固体酸WO3/TiO2负载锂锰催化剂组成对其甲烷氧化偶联反应性能的影响

doi:10.3866/PKU.WHXB201902004

物理化学学报 >> 2019, Vol. 35 >> Issue (9): 1027-1036.doi: 10.3866/PKU.WHXB201902004

所属专题：碳氢键活化

论文上一篇

固体酸WO₃/TiO₂负载锂锰催化剂组成对其甲烷氧化偶联反应性能的影响

程飞^1,²,杨建^1,*(),闫亮¹,赵军¹,赵华华¹,宋焕玲¹,丑凌军^1,^3,*()

¹ 兰州化学物理研究所，羰基合成与选择氧化国家重点实验室，甘肃兰州 730000
² 中国科学院大学，北京 100049
³ 中国科学院兰州化物所苏州研究院，江苏苏州 215123

收稿日期:2019-02-01 录用日期:2019-03-06 发布日期:2019-03-08
通讯作者: 杨建,丑凌军 E-mail:yjian@licp.cas.cn;ljchou@licp.cas.cn
基金资助:
中国石油科技创新基金(2016D-5007-0506);中国科学院战略性先导科技专项(XDA09030101)

Influence of the Composition/Texture of Solid Acid WO₃/TiO₂-Supported Lithium-Manganese Catalysts on the Oxidative Coupling of Methane

Fei CHENG^1,²,Jian YANG^1,*(),Liang YAN¹,Jun ZHAO¹,Huahua ZHAO¹,Huanling SONG¹,Lingjun CHOU^1,^3,*()

¹ State Key Laboratory for Oxo Synthesis and Selective Oxidation, Lanzhou Institute of Chemical Physics, Chinese Academy of Sciences, Lanzhou 730000, P. R. China
² University of Chinese Academy of Sciences, Beijing 100049, P. R. China
³ Suzhou Research Institute of LICP, Chinese Academy of Sciences, Suzhou 215123, Jiangsu Province, P. R. China

Received:2019-02-01 Accepted:2019-03-06 Published:2019-03-08
Contact: Jian YANG,Lingjun CHOU E-mail:yjian@licp.cas.cn;ljchou@licp.cas.cn
Supported by:
The project was supported by the Petro China Innovation Foundation(2016D-5007-0506);the "Strategic Priority Research Program" of the Chinese Academy of Sciences(XDA09030101)

摘要/Abstract

摘要：

甲烷氧化偶联制乙烷、乙烯是一种最直接有效的甲烷转化工艺路线。催化剂的结构、碱性、活性组分的状态及分布和氧物种的性质是影响甲烷氧化偶联性能的重要因素，而这些因素与催化剂组成直接相关。以固体酸WO₃/TiO₂为载体，采用浸渍法制备出一系列负载Li、Mn活性组分的催化剂。利用电感耦合等离子体发射光谱(ICP-OES)、X射线衍射(XRD)、高分辨透射电镜(HRTEM)、CO₂程序升温脱附(CO₂-TPD)、O₂程序升温脱附(O₂-TPD)、H₂程序升温还原(H₂-TPR)、拉曼光谱(Raman)、X射线光电子能谱(XPS)和CH₄程序升温表面反应(CH₄-TPSR)等表征技术对催化剂进行了研究，发现Li的添加提高了C₂选择性，并有效抑制了甲烷深度氧化形成CO₂的过程。XRD分析表明Li的添加不仅能够促进锐钛矿型二氧化钛向金红石型二氧化钛转化而且促使了高价锰离子的还原。XPS与CO₂-TPD分析表明Li的增加有利于增加催化剂表面的晶格氧含量和降低催化剂表面的碱性。O₂-TPD分析表明Li含量逐渐升高能够促使晶格氧的移动性增强，从而提高催化剂的反应性能。催化剂的性能受Mn物种的含量与价态的影响，过多的Mn物种对甲烷氧化偶联是不利的，易造成甲烷的深度氧化。同时，Li和Mn活性组分通过协同作用影响着催化剂的反应性能，能够形成新的活性物种MnTiO₃提高甲烷氧化偶联的低温活性。催化剂在n(Li) : n(Mn) = 2 : 1、反应温度750 ℃条件下，C₂产率达16.3%，表现出最佳催化效果。

