Volume 46 Issue 1
Jan.  2018
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Article Contents
LIU He, WANG Zong-xian, ZHAO Xiang-kun, LI Yu-xing, CHEN Kun, GUO Ai-jun. Partial upgrading of vacuum residue from Canadian oil sand bitumen under CO/H2-H2O[J]. Journal of Fuel Chemistry and Technology, 2018, 46(1): 45-53.
Citation: LIU He, WANG Zong-xian, ZHAO Xiang-kun, LI Yu-xing, CHEN Kun, GUO Ai-jun. Partial upgrading of vacuum residue from Canadian oil sand bitumen under CO/H2-H2O[J]. Journal of Fuel Chemistry and Technology, 2018, 46(1): 45-53.

Partial upgrading of vacuum residue from Canadian oil sand bitumen under CO/H2-H2O

Funds:

National Natural Science Foundation of China 21776313

the China Postdoctoral Science Foundation 2016M602219

Provincial Natural Science Foundation of Shandong ZR2017BB021

Qingdao Postdoctoral Applied Research Project 2016224

State Key Laboratory of Heavy Oil Processing SLKZZ-2017003

State Key Laboratory of Heavy Oil Processing SLKZZ-2017011

Key Research and Development Plan of Shandong Province 2017GGX70108

Fundamental Research Funds for the Central Universities Special Projects, 17CX05016

PetroChina Innovation Foundation 2017D-5007-0506

China National Petroleum Corporation CNPC, PRIKY16066

Shandong Postdoctoral Funded Project 201702028

More Information
  • Corresponding author: WANG Zong-xian, Tel: 0532-86981851, E-mail: zxwang@upc.edu.cn
  • Received Date: 2017-09-27
  • Rev Recd Date: 2017-12-01
  • Available Online: 2021-01-23
  • Publish Date: 2018-01-10
  • The upgrading of the vacuum residue from Canadian oil sand bitumen was performed in a batch reactor with the syngas (CO/H2) and H2O. The effect of CO/H2-H2O for residue upgrading was verified. In the presence of CO/H2-H2O, the coke induction period is postponed by 3.5-6.5 min. When the coke yield is about 0.1%, the viscosity reduction efficiency can be raised by 29.1% at 410℃ and even 54.6% at 420℃. The upgrading experiments were also carried out in the presence of N2-H2O, CO-H2O, and H2-H2O, respectively. The results show that the capability to inhibit the coke formation was in the order of H2-H2O > CO/H2-H2O > CO-H2O > N2-H2O. The impetus of CO/H2-H2O to BVR upgrading could be attributed to the active hydrogen mainly from H2, nascent hydrogen by water-gas shift reaction as well as aqua-thermolysis. The thermal conditions such as the pressure of syngas, water content and reaction temperature could influence the coking propensity of BVR under CO/H2-H2O by affecting the three different attributions. These results indicate that the more accessible and low-cost syngas could provide the necessary hydrogen for BVR upgrading. Water presents a synergism with syngas for further promoting the BVR upgrading process.
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  • [1]
    李振宇, 乔明, 任文坡.委内瑞拉超重原油和加拿大油砂沥青加工利用现状[J].石油学报(石油加工), 2012, 28(3):517-524. http://www.doc88.com/p-5408063729438.html

    LI Zhen-yu, QIAO Ming, Ren Wen-po. Current development of venezuela extra heavy crude and canadian oil sands processing[J]. Acta Pet Sin (Pet Process Sect), 2012, 28(3):517-524. http://www.doc88.com/p-5408063729438.html
    [2]
    尹佳音, 唐葆君.中国石油进口安全影响因素分析[J].中国能源, 2016, 38(11):29-33. doi: 10.3969/j.issn.1003-2355.2016.11.006

    YIN Jia-yin, TANG Bao-jun. Analysis of influencing factors of China oil security from oil imports[J]. Energy China, 2016, 38(11):29-33. doi: 10.3969/j.issn.1003-2355.2016.11.006
    [3]
    BORDEN K. The challenges of processing and transporting heavy crude[J]. Oil Gas Facil, 2015, 2(5):22-26. https://www.researchgate.net/publication/274747516_The_Challenges_of_Processing_and_Transporting_Heavy_Crude
    [4]
    SANTOS R G, LOH W, BANNWART A C, TREVISAN O V. An overview of heavy oil properties and its recovery and transportation methods[J]. Braz J Chem Eng, 2014, 31(3):571-590. doi: 10.1590/0104-6632.20140313s00001853
    [5]
    王齐, 王宗贤, 沐宝泉, 郭爱军, 郭凯黎.委内瑞拉常压渣油供氢热转化研究[J].燃料化学学报, 2012, 40(10):1200-1205. doi: 10.3969/j.issn.0253-2409.2012.10.008

