Influence of Ni crystallite size on deoxygenation of methyl laurate to hydrocarbons over Ni/SiO2 catalyst
-
摘要: 采用等体积浸渍-干燥-还原法及等体积浸渍-干燥-焙烧-还原法制备了3种具有不同Ni晶粒粒径的Ni/SiO2催化剂,利用H2-TPR、XRD、TEM、H2-TPR、NH3-TPD及TGA技术对其及前驱体进行了表征,并在固定床反应器上评价了其催化月桂酸甲酯脱氧制十一烷(C11)和十二烷(C12)的性能,分析了Ni晶粒粒径对其脱氧性能的影响。结果表明,采用等体积浸渍-干燥-还原法制备的催化剂中Ni晶粒粒径较小,提高还原温度可以促进Ni晶粒长大。随Ni晶粒粒径增大,月桂酸甲酯的转换频率提高,而C11和C12总选择性、C11/C12物质的量比及裂解产物选择性降低,Ni/SiO2催化剂上月桂酸甲酯脱氧为结构敏感反应。此外,还考察了重时空速对Ni/SiO2催化剂脱氧性能的影响,随重时空速提高,月桂酸甲酯转化率、C11和C12总选择性、C11/C12物质的量比及裂化产物选择性降低。月桂酸甲酯通过脱羰/脱羧反应路径生成的CO/CO2几乎全部加氢转化为CH4,表明Ni/SiO2催化剂具有很高的甲烷化活性。研究还发现,较小Ni晶粒烧结、有机物种吸附及积炭会导致催化剂失活。Abstract: Three Ni/SiO2 catalysts with different Ni crystallite sizes were prepared by the incipient wetness impregnation-drying-reduction and incipient wetness impregnation-drying-calcination-reduction methods. The catalysts were characterized by H2-TPR, XRD, TEM, H2 chemisorption, NH3-TPD and TGA techniques. Their catalytic performances in the deoxygenation of methyl laurate to undecane (C11) and dodecane (C12) were evaluated in a fixed bed reactor. The effects of Ni crystallite size on the catalyst structure and performance were investigated. It was found that the impregnation-drying-reduction method gave smaller Ni crystallite size, and the high reduction temperature promoted the growth of Ni crystallite. With the increase of the Ni crystallite size, the turnover frequency of methyl laurate increased, while the total selectivity to C11 and C12 (sC11+C12), C11/C12 mol ratio and the selectivity to cracking products decreased. We suggest that the deoxygenation of methyl laurate on Ni/SiO2 is structurally sensitive. The effects of weight hourly space velocity (WHSV) on performance of Ni/SiO2 were also investigated. As WHSV increased, the methyl laruate conversion, sC11+C12, C11/C12 mol ratio and the selectivity to cracking products decreased. In addition, CO and CO2 generated from the decarbonylation/decarboxylation pathway were converted to CH4, indicating that Ni/SiO2 had high activity for methanation. It was also found that the sintering of small Ni crystallites, the adsorption of organic compounds and carbon deposit led to catalyst deactivation.
-
谭天伟, 王芳, 邓立, 徐家立, 王丽娟. 生物柴油的生产和应用[J]. 现代化工, 2002, 22(2): 4-6. (TAN Tian-wei, WANG Fang, DENG Li, XU Jia-li, WANG Li-juan. Production and application of biodiesel[J]. Modern Chemical Industry, 2002, 22(2): 4-6.) 左华亮, 刘琪英, 王铁军, 史娜, 刘建国, 马隆龙. 负载的Ni催化剂上植物油脂加氢脱氧制备第二代生物柴油[J]. 燃料化学学报, 2012, 40(9): 1067-1073. (ZUO Hua-liang, LIU Qi-ying, WANG Tie-jun, SHI Na, LIU Jian-guo, MA Long-long. Catalytic hydrodeoxygenation of vegetable oil over Ni catalysts to produce second-generation biodiesel[J]. Journal of Fuel Chemistry and Technology, 2012, 40(9): 1067-1073.) SHARMA Y C, SINGH B, UPADHYAY S N. Advancements in development and characterization of biodiesel: A review[J]. Fuel, 2008, 87(12): 2355-2373. MARCHETTI J M, MIGUEL V U, ERRAZU A F. Possible methods for biodiesel production[J]. Renew Sus Energy Rev, 2007, 11(6): 1300-1311. MORGAN T, GRUBB D, SANTILLAN-JIMENEZ E, CROCKER M. Conversion of triglycerides to hydrocarbons over supported metal catalysts[J]. Top Catal, 2010, 53(11/12): 