关键词: 甲烷氧化偶联, 锰物种, WO₃/TiO₂, 晶格氧, MnTiO₃

Abstract:

The selective oxidation of methane to basic petrochemicals (ethylene and ethane) is desirable and has attracted extensive research attention. The oxidative coupling of methane (OCM) is considered a promising one-step route for the production of C₂ compounds (ethylene and ethane) from methane, and has been the focus of industrial and fundamental studies. It is widely accepted that the composition is a crucial factor governing the activity of a catalyst system. It was found that the phase structures, basicity, existing status and distribution of the active components, oxygen species, and chemical states of the catalyst were influenced by the composition and ratio, resulting in different catalytic performances for the OCM. In this study, a series of solid acid WO₃/TiO₂-supported lithium-manganese oxide catalysts for OCM were synthesized via the impregnation method. The impacts of diverse compositions, such as the individual contents (Li and Mn) and dual contents (Li-Mn), on the OCM were investigated in detail, using inductively coupled plasma optical emission spectrometry, X-ray diffraction, high-resolution transmission electron microscopy, CO₂-temperature-programmed desorption, O₂-temperature-programmed desorption, H₂-temperature-programmed reduction, Raman spectroscopy, X-ray photoelectron spectroscopy, and CH₄-temperature-programmed surface reaction. The addition of Li content to the catalyst not only led to the anatase-to-rutile crystal structure transformation of TiO₂, and the reduction of the high-valence-state Mn species to low-valence-state Mn, but also increased the content of surface lattice oxygen and decreased the surface basicity. The observed effects on the structures and catalytic performance suggest that the Li content is helpful in suppressing the formation of completely oxidized CO₂, and increases the C₂ selectivity. Moreover, increasing the Li content of the catalyst facilitated the mobility of the lattice oxygen, which triggered the promotion of CH₄ activation, thereby enhancing the OCM catalytic performance. The Mn content acted as the active sites for OCM; therefore, the performance of the catalyst was closely related to the Mn concentration and valence state. However, the WO₃/TiO₂-supported catalyst with excessive Mn content exhibited a high surface basicity, high valence state of Mn, and low abundant lattice oxygen, which was unfavorable for C₂ selectivity. The Raman spectroscopy results revealed that MnTiO₃ was formed due to the co-existence of Li and Mn on WO₃/TiO₂, and played an essential role in improving the low-temperature OCM performance. There was a synergic effect of the Li and Mn components on the OCM. The optimal performance (16.3% C₂ yield) was achieved over the WO₃/TiO₂-supported lithium-manganese catalyst with n(Li) : n(Mn) = 2 : 1 at 750 ℃.

Key words: OCM, Mn species, WO₃/TiO₂, Lattice oxygen, MnTiO₃

MSC2000:

O643

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程飞,杨建,闫亮,赵军,赵华华,宋焕玲,丑凌军. 固体酸WO₃/TiO₂负载锂锰催化剂组成对其甲烷氧化偶联反应性能的影响[J]. 物理化学学报, 2019, 35(9): 1027-1036.

Fei CHENG,Jian YANG,Liang YAN,Jun ZHAO,Huahua ZHAO,Huanling SONG,Lingjun CHOU. Influence of the Composition/Texture of Solid Acid WO₃/TiO₂-Supported Lithium-Manganese Catalysts on the Oxidative Coupling of Methane[J]. Acta Physico-Chimica Sinica, 2019, 35(9): 1027-1036.