    WANG Qi, WANG Zong-xian, MU Bao-quan, GUO Ai-jun, GUO Kai-li. Hydrogen donor visbreaking of Venezuelan atmospheric residue[J]. J Fuel Chem Technol, 2012, 40(10):1200-1205. doi: 10.3969/j.issn.0253-2409.2012.10.008
    [6]
    ZHANG N, ZHAO S, SUN X, XU Z, XU C. Storage stability of the visbreaking product from venezuela heavy oil[J]. Energy Fuels, 2010, 24(7):3970-3976. doi: 10.1021/ef100272e
    [7]
    王齐, 郭磊, 王宗贤, 沐宝泉, 郭爱军, 刘贺.委内瑞拉减压渣油供氢热转化基础研究[J].燃料化学学报, 2012, 40(11):1317-1322. doi: 10.3969/j.issn.0253-2409.2012.11.006

    WANG Qi, GUO Lei, WANG Zong-xian, MU Bao-quan, GUO Ai-jun, LIU He. Hydrogen donor visbreaking of venezuelan vacuum residue[J]. J Fuel Chem Technol, 2012, 40(11):1317-1322. doi: 10.3969/j.issn.0253-2409.2012.11.006
    [8]
    TAKATUKA T, WADA Y, FUKUI Y, KOMATSU S, SHIMIZU S. VisABC process[C]//Heavy Oil and Oil Sands Technical Symposium, Calgary, Canada, 1988.
    [9]
    冯婉璐, 吴诗勇, 尤全, 吴幼青, 郑化安, 闵小建.合成气气氛下含水量对锡林浩特煤液化性能的影响[J].华东理工大学学报(自然科学版), 2017, 43(2):156-161. http://www.cqvip.com/QK/90601A/201702

    FENG Wan-lu, WU Shi-yong, YOU Quan, WU You-qing, ZHENG Hua-an, MIN Xiao-jian. Effect of moisture amount on liquefaction of Xinlinhaote coal under syngas[J]. J East China Univ Sci Technol (Nat Sci Ed), 2017, 43(2):156-161. http://www.cqvip.com/QK/90601A/201702
    [10]
    熊奇, 乔建超, 韩菊红, 盛清涛, 申峻.非纯氢气氛下煤直接液化的研究[J].煤化工, 2013, 41(5):21-24. http://d.wanfangdata.com.cn/Periodical_mhg201305006.aspx

    XIONG Qi, QIAO Jian-chao, HAN Ju-hong, SHENG Qing-tao, SHEN Jun. Study on direct coal liquefaction in non-pure hydrogen atmosphere[J]. Coal Chem Ind, 2013, 41(5):21-24. http://d.wanfangdata.com.cn/Periodical_mhg201305006.aspx
    [11]
    袁明江, 赵锁奇, 闫东菊.合成气氢源下悬浮床加氢反应焦炭及催化剂特性分析[J].石油炼制与化工, 2010, 41(10):52-57. doi: 10.3969/j.issn.1005-2399.2010.10.010

    YUAN Ming-jiang, ZHAO Suo-qi, YAN Dong-ju. An analysis of coke and dispersed catalysts in slurry-bed hydrocracking using syngas as hydrogen source[J]. Pet Process Petrochem, 2010, 41(10):52-57. doi: 10.3969/j.issn.1005-2399.2010.10.010
    [12]
    王刚, 李文, 衣悦涛, 薛钦昭, 李保庆.氢气和合成气下生物质高压液化过程的实验研究[J].燃料化学学报, 2008, 36(5):563-569. http://manu60.magtech.com.cn/rlhxxb/CN/abstract/abstract17298.shtml

