Volume 44 Issue 1
Jan.  2016
Turn off MathJax
Article Contents
YANG Na, WANG Hong-ying, LIU Yun-qi, LIU Chen-guang. Study on the transformation rule of different long chain alkane hydroisomerization over Pt/SAPO-11 catalyst[J]. Journal of Fuel Chemistry and Technology, 2016, 44(1): 91-98.
Citation: YANG Na, WANG Hong-ying, LIU Yun-qi, LIU Chen-guang. Study on the transformation rule of different long chain alkane hydroisomerization over Pt/SAPO-11 catalyst[J]. Journal of Fuel Chemistry and Technology, 2016, 44(1): 91-98.

Study on the transformation rule of different long chain alkane hydroisomerization over Pt/SAPO-11 catalyst

Funds:

The project was supported by National Natural Science Foundation of China 21006128

The project was supported by National Natural Science Foundation of China U1162203

China University of Petroleum (East China) Innovation Project YCX2015025

More Information
  • Corresponding author: LIU Yun-qi, E-mail: Liuyq@upc.edu.cn
  • Received Date: 2015-07-28
  • Rev Recd Date: 2015-09-28
  • Available Online: 2022-03-23
  • Publish Date: 2016-01-01
  • The reaction mechanism of hydroisomerization of n-alkanes, from n-decane to n-tetrodecane, over Pt/SAPO-11 catalyst was studied. Results indicated that the n-alkanes with different carbon atom numbers exhibited higher isomerization selectivity at lower temperatures. The isomerization selectivity of n-alkanes can reach 90% by controlling temperature to keep the conversion rate lower than 85%. The conversion rate of n-alkanes was increased and the selectivity of isomerization was decreased with the increase of carbon atom number and temperature due to the occurrence of cracking reaction. Bifunctional catalyst has a good product shape selective effects. The isomerization products are mainly composed of unilateral chain isomers which have the methyl at the end and the center of the carbon chain. At low conversion rate, the cracking reaction of the long-chain n-alkanes over the Pt/SAPO-11 catalyst was mainly catalytic hydrocracking, the carbon number distribution of the cracking products was uniform. However, at high conversion rate, the reaction was mainly acid catalytic cracking, the carbon number distribution of cracking products was obvious asymmetric distribution.
  • loading
  • [1]
    MILLER S J. New molecular sieve process for lube dewaxing by wax isomerization[J]. Microporous Mater, 1994, 2(5): 439-449. doi: 10.1016/0927-6513(94)00016-6
    [2]
    MILLER S J. Studies on wax isomerization for lubes and fuels[J]. Stud Sur Sci Catal, 1994, 84: 2319-2326. doi: 10.1016/S0167-2991(08)63796-9
    [3]
    BRENMAN J A.Wide-temperature range synthetic hydrocarbon fluids[J]. Ind Chem Prod Res Dev, 1980, 19(1): 2-6. doi: 10.1021/i360073a002
    [4]
    水天德.现代润滑油生产工艺[M].北京:中国石化出版社, 1997: 29-37.

    SHUI Tian-de. Modern oil production process[M]. Beijing: China Petrochemical Press, 1997: 29-37.
    [5]
    刘维桥, 刘平, 任杰, 孙予罕.正构烷烃临氢异构化反应研究进展[J].精细石油化工进展, 2007, 8(10): 19-26. http://www.cnki.com.cn/Article/CJFDTOTAL-JXSI200710009.htm

    LIU Wei-qiao, LIU Ping, REN Jie, SUN Yu-han. Advances in research of n-paraffin hydroisomerization[J]. Adv Fine Petrochem, 2007, 8(10): 19-26. http://www.cnki.com.cn/Article/CJFDTOTAL-JXSI200710009.htm
    [6]
    刘维桥, 尚通明, 崔益梅. Pt (Pd)/SAPO-11的正庚烷临氢异构化反应特性[J].江苏技术师范学院学报, 2008, 14(1): 1-5. http://www.cnki.com.cn/Article/CJFDTOTAL-CZJF200801001.htm

    LIU Wei-qiao, SHANG Tong-ming, CUI Yi-mei. Characteristics of heptane hydroisomerization over Pt (Pd)/SAPO-11 catalyst[J]. J Jiangsu. Teach Univ Technol, 2008, 14(1): 1-5. http://www.cnki.com.cn/Article/CJFDTOTAL-CZJF200801001.htm
    [7]
    MÉRIAUDEAU P, TUAN V A, NGHIEM V T, LAI S Y, HUNG L N, NACCACHE C. SAPO-11, SAPO-31 and SAPO-41 molecular sieves: Synthesis, characterization, and catalytic properties in n-octane hydroisomerization[J]. J Catal, 1997, 169(4): 55-66. https://www.researchgate.net/publication/238644903_SAPO-11_SAPO-31_and_SAPO-41_Molecular_Sieves_Synthesis_Characterization_and_Catalytic_Properties_in_n-Octane_Hydroisomerization
    [8]
    耿承辉, 张飞, 高志贤, 周敬来, 任杰. Pt/SAPO-11催化剂上长链烷烃临氢异构化产物分布规律的研究[J].石油学报(石油加工), 2005, 2: 16-22. http://www.cnki.com.cn/Article/CJFDTOTAL-SXJG200502002.htm

