子化学处理 1000 千克燃料油的总耗电量约为 30-40 千瓦(包括等离子化学反应器运行时的 6-8 千瓦)。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
求助全文
约1分钟内获得全文 去求助
来源期刊
Coke and Chemistry
Coke and Chemistry ENGINEERING, CHEMICAL-
CiteScore
0.70
自引率
50.00%
发文量
36
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.
期刊最新文献
Influence of the Pyrolytic Temperature on the Carbon Structure of the α Fraction from Coal Tar Pitch: EPR and NMR Spectroscopy Using Anthracene Oil from Coal Tar in the Thermal Solvolysis of Polymers Modernization of Coke Production at Magnitogorsk Iron and Steel Works (MMK) Improvement in Heat Transfer at Coke Battery Chamber Walls Surface State of Purolate Standard Activated Carbon after Sorption of Minerals
×
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
现在去查看 取消
×
提示
确定
0
微信
客服QQ
Book学术公众号 扫码关注我们
反馈
×
意见反馈
请填写您的意见或建议
请填写您的手机或邮箱
已复制链接
已复制链接
快去分享给好友吧!
我知道了
×
扫码分享
扫码分享
Book学术官方微信
Book学术文献互助
Book学术文献互助群
群 号:481959085
Book学术
文献互助 智能选刊 最新文献 互助须知 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 Book学术 All rights reserved.
ghs 京公网安备 11010802042870号 京ICP备2023020795号-1