    WANG Gang, LI Wen, YI Yue-tao, XUE Qin-zhao, LI Bao-qing. Experimental study on high-pressure liquefaction of biomass in H2 and syngas[J]. J Fuel Chem Technol, 2008, 36(5):563-569. http://manu60.magtech.com.cn/rlhxxb/CN/abstract/abstract17298.shtml
    [13]
    XU Y, YUAN M, ZHAO S, XU C. Upgrading heavy oil using syngas as the hydrogen source with dispersed catalysts[J]. Pet Sci Technol, 2009, 27(7):712-732. doi: 10.1080/10916460802105641
    [14]
    YAN D, YUAN M, SUN X, ZHAO S. A Fundamental research for upgrading heavy oil using syngas as hydrogen source[C]//Proceedings of 1st world heavy oil conference, 2006, 930-941.
    [15]
    HOOK B D, AKGERMAN A. Desulfurization of dibenzothiophene by in-situ hydrogen generation through a water gas shift reaction[J]. Ind Eng Chem Process Des Dev, 1986, 25(25):278-284. https://web.anl.gov/PCS/acsfuel/preprint%20archive/Files/39_2_SAN%20DIEGO_03-94_0623.pdf
    [16]
    LIU C, NG F T T. HDS of DBT using in situ generated hydrogen in the presence of dispersed Mo catalysts Ⅱ. Comparison between in situ hydrogen and molecular H2[J]. Chin J Catal, 1999, 20(5):597-59. https://www.sciencedirect.com/science/article/pii/S0920586109002806
    [17]
    NG F T T, TSAKIRI S K. Activation of water in emulsion for catalytic desulphurization of benzothiophene[J]. Fuel, 1992, 71(11):1309-1314. doi: 10.1016/0016-2361(92)90059-W
    [18]
    ALGHAMDI A. Hydrodesulphurization of light gas oil using hydrogen from the water gas shift reaction[D]. Waterloo:University of Waterloo, 2009.
    [19]
    LIU K. Hydrodesulfurization and hydrodenitrogenation of model, compounds using in-situ hydrogen over nano-dispersed, Mo sulfide based catalysts[D]. Waterloo:University of Waterloo, 2010.
    [20]
    JIA L. Oil sands bitumen emulsion upgrading by using in situ hydrogen generated through the water gas shift reaction[D]. Waterloo:University of Waterloo, 2014.
    [21]
    CHOY C. Naphthalene hydrogenation with water gas shift in model oil/water emulsion slurry over molybdenum sulfide[D]. Waterloo:University of Waterloo, 2009.
    [22]
    ARAI K, TADAFUMI ADSCHIRI A, WATANABE M. Hydrogenation of hydrocarbons through partial oxidation in supercritical water[J]. Ind Eng Chem Res, 2000, 39(12):4697-4701. doi: 10.1021/ie000326g
    [23]
    SATO T, SUMITA T, ITOH N. Effect of CO addition on upgrading bitumen in supercritical water[J]. J Supercrit Fluids, 2015, 104:171-176. doi: 10.1016/j.supflu.2015.06.004
    [24]
    YUAN P Q, CHENG Z M, JIANG W L, ZHANG R, YUAN W K. Catalytic desulfurization of residual oil through partial oxidation in supercritical water[J]. J Supercrit Fluids, 2005, 35(1):70-75. doi: 10.1016/j.supflu.2004.11.002
    [25]
    程健, 刘以红, 罗运华, 刘国祥, 阙国和.孤岛渣油超临界水-合成气中悬浮床加氢裂化反应研究Ⅰ.催化剂的影响[J].燃料化学学报, 2003, 31(6):574-578. http://manu60.magtech.com.cn/rlhxxb/CN/abstract/abstract16868.shtml

    CHENG Jian, LIU Yi-hong, LUO Yun-hua, LIU Guo-xiang, QUE Guo-he. Hydrocracking of Gudao residual oil in suspended bed using supercritical water-syngas as hydrogen source Ⅰ. The effect of catalyst on hydrocracking[J]. J Fuel Chem Technol, 2003, 31(6):574-578. http://manu60.magtech.com.cn/rlhxxb/CN/abstract/abstract16868.shtml
    [26]
    程健, 李晶, 刘以红, 罗运华, 刘国祥, 阙国和.孤岛渣油超临界水-合成气中悬浮床加氢裂化反应研究Ⅱ.不同氢源下的加氢裂化反应[J].燃料化学学报, 2004, 32(2):180-184. http://manu60.magtech.com.cn/rlhxxb/CN/abstract/abstract16712.shtml