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参考文献 51

1	Ji S. F. ; Xiao T. C. ; Li S. B. ; Chou L. J. ; Zhang B. ; Xu C. Z. ; Hou R. L. ; York A. P. E. ; Green M. L. H. J. Catal. 2003, 220, 47. doi: 10.1016/S0021-9517(03)00248-3
2	Elkins T. W. ; Roberts S. J. ; Hagelin-Weaver H. E. Appl. Catal. A Gen. 2016, 528, 175. doi: 10.1016/j.apcata.2016.09.011
3	Lee H. ; Lee D. H. ; Ha J. M. ; Kim D. H. Appl. Catal. A Gen. 2018, 557, 39. doi: 10.1016/j.apcata.2018.03.007
4	Igenegbai V. O. ; Meyer R. J. ; Linic S. Appl. Catal. B Environ. 2018, 230, 29. doi: 10.1016/j.apcatb.2018.02.040
5	Keller G. E. ; Bhasin M. M. J. Catal. 1982, 73, 9. doi: 10.1016/0021-9517(82)90075-6
6	Rane V. H. ; Chaudhari S. T. ; Choudhary V. R. J. Nat. Gas Chem. 2008, 17, 313. doi: 10.1016/S1003-9953(09)60001-3
7	Cheng F. ; Yang J. ; Yan L. ; Zhao J. ; Zhao H. H. ; Song H. L. ; Chou L. J. React. Kinet. Mech. Cat. 2018, 125, 675. doi: 10.1007/s11144-018-1477-y
8	Wang P. W. ; Zhang X. ; Zhao G. F. ; Liu Y. ; Lu Y. Chin. J. Catal. 2018, 39, 1395. doi: 10.1016/S1872-2067(18)63076-1
9	Arandiyan H. ; Dai H. X. ; Deng J. G. ; Wang Y. ; Sun H. Y. ; Xie S. H. ; Bai B. Y. ; Liu Y. ; Ji K. M. ; Li J. H. J. Phys. Chem. C 2014, 118, 14913. doi: 10.1021/jp502256t
10	Takanabe K. ; Iglesia E. J. Phys. Chem. C 2009, 113, 10131. doi: 10.1021/jp9001302
11	Zavyalova U. ; Holena M. ; Schlögl R. ; Baerns M. ChemCatChem 2011, 3, 1935. doi: 10.1002/cctc.201100186
12	Dubois J. L. ; Rebours B. ; Cameron C. J. Appl. Catal. 1990, 67, 73. doi: 10.1016/S0166-9834(00)84432-2
13	Luo L. F. ; Jin Y. K. ; Pan H. B. ; Zheng X. S. ; Wu L. H. ; You R. ; Huang W. X. J. Catal. 2017, 346, 57. doi: 10.1002/cctc.201700610
14	Yunarti R. T. ; Lee M. ; Hwang Y. J. ; Choi J. W. ; Suh D. J. ; Lee J. ; Kim I. W. ; Ha J. M. Catal. Commun. 2014, 50, 54. doi: 10.1016/j.catcom.2014.02.026
15	Wang J. X. ; Chou L. J. ; Zhang B. ; Song H. L. ; Zhao J. ; Yang J. ; Li S. B. J. Mol. Catal. A Chem. 2006, 245, 272. doi: 10.1016/j.molcata.2005.09.038
16	Peng L. ; Xu J. W. ; Fang X. Z. ; Liu W. M. ; Xu X. L. ; Liu L. ; Li Z. C. ; Peng H. G. ; Zheng R. Y. ; Wang X. Eur. J. Inorg. Chem. 2018, 2018, 1787. doi: 10.1002/ejic.201701440
17	Kus S. ; Otremba M. ; Taniewski M. Fuel 2003, 82, 1331. doi: 10.1016/S0016-2361(03)00030-9
18	Li Z. N. ; Wang S. L. ; Hong W. ; Zou S. H. ; Xiao L. Q. ; Fan J. ChemNanoMat 2018, 4, 487. doi: 10.1002/cnma.201800019
