Optimization of Catalyst Hydrogenation Technology for White Oil Production Based on Medium Pressure Hydrogenation

被引:0
|
作者
Rui Yu
Guangfa Miao
Hua Liu
Xueqin Han
机构
[1] Dongying Junyuan Petroleum Technology Development Company,
[2] Dongying Non-public Economy Development Promotion Center,undefined
来源
Chemistry and Technology of Fuels and Oils | 2023年 / 59卷
关键词
white oil; hydrogenation technology; hydrogenation catalyst; reaction temperature; liquid space velocity;
D O I
暂无
中图分类号
学科分类号
摘要
Because the requirements of environmental protection are becoming strict, the preparation of petroleum products such as white oil needs to be harmless. In order to produce high-grade white oil products, it is necessary to study the medium-pressure hydrogenation technology and the suitable high-activity hydrogenation catalyst. The medium-pressure hydrogenation technology is proposed to produce white oil by a one-stage hydrogenation process under 7-8 MPa hydrogen partial pressure. The paper optimized the optimum conditions for medium-pressure hydrogenation of white oil. The initial reaction temperature was 210°C. The reaction pressure was 8 MPa. The liquid space velocity was 0.4 h-1. The hydrogen oil ratio was 500:1 V/V. The catalyst life evaluation experiment was carried out. The research results can provide a basis for the selection of hydrogenation catalysts.
引用
收藏
页码:1070 / 1078
页数:8
相关论文
共 50 条
  • [31] Simulation, exergy analysis and optimization of a shale oil hydrogenation process for clean fuels production
    Luo, Xiaoman
    Guo, Qi
    Zhang, Dawei
    Zhou, Huairong
    Yang, Qingchun
    APPLIED THERMAL ENGINEERING, 2018, 140 : 102 - 111
  • [32] STUDIES ON THE HYDROGENATION OF FATTY OILS .2. HYDROGENATION OF FINBACK WHALE OIL AND SOY BEAN OIL BY H ADKINS CATALYST
    MIYAKE, R
    YAKUGAKU ZASSHI-JOURNAL OF THE PHARMACEUTICAL SOCIETY OF JAPAN, 1948, 68 (1-2): : 8 - 11
  • [33] RATE FACTORS IN LIQUID PHASE HYDROGENATION .2. SIMULATION AND OPTIMIZATION OF HYDROGENATION OF COTTONSEED OIL
    LUNDQVIST, LE
    SCHOON, NH
    ACTA POLYTECHNICA SCANDINAVICA-CHEMISTRY INCLUDING METALLURGY SERIES, 1971, (100): : 37 - +
  • [34] TRISATURATES IN THE HYDROGENATION OF CANOLA OIL WITH A COMMERCIAL NICKEL-CATALYST
    DEMAN, L
    DEMAN, JM
    ACKMAN, RG
    RATNAYAKE, WMN
    JOURNAL OF THE AMERICAN OIL CHEMISTS SOCIETY, 1985, 62 (04) : 703 - 706
  • [35] Hydrogenation catalyst based on modified carbon nanofibers
    Osipov, N. N.
    Klyuev, M., V
    IV NANOTECHNOLOGY INTERNATIONAL FORUM (RUSNANOTECH 2011), 2012, 345
  • [36] CLA formation in oils during hydrogenation process as affected by catalyst types, catalyst contents, hydrogen pressure, and oil species
    Jung, MO
    Ju, JW
    Choi, DS
    Yoon, SH
    Jung, MY
    JOURNAL OF THE AMERICAN OIL CHEMISTS SOCIETY, 2002, 79 (05) : 501 - 510
  • [37] Cis selectivity of mixed catalyst systems in canola oil hydrogenation
    Wright, AJ
    Mihele, AL
    Diosady, LL
    FOOD RESEARCH INTERNATIONAL, 2003, 36 (08) : 797 - 804
  • [38] Influence of rapeseed oil hydrotreating on hydrogenation activity of CoMo catalyst
    Kochetkova, Daria
    Blazek, Josef
    Simacek, Pavel
    Stas, Martin
    Beno, Zdenek
    FUEL PROCESSING TECHNOLOGY, 2016, 142 : 319 - 325
  • [39] Highly stable platinum monolith catalyst for the hydrogenation of vegetable oil
    David Troncoso, Franco
    Marta Tonetto, Gabriela
    CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2022, 170
  • [40] EFFECT OF AGING ON PERFORMANCE OF NICKEL FORMATE AS A CATALYST IN OIL HYDROGENATION
    NANAVATI, DD
    INDIAN JOURNAL OF TECHNOLOGY, 1974, 12 (02): : 61 - 63