    CHENG Jian, LI Jing, LIU Yi-hong, LUO Yun-hua, LIU Guo-xiang, QUE Guo-he. Gudao residual oil hydrocracking with dispersed catalysts using supercritical water-syngas as hydrogen source Ⅱ. The comparison of residue hydrocracking using different hydrogen sources[J]. J Fuel Chem Technol, 2004, 32(2):180-184. http://manu60.magtech.com.cn/rlhxxb/CN/abstract/abstract16712.shtml
    [27]
    张龙力, 张世杰, 杨国华, 蒋云, 阙国和.常压渣油热反应过程中胶体的稳定性[J].石油学报(石油加工), 2003, 19(2):82-87. http://www.cqvip.com/QK/94167X/200302/7839649.html

    ZHANG Long-li, ZHANG Shi-jie, YANG Guo-hua, JIANG Yun, QUE Guo-he. Colloid stability of atmospheric residual oil during thermal reaction[J]. Acta Pet Sin (Pet Process Sect), 2003, 19(2):82-87. http://www.cqvip.com/QK/94167X/200302/7839649.html
    [28]
    张龙力, 杨国华, 阙国和, 杨朝合, 山红红.大港常压渣油临氮与临氢热反应过程中胶体稳定性变化研究[J].燃料化学学报, 2011, 39(9):682-688. http://manu60.magtech.com.cn/rlhxxb/CN/abstract/abstract17802.shtml

    ZHANG Long-li, YANG Guo-hua, QUE Guo-he, YANG Chao-he, SHAN Hong-hong. Colloidal stability variation of Dagang atmosphere residue during thermal reaction under nitrogen or hydrogen[J]. J Fuel Chem Technol, 2011, 39(9):682-688. http://manu60.magtech.com.cn/rlhxxb/CN/abstract/abstract17802.shtml
    [29]
    郭爱军, 薛鹏, 陈建涛, 王宗贤.超稠油掺炼供氢剂的减黏裂化研究[J].炼油技术与工程, 2013, 43(5):28-32. http://www.cqvip.com/QK/92738A/201305/46922254.html

    GUO Ai-jun, XUE Peng, CHEN Jian-tao, WANG Zong-xian. Study on application of hydrogen donor in visbreaking of ultra-heavy oil[J]. Pet Refin Eng, 2013, 43(5):28-32. http://www.cqvip.com/QK/92738A/201305/46922254.html
    [30]
    MURAZA O, GALADIMA A. Aquathermolysis of heavy oil:A review and perspective on catalyst development[J]. Fuel, 2015, 157:219-231. doi: 10.1016/j.fuel.2015.04.065
    [31]
    吴川, 雷光伦, 姚传进, 盖平原, 曹嫣镔, 李啸南.双亲催化剂作用超稠油水热裂解降黏机理研究[J].燃料化学学报, 2010, 38(6):684-690. http://manu60.magtech.com.cn/rlhxxb/CN/abstract/abstract17648.shtml

    WU Chuan, LEI Guang-lun, YAO Chuan-jin, GAI Ping-yuan, CAO Yan-bin, LI Xiao-nan. Mechanism for reducing the viscosity of extra-heavy oil by aquathermolysis with an amphiphilic catalyst[J]. J Fuel Chem Technol, 2010, 38(6):684-690. http://manu60.magtech.com.cn/rlhxxb/CN/abstract/abstract17648.shtml
    [32]
    樊泽霞, 赵福麟, 王杰祥, 巩永刚.超稠油供氢水热裂解改质降黏研究[J].燃料化学学报, 2006, 34(3):315-318. http://manu60.magtech.com.cn/rlhxxb/CN/abstract/abstract17002.shtml

    FAN Ze-xia, ZHAO Fu-lin, WANG Jie-xiang, GONG Yong-gang. Upgrading and viscosity reduction of super heavy oil by aqua-thermolysis with hydrogen donor[J]. J Fuel Chem Technol, 2006, 34(3):315-318. http://manu60.magtech.com.cn/rlhxxb/CN/abstract/abstract17002.shtml
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