-
摘要: 将Pt前驱体分别溶解于水、乙醇、丙酮、乙酸中,采用浸渍法制备了一系列成型Pt/ZSM-22催化剂。通过XRD、BET、TEM、CO-chemisorption、CO-FTIR和Py-FTIR等表征手段对催化剂的物相结构、织构性质、金属性质和酸性进行了系统地考察并以正十二烷为模型化合物,研究了前躯体溶剂对临氢异构反应性能的影响。结果表明,溶剂极性是造成Pt分散差异的主要原因;以乙醇、丙酮和乙酸为浸渍溶剂制备的催化剂,Pt多分布于ZSM-22分子筛上,并与酸性位相互作用造成Pt缺电子;而以水为溶剂则造成Pt多分布于氧化铝黏结剂上,对Pt的电子性质影响较小。在临氢异构反应中,与Pt落位于氧化铝相比,Pt分布于ZSM-22分子筛上表现出更高的活性和异构选择性,表明缩短酸性位与金属位间距可使反应物和异构中间体迅速扩散至金属位上发生脱氢和加氢反应。Abstract: A series of Pt/ZSM-22 bifunctional catalysts were prepared by using different metal precursor solvents including water, methanol, acetone and acetic acid. The phase structure, texture properties, metal properties and acidity were systematically investigated by XRD, BET, TEM, CO-chemisorption, CO-FTIR and Py-FTIR. The effect of metal precursor solvents on n-dodecane isomerization was also studied. The results indicate that the solvents with different polarities lead to different locations of Pt particles. Part of Pt particles locate on ZSM-22 when methanol, acetone and acetic acid are used as solvents, and the interaction between Pt and acid sites lead to the electron-deficient of Pt. However, the Pt particles almost locate on the Al2O3 binders when water is used as solvent, and their electronic properties are little affected. Higher activity and selectivity are achieved when Pt particles locate on ZSM-22 in the n-dodecane isomerization reactions. These results indicate that shorten the distance between acid sites and metal sites can expedite the diffusion of reactants and isomerized intermediates to proceed dehydrogenation and hydrogenation reactions.
-
Key words:
- Pt/ZSM-22 /
- precursor solvent /
- metal location /
- electronic property /
- hydroisomerization
1) 本文的英文电子版由Elsevier出版社在ScienceDirect上出版(http://www.sciencedirect.com/science/journal/18725813). -
表 1 不同样品的物理化学性质
Table 1 Physicochemical properties of different samples
Sample Pt contents w/%a Micropore surface area
A/(m2·g-1) bMicropore volume
v/(cm3·g-1) bPt diameter
d/nmcPt dispersion /%c ZSM-22 - 148.8 0.075 - - Pt-WAT 0.5 147.9 0.074 1.3 85.9 Pt-ETH 0.5 142.6 0.070 1.6 72.2 Pt-ACE 0.5 143.9 0.071 1.7 67.9 Pt-ACI 0.5 142.4 0.070 2.0 58.8 Pt-WAT-120 0.5 149.2 0.075 1.3 86.3 a: determined by ICP-AES;
b: obtained by the N2-adsorption at -196 ℃;
c: determined by CO chemisorption表 2 不同样品的酸性表征
Table 2 Acidity of different samples determined by Py-FTIR spectra
Sample Acid types /(μmol·g-1) a B acid sites L acid sites 200 ℃ 350 ℃ 200 ℃ 350 ℃ ZSM-22 84 80 77 42 Pt-WAT 83 78 74 40 Pt-WAT-0.8 81 76 73 38 Pt-WAT-120 75 70 68 35 Pt-ETH 61 50 50 30 Pt-ACE 59 49 41 28 Pt-ACI 52 49 37 26 a: Brønsted and Lewis acid sites calculated from the peak area of FT-IR spectra by pyridine desorption at different temperatures -