19	Qin H. L. ; Chen L. ; Yu X. W. ; Wu M. Y. ; Yan Z. C. J. Mater. Sci: Mater. Electron. 2018, 29, 2060. doi: 10.1007/s10854-017-8119-4
20	Zhao W. Y. ; Li Z. Q. ; Wang Y. ; Fan R. R. ; Zhang C. ; Wang Y. ; Guo X. ; Wang R. ; Zhang S. L. Catalysts 2018, 8, 375. doi: 10.3390/catal8090375
21	Shubin A. ; Zilberberg I. ; Ismagilov I. ; Matus E. ; Kerzhentsev M. ; Ismagilov Z. Mol. Catal. 2018, 445, 307. doi: 10.1016/j.mcat.2017.11.039
22	Koirala R. ; Büchel R. ; Pratsinis S. E. ; Baiker A. Appl. Catal. A Gen. 2014, 484, 97. doi: 10.1016/j.apcata.2014.07.013
23	Simon U. ; Villaseca S. A. ; Shang H. H. ; Levchenko S. V. ; Arndt S. ; Epping J. D. ; Görke O. ; Scheffler M. ; Schomäker R. ; Tol J. V. ; et al ChemCatChem 2017, 9, 3597. doi: 10.1002/cctc.201700610
24	Chen F. F. ; Cao F. L. ; Li H. X. ; Bian Z. F. Langmuir 2015, 31, 3494. doi: 10.1021/la5048744
25	Arillo M.Á. ; López M. L. ; Pico C. ; Veiga M. L. Solid State Sci. 2008, 10, 1612. doi: 10.1016/j.solidstatesciences.2008.03.020
26	Vu N. H. ; Arunkumar P. ; Won S. ; Kim H. J. ; Unithrattil S. ; Oh Y. ; Leed J. W. ; Im W. B. Electrochim. Acta 2017, 225, 458. doi: 10.1016/j.electacta.2016.12.180
27	Wang S. H. ; Yang J. ; Wu X. B. ; Li Y. X. ; Gong Z. L. ; Wen W. ; Lin M. ; Yang J. H. ; Yang Y. J. Power Sources 2014, 245, 570. doi: 10.1016/j.jpowsour.2013.07.021
28	Wang P. W. ; Zhao G. F. ; Wang Y. ; Lu Y. Sci. Adv. 2017, 3, 1. doi: 10.1126/sciadv.1603180
29	Song J. J. ; Sun Y. N. ; Ba R. B. ; Huang S. S. ; Zhao Y. H. ; Zhang J. ; Sun Y. H. ; Zhu Y. Nanoscale 2015, 7, 2260. doi: 10.1039/c4nr06660j
30	Istadi ; Amin N. A. S. J. Mol. Catal. A 2006, 259, 61. doi: 10.1016/j.molcata.2006.06.003
31	Chu C. Q. ; Zhao Y. H. ; Li S. G. ; Sun Y. H. Phys. Chem. Chem. Phys. 2016, 18, 16509. doi: 10.1039/c6cp02459a
32	Istadi A. N. A. S. J. Nat. Gas Chem. 2004, 13, 23.
33	Wang Y. ; Arandiyan H. ; Tahini H. A. ; Scott J. ; Tan X. ; Dai H. ; Gale J. D. ; Rohl A. L. ; Smith S. C. ; Amal R. Nat. Commun. 2017, 8, 15553. doi: 10.1038/ncomms15553
34	Chou L. J. ; Cai Y. C. ; Zhang B. ; Niu J. Z. ; Ji S. F. ; Li S. B. Appl. Catal. A Gen. 2003, 238, 185. doi: 10.1016/S0926-860X(02)00343-5
35	Jeon W. ; Lee J. Y. ; Lee M. ; Choi J. W. ; Ha J. M. ; Suh D. J. ; Kim I. W. Appl. Catal. A Gen. 2013, 464-465, 68. doi: 10.1016/j.apcata.2013.05.020