    GEN Cheng-hui, ZHANG Fei, GAO Zhi-xian, ZHOU Jing-lai, REN Jie. Study on the production distribution of long chain alkane hydroisomerization over Pt/SAPO-11 catalyst[J]. Acta Pet Sin (Pet Process Sec), 2005, 2: 16-22. http://www.cnki.com.cn/Article/CJFDTOTAL-SXJG200502002.htm
    [9]
    CAMPELO J M, LAFONT F, MARINAS J M. Comparison of the acrivity and selectivity of Pt/SAPO-5 and Pt/SAPO-11 in n-hexane and n-heptane hydroconvertion[J]. Appl Catal, 1997, 152(1): 53-62. doi: 10.1016/S0926-860X(96)00347-X
    [10]
    CAMPELO J M, LAFONT F, MARINAS J M. Hydroconversion of n-dodecane over Pt/SAPO-11 catalyst[J]. Appl Catal, 1998, 170(1): 139-144. doi: 10.1016/S0926-860X(98)00036-2
    [11]
    SINHA A K, SIVASANKER S, RATNASAMY P. Hydroisomerization of n-alkanes over Pt-SAPO-11 and Pt-SAPO-31 synthesized from aqueous and nonaqueous media[J]. Ind Eng Chem Res, 1998, 37(6): 2208-2214. doi: 10.1021/ie9707228
    [12]
    高志贤, 耿承辉, 张飞, 李源.一种长链正构烷烃临氢异构化催化剂及其应用方法[P].中国, 03145688.

    X. 2004-02-18.GAO Zhi-xian, GENG Chen-hui, ZHANG Fei, LI Yuan. A long-chain n-alkanes hydroisomerization catalyst and application method: CN, 03145688. X[P]. 2004-02-18.
    [13]
    张志华, 胡胜, 韩雪莲, 许本静, 田永亮, 阎子峰. Pt/SAPO-11催化剂上柴油馏分临氢异构化改质反应研究[J].分子催化, 2005, 5: 20-25. http://www.cnki.com.cn/Article/CJFDTOTAL-FZCH200505002.htm

    ZHANG Zhi-hua, HU Sheng, HAN Xue-lian, XU Ben-jing, TIAN Yong-liang, YAN Zi-feng. Study on hydroisomerization of diesel fuel over Pt/SAPO-11[J]. J Mol Catal, 2005, 5: 20-25. http://www.cnki.com.cn/Article/CJFDTOTAL-FZCH200505002.htm
    [14]
    CLAUDE M C, MARTENS J A. Monomethyl branching of long n-alkanes in the range from decane to tetracosane on Pt/HZSM-22 Bi-function catalyst[J]. J Catal, 2000, 190(1): 39-48. doi: 10.1006/jcat.1999.2714
    [15]
    MARTENS J A, VANBUTSELE G, JACOBS P A, DENAYER J, OCAKOGLU R, BARON G, MUNOZ ARROYO J A, THYBAUT J, MARIN G B. Evidences for pore mouth and key-lock catalysis in hydroisomerization of long n-alkanes over 10-ring tubular pore bifunctional zeolites[J]. Catal Today, 2001, 65(2): 111-116. http://www.academia.edu/14026190/Evidences_for_pore_mouth_and_key_lock_catalysis_in_hydroisomerization_of_long_n-alkanes_over_10-ring_tubular_pore_bifunctional_zeolites
    [16]
    WEITKAMP J. Isomerization of long-chain n-alkanes on a Pt/CaY zeolite catalyst[J]. Ind Eng Chem Prod Res Dev, 1982, 21(4): 550-558. doi: 10.1021/i300008a008
    [17]
    CAMPELO J M, LAFONT F, MARINAS J M. Hydroconversion of n-dodecane over Pt/SAPO-11 catalyst[J]. Appl Catal A: Gen, 1998, 170: 139-144. doi: 10.1016/S0926-860X(98)00036-2
  • 加载中

Catalog

    通讯作者: 陈斌, bchen63@163.com
    • 1. 

      沈阳化工大学材料科学与工程学院 沈阳 110142

    1. 本站搜索
    2. 百度学术搜索
    3. 万方数据库搜索
    4. CNKI搜索

    Article Metrics

    Article views (115) PDF downloads(6) Cited by()
    Proportional views
    Related

    /

    DownLoad:  Full-Size Img  PowerPoint
    Return
    Return