An exploratory study for obtaining synthetic crudes from heavy crude oils via hydrotreating

被引:49
作者
Ancheyta, J
Betancourt-Rivera, G
Marroquín-Sánchez, G
Pérez-Arellano, AM
Maity, SK
Cortez, T
del Río-Soto, R
机构
[1] Inst Mexicano Petr, Mexico City 07730, DF, Mexico
[2] Inst Politecn Nacl, ESIQIE, Mexico City 07738, DF, Mexico
[3] GIDT, Mexico City 11311, DF, Mexico
关键词
D O I
10.1021/ef000141m
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
In this work we present an experimental evaluation about the catalytic hydrotreating (HDT) of Maya heavy crude oil. The study was carried out in a high-pressure fixed bed pilot plant. The HDT reactions were conducted at 54-100 kg/cm(2) pressure, 0.5-1.5 h(-1) LHSV, 380-420 degreesC temperature, and 5000-10 000 ft(3)/bbl H-2/oil ratio using an experimental NiMo/Al2O3-TiO2 catalyst. The data showed that API gravity and sulfur, nitrogen, Ramsbottom carbon, asphaltenes, and metals (Ni, V) contents can be improved by direct HDT of Maya crude oil. Values very similar to the Isthmus light crude oil properties were obtained at severe operating conditions. Naphtha, middle distillates, and FCC feedstock fractions yield obtained from TBP distillation of the synthetic crudes increase as the severity of the HDT was increased. Middle distillates showed the greatest yield increase.
引用
收藏
页码:120 / 127
页数:8
相关论文
共 18 条
  • [1] COKE FORMATION ON CATALYSTS DURING THE HYDROPROCESSING OF HEAVY OILS-ALPHA
    ABSIHALABI, M
    STANISLAUS, A
    TRIMM, DL
    [J]. APPLIED CATALYSIS, 1991, 72 (02): : 193 - 215
  • [2] HYDRODEMETALATION OF NICKEL AND VANADIUM PORPHYRINS .2. INTRAPARTICLE DIFFUSION
    AGRAWAL, R
    WEI, J
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1984, 23 (03): : 515 - 522
  • [3] HYDRODEMETALATION OF NICKEL AND VANADIUM PORPHYRINS .1. INTRINSIC KINETICS
    AGRAWAL, R
    WEI, J
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1984, 23 (03): : 505 - 514
  • [4] Selection of catalysts and reactors for hydroprocessing
    Furimsky, E
    [J]. APPLIED CATALYSIS A-GENERAL, 1998, 171 (02) : 177 - 206
  • [5] KINETIC-STUDY ON THE HYDROTREATING OF HEAVY OIL .2. EFFECT OF CATALYST PORE-SIZE
    KOBAYASHI, S
    KUSHIYAMA, S
    AIZAWA, R
    KOINUMA, Y
    INOUE, K
    SHIMIZU, Y
    EGI, K
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1987, 26 (11) : 2245 - 2250
  • [6] Recent developments in fixed-bed catalytic residue upgrading
    Kressmann, S
    Morel, F
    Harle, V
    Kasztelan, S
    [J]. CATALYSIS TODAY, 1998, 43 (3-4) : 203 - 215
  • [7] OHTSUKA T, 1997, CATAL REV SCI ENG, V16, P291
  • [8] RHODES AK, 1997, OIL GAS J 1006, P41
  • [9] SCHEFFER B, 1988, CATAL TODAY, V43, P271
  • [10] SCHULMAN BL, 1996, UPGRADATION HEAVY CR