• Title/Summary/Keyword: Deasphalted oil

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Extraction of Deasphalted Oil from Vacuum Residue (감압잔사유로부터 탈아스팔트오일의 추출)

  • 백일현;김춘호;김성현;김영일;홍성선
    • Journal of Energy Engineering
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    • v.2 no.1
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    • pp.68-74
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    • 1993
  • In order to maximize the utility of vacuum residue, supercritical solvent extraction technique where n-pentane was used as a supercritical solvent was applied to obtain deasphalted oil from vacuum residue. Oil-extraction yield at various temperatures and pressures and the contents of metal complex and sulfur of extracted oil were investigated. In supercritical state, extraction yield of deasphalted oil was found to be strongly dependent on the n-pentane density, and the metal complex content of extracted oil was effectively lowered when compared with that of vacuum residue. However, the sulfur content of extracted oil showed little difference when compared with that of vacuum residue.

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Study on the Pyrolysis Kinetics of Deasphalted Oil Using Thermogravimetric Analysis (열중량 분석법을 이용한 Deasphalted Oil의 열분해 특성 분석)

  • Shin, Sang Cheol;Lee, Jung Moo;Lee, Ki Bong;Jeon, Sang Goo;Na, Jeong Geol;Nho, Nam Sun
    • Korean Chemical Engineering Research
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    • v.50 no.3
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    • pp.391-397
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    • 2012
  • The depletion of conventional oil reserves and the increasing energy need in developing countries such as China and India result in exceeding oil demand over supply. As a solution of the problem, the efficient utilization of heavy oil has been receiving more and more interest. In order to utilize heavy oil, upgrading processes are required. Among the upgrading processes, thermal decomposition is thought to be relatively simple and economical. In this study, to understand basic characteristics of thermal decomposition of heavy oil, we conducted pyrolysis experiments of deasphalted oil (DAO) produced by a solvent deasphalting process. DAO is a mixture of many components and consists mainly of materials of carbon number 20~40. For the comparison with results of DAO pyrolysis, additional pyrolysis experiments with single materials of carbon number 30 ($C_{30}H_{62}$, $C_{30}H_{58}O_4S$, $C_{30}H_{63}O_3P$) were conducted. Pyrolysis experiments were carried out non-isothermally with variation of heating rate (10, 50, $100^{\circ}C$/min) in a thermogravimetric analyzer. Average pyrolysis activation energy determined by using Arrhenius method, Ingraham and Marrier method, and Coats and Redfern method was 72~99 kJ/mol. In the activation energy calculated by Ozawa-Flynn-Wall method, DAO had wider variation than other single materials.

Separation of Deasphalted Oil from Atmospheric Residue Using Continuous Feeding System (Continuous feeding system을 이용한 상압 잔사유로부터 탈아스팔트오일 분리)

  • Baek, Il-Hyun;Kim, Choon-Ho;Kim, Sung-Hyun;Kim, Young-Il;Hong, Sung-Sun
    • Applied Chemistry for Engineering
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    • v.4 no.3
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    • pp.515-521
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    • 1993
  • Separation of deasphalted oil from atmospheric residue using n-pentane as a solvent was carried out to obtain the valuable heavy hydrocarbon products that can be used lube base oil. After separation experiments, it is shown that the separation yield of oil from atmospheric residue was dependent on n-pentane density and increased in the critical region of n-pentane. Also, the metal content of separated oil was much lowered when compared with that of atmospheric residue. However, there's slight differences in sulfur removal between above two cases.

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Patent Analysis of SDA Technology for Heavy Oil Upgrading (중질유 고부가화를 위한 SDA 개발 기술의 특허 정보 분석)

  • Kim, Yong-Heon;Lee, Won-Su;Kim, Jae-Ho;Jeon, Sang-Goo;Na, Jeong-Geol;Nho, Nam-Sun;Lee, Ki-Bong
    • Applied Chemistry for Engineering
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    • v.21 no.4
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    • pp.372-376
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    • 2010
  • Non-conventional energy is considered as important future energy source, as conventional energy has limitation for its capacity. The demand on value added process in heavy oil/oil sand bitumen is increasing in particular. Solvent Deasphalting (SDA) process for Deasphalted Oil (DAO) is used as heavy oil upgrading process in existing refinery process. SDA process for heavy oil upgrading has been already commercialized by leading countries. SDA R&D projects have been carried out actively by those countries. In this study, patent analysis for SDA technology development was carried out. From 1970's, when SDA patents were applied, the patents in Korea, USA, Japan, Canada and Europe were searched and distributed to extraction, recovery, solvent and etc. 334 patents were selected relating to heavy oil upgrading SDA process. The application status of SDA process patents showed a tendency to increase slightly. The number of patent applied was USA patent 131 (39%), Canada patent 83 (25%), Japan patent 35 (11%) and Korea patent 6 (2%). It will be necessary for efficient use of energy resource to support SDA R&D by government.