[1] 任杰, 张怀科, 李永旺. F-T合成油品加工技术的研究进展[J].燃料化学学报, 2009, 37(6):769-776. doi: 10.3969/j.issn.0253-2409.2009.06.023REN Jie, ZHANG Huai-ke, LI Yong-wang. Research progress of the processing technology for Fischer-Tropsch syncrude[J]. J Fuel Chem Technol, 2009, 37(6):769-776. doi: 10.3969/j.issn.0253-2409.2009.06.023 [2] BOUCHY C, HASTOY G, GUILLON E, MARTENS J A. Fischer-Tropsch waxes upgrading via hydrocracking and selective hydroisomerization[J]. Oil Gas Sci Technol, 2009, 64(64):91-112. http://d.old.wanfangdata.com.cn/NSTLQK/NSTL_QKJJ024141887/ [3] 王宏浩, 刘粟侥, 张怀科, 郭大光, 马骏, 任杰, 王海彦. ZSM-22分子筛的合成、表征及烷基化性能研究[J].燃料化学学报, 2016, 44(8):1010-1016. doi: 10.3969/j.issn.0253-2409.2016.08.016WANG Hong-hao, LIU Su-yao, ZHANG Huai-ke, GUO Da-guang, MA Jun, REN Jie, WANG Hai-yan. Synthesis and characterization of ZSM-22 zeolites and their catalytic performance in alkylation reaction[J]. J Fuel Chem Technol, 2016, 44(8):1010-1016. doi: 10.3969/j.issn.0253-2409.2016.08.016 [4] LIU S, REN J, ZHANG H, LV E, YANG Y, LI Y W. Synthesis, characterization and isomerization performance of micro/mesoporous materials based on H-ZSM-22 zeolite[J]. J Catal, 2016, 335:11-23. doi: 10.1016/j.jcat.2015.12.009 [5] LIU S, REN J, ZHU S, ZHANG H, LV E, XU J, LI Y W. Synthesis and characterization of the Fe-substituted ZSM-22 zeolite catalyst with high n-dodecane isomerization performance[J]. J Catal, 2015, 330:485-496. doi: 10.1016/j.jcat.2015.07.027 [6] ZEČEVIĆ J, VANBUTSELE G, DE JONG K P, MARTENS J A. Nanoscale intimacy in bifunctional catalysts for selective conversion of hydrocarbons[J]. Nature, 2015, 528(7581):245-248. doi: 10.1038/nature16173 [7] FRANCIS J, GUILLON E, BATS N, PICHON C, CORMA A, SIMON L J. Design of improved hydrocracking catalysts by increasing the proximity between acid and metallic sites[J]. Appl Catal A:Gen, 2011, 409(23):140-147. http://www.wanfangdata.com.cn/details/detail.do?_type=perio&id=97b8559e316027798b2cfdce331bfaaf [8] KIM J, KIM W, SEO Y, KIM J C, RYOO R. n-Heptane hydroisomerization over Pt/MFI zeolite nanosheets:Effects of zeolite crystal thickness and platinum location[J]. J Catal, 2013, 301(5):187-197. http://www.sciencedirect.com/science/article/pii/S002195171300064X [9] WEISZ P B. Polyfunctional heterogeneous catalysis[J]. Adv Catal, 1962, 13:137-190. http://d.old.wanfangdata.com.cn/NSTLQK/NSTL_QKJJ024009182/ [10] SAMAD J E, BLANCHARD J, SAYAG C, LOUIS C, REGALBUTO J R. The controlled synthesis of metal-acid bifunctional catalysts:The effect of metal:Acid ratio and metal-acid proximity in Pt silica-alumina catalysts for n-heptane isomerization[J]. J Catal, 2016, 342:203-212. doi: 10.1016/j.jcat.2016.08.004 [11] BATALHA N, PINARD L, BOUCHY C, GUILLON E, GUISNET M. n-Hexadecane hydroisomerization over Pt-HBEA catalysts. Quantification and effect of the intimacy between metal and protonic sites[J]. J Catal, 2013, 307(6):122-131. http://www.wanfangdata.com.cn/details/detail.do?