820-829. LESTARI S, SIMAKOVA I, TOKAREV A, MÄKI-ARVELA P, ERÄNEN K, MURZIN D Y. Synthesis of biodiesel via deoxygenation of stearic acid over supported Pd/C catalyst[J]. Catal Lett, 2008, 122(3/4): 247-251. LESTARI S, MÄKI-ARVELA P, ERÄNEN K, BELTRAMINI J, LU G Q M, MURZIN D Y. Diesel-like hydrocarbons from catalytic deoxygenation of stearic acid over supported Pd nanoparticles on SBA-15 catalysts[J]. Catal Lett, 2010, 134(3/4): 250-257. SENOL O I, RYYMIN E M, VILJAVA T R, KRAUSE A O I. Reactions of methyl heptanoate hydrodeoxygenation on sulphided catalysts[J]. J Mol Catal A: Chem, 2007, 268(1/2): 1-8. ZUO H L, LIU Q Y, WANG T J, MA L L, ZHANG Q, ZHANG Q. Hydrodeoxygenation of methyl palmitate over supported Ni catalysts for diesel-like fuel production[J]. Energy Fuels, 2012, 26(6): 3747-3755. PENG B X, YUAN X G, ZHAO C, LERCHER J A. Stabilizing catalytic pathways via redundancy: selective reduction of microalgae oil to alkanes[J]. J Am Chem Soc, 2012, 134(22): 9400-9405. SNÅRE M, KUBICKOVÁ I, MÄKI-ARVELA P, ERÄNEN K, MURZIN D Y. Heterogeneous catalytic deoxygenation of stearic acid for production of biodiesel[J]. Ind Eng Chem Res, 2006, 45(16): 5708-5715. SONG W J, CHEN Z, LERCHER J A. Importance of size and distribution of Ni nanoparticles for the hydrodeoxygenation of microalgae oil[J]. Chem Eur J, 2013, 19(30): 9833-9842. LOUIS C, CHENG Z-X, CHE M. Characterization of Ni/SiO2 catalysts during impregnation and further thermal activation treatment leading to metal particles[J]. J Phys Chem, 1993, 97(21): 5703-5712. LI K L, WANG R J, CHEN J X. Hydrodeoxygenation of anisole over silica-supported Ni2P, MoP, and NiMoP catalysts[J]. Energy Fuels, 2011, 25(3): 854-863. CLAUSE O, BONNEVIOT L, CHE M. Effect of the preparation method on the thermal stability of silica-supported nickel oxide as studied by EXAFS and TPR techniques[J]. J Catal, 1992, 138(1): 195-205. RODRIGUEZ J A, HANSON J C, FRENKEL A I, KIM J Y, PREZ M. Experimental and theoretical studies on the reaction of H2 with NiO: Role of O vacancies and mechanism for oxide reduction[J]. J Am Chem Soc, 2002, 124(2): 346-354. FURSTENAU R P, MCDOUGALL G, LANGELL M A. Initial stages of hydrogen reduction of NiO(100)[J]. Surf Sci, 1985, 150(1): 55-79. HADJⅡVANOV K, MIHAYLOV M, KLISSURSKI D, STEFANOV P, ABADJIEVA N, VASSILEVA E, MINTCHEV L. Characterization of Ni/SiO2 catalysts prepared by successive deposition and reduction of Ni2+ ions[J]. J Catal, 1999, 185(2): 314-323. FANG K G, REN J, SUN Y H. Effect of nickel precursors on the performance of Ni/AlMCM-41 catalysts for n-dodecane hydroconversion[J]. J Mol Catal A: Chem, 2005, 229 (1/2): 51-58. 刘旭光. 二氧化硅负载镍或磷化镍催化氯苯气相加氢脱氯的研究[D]. 天津: 天津大学, 2007. (LIU Xu-guang. Study on catalytic hydrodechlorination of chlorobenzen in gas phase over silica supported nickel or nickel phosphide catalysts[D]. Tianjin: Tianjin University, 2007.) YANG Y, CHEN J X, SHI H. Deoxygenation of methyl laurate as a model compound to hydrocarbons on Ni2P/SiO2, Ni2P/MCM-41, and Ni2P/SBA-15 catalysts with different dispersions[J]. Energy Fuels, 2013, 27(6): 3400-3409.
点击查看大图
计量
- 文章访问数: 642
- HTML全文浏览量: 19
- PDF下载量: 1151
- 被引次数: 0