_type=perio&id=597619ac2fbb1e0366b1456a5a452d11 [12] MILLER J T, SCHREIER M, KROPF A J, REGALBUTO J R. A fundamental study of platinum tetraammine impregnation of silica:2. The effect of method of preparation, loading, and calcination temperature on (reduced) particle size[J]. J Catal, 2004, 225(1):190-202. doi: 10.1016/j.jcat.2004.03.034 [13] CHEN Z, LIU S, WANG H, NING Q, ZHANG H, YUN Y, REN J, LI Y W. Synthesis and characterization of bundle-shaped ZSM-22 zeolite via the oriented fusion of nanorods and its enhanced isomerization performance[J]. J Catal, 2018, 361:177-185. doi: 10.1016/j.jcat.2018.02.019 [14] TREACY M M J, PRINCETON, N J. Collection of simulated XRD powder patterns for zeolites[J]. Appl Catal, 1986, 21(2):388-389. http://www.sciencedirect.com/science/article/pii/S0166983400813822 [15] ARISTIZÁBAL A, CONTRERAS S, DIVINS N J, LLORCA J, MEDINA F. Pt-Ag/activated carbon catalysts for water denitration in a continuous reactor:Incidence of the metal loading, Pt/Ag atomic ratio and Pt metal precursor[J]. Appl Catal B:Environ, 2012, 127:351-362. doi: 10.1016/j.apcatb.2012.08.039 [16] 杨春雁, 杨卫亚, 凌凤香, 范峰.负载型金属催化剂表面金属分散度的测定[J].化工进展, 2010, 29(8):1468-1473. http://d.old.wanfangdata.com.cn/Periodical/hgjz201008015YANG Chun-yan, YANG Wei-ping, LING Feng-xiang, FAN Feng. Determination of metal dispersion on supported metal catalyst surface[J]. Chem Ind Eng Prog, 2010, 29(8):1468-1473. http://d.old.wanfangdata.com.cn/Periodical/hgjz201008015 [17] WANG Y, TAO Z, WU B, XU J, HUO C, LI K, CHEN H, YANG Y, LI Y. Effect of metal precursors on the performance of Pt/ZSM-22 catalysts for n-hexadecane hydroisomerization[J]. J Catal, 2015, 322:1-13. doi: 10.1016/j.jcat.2014.11.004 [18] XU D, WU B, REN P, WANG S, HUO C, ZHANG B, GUO W, HUANG L, WEN X, QIN Y, YANG Y, LI Y. Controllable deposition of Pt nanoparticles into a KL zeolite by atomic layer deposition for highly efficient reforming of n-heptane to aromatics[J]. Catal Sci Technol, 2017, 7(6):1342-1350. doi: 10.1039/C6CY02652D [19] HAN W J, KOOH A B, HICKS R F. Infrared spectroscopy of carbon monoxide adsorbed on Pt/L zeolite[J]. Catal Lett, 1993, 18(3):193-208. doi: 10.1007/BF00769438 [20] JACOBS G, GHADIALI F, PISANU A, PADRO C L, BORGNA A, ALVAREZ W E, RESASCO D E. Increased sulfur tolerance of Pt/KL catalysts prepared by vapor-phase impregnation and containing a Tm promoter[J]. J Catal, 2000, 191(1):116-127. doi: 10.1006/jcat.1999.2779 [21] MENACHERRY P V, HALLER G L. Electronic effects and effects of particle morphology in n-hexane conversion over zeolite-supported platinum catalysts[J]. J Catal, 1998, 177(2):175-188. doi: 10.1006/jcat.1998.2048 [22] FUKASE S, KUMAGAI H, SUZUKA T. Catalytic behavior of platinum ion-exchanged zinc-aluminosilicates in n-pentane aromatization[J]. Appl Catal A:Gen, 1992, 93(1):35-45. doi: 10.1016/0926-860X(92)80292-K [23] NODA T, SUZUKI K, KATADA N, NIWA M. Combined study of IRMS-TPD measurement and DFT calculation on Brφnsted acidity and catalytic cracking activity of cation-exchanged Y zeolites[J]. J Catal, 2008, 259(2):203-210. doi: 10.1016/j.jcat.2008.08.004 [24] NAVARRO R M, PAWELEC B, TREJO J M, MARISCAL R, FIERRO J L G. Hydrogenation of aromatics on sulfur-resistant PtPd bimetallic catalysts[J]. J Catal, 2000, 189(1):184-194. doi: 10.1006/jcat.1999.2693