36	Fleischer V. ; Steuer R. ; Parishan S. ; Schomäcker R. J. Catal. 2016, 341, 91. doi: 10.1016/j.jcat.2016.06.014
37	Palermo A. ; Vazquez J. P. H. ; Lee A. F. ; Tikhov M. S. ; Lambert R. M. J. Catal. 1998, 177, 259. doi: 10.1006/jcat.1998.2109
38	Liu W. C. ; Ralston W. T. ; Melaet G. ; Somorjai G. A. Appl. Catal. A Gen. 2017, 545, 17. doi: 10.1016/j.apcata.2017.07.017
39	Jiang Z. C. ; Gong H. ; Li S. B. Stud. Surf. Sci. Catal. 1997, 112, 481. doi: 10.1016/S0167-2991(97)80872-5
40	Lomonosov V. I. ; Gordienko Y. A. ; Sinev M. Y. ; Rogov V. A. ; Sadykov V. A. Russ. J. Phys. Chem. A 2018, 92, 430. doi: 10.1134/S0036024418030147
41	Shahri S. M. K. ; Alavi S. M. J. Nat. Gas Chem. 2009, 18, 25. doi: 10.1016/S1003-9953(08)60079-1
42	Xu X. L. ; Liu F. ; Han X. ; Wu Y. Y. ; Liu W. M. ; Zhang R. B. ; Zhang N. ; Wang X. Catal. Sci. Technol. 2016, 6, 5280. doi: 10.1039/c5cy01870f
43	Sun G. B. ; Hidajat K. ; Wu X. S. ; Kawi S. Appl. Catal. B Environ. 2008, 81, 303. doi: 10.1016/j.apcatb.2007.12.021
44	Brabers V. A. M. ; Setten F. M. V. ; Knapen P. S. A. J. Solid State Chem. 1983, 49, 93. doi: 10.1016/0022-4596(83)90220-7
45	Zheng W. ; Cheng D. G. ; Zhu N. ; Chen F. Q. ; Zhan X. L. J. Nat. Gas Chem. 2010, 19, 15. doi: 10.1016/S1003-9953(09)60029-3
46	Arndt S. ; Otremba T. ; Simon U. ; Yildiz M. ; Schubert H. ; Schomäcker R. Appl. Catal. A Gen. 2012, 425-426, 53. doi: 10.1002/chin.201229234
47	Jiang Z. C. ; Yu C. J. ; Fang X. P. ; Li S. B. ; Wang H. L. J. Phys. Chem. 1993, 97, 12870. doi: 10.1021/j100151a038
48	Kang M. ; Park E. D. ; Kim J. M. ; Yie J. E. Appl. Catal. A Gen. 2007, 327, 261. doi: 10.1016/j.apcata.2007.05.024
49	Gambo Y. ; Jalila A. A. ; Triwahyono S. ; Abdulrasheed A. A. J. Ind. Eng. Chem. 2018, 59, 218. doi: 10.1016/j.jiec.2017.10.027
50	Lee M. R. ; Park M. J. ; Jeon W. ; Choi J. W. ; Suh Y. W. ; Suh D. J. Fuel Process. Technol. 2012, 96, 175. doi: 10.1016/j.fuproc.2011.12.038
51	Sun J. ; Thybaut J. W. ; Marin G. B. Catal. Today 2008, 137, 90. doi: 10.1016/j.cattod.2008.02.026

Catalyst	Catalyst Catalyst bed temperature (℃)	Conversion (%)	Selectivity (%)				Yield (%)
Catalyst	Catalyst Catalyst bed temperature (℃)	CH₄	C₂	C₂H₄	CO₂	CO	C₂	C₂H₄
WT	756.6	12.1	1.2	0.0	13.7	85.2	0.0	0
Mn/WT	760.9	16.1	11.7	4.1	73.2	9.6	1.9	0.7
Li-Mn/WT	763.4	28.2	52.5	32.2	33.2	11.8	1 4.8	9.1
2Li-Mn/WT	761.0	28.1	58.0	36.6	25.6	14.9	1 6.3	1 0.3
3Li-Mn/WT	758.4	25.3	60.8	37.9	21.6	15.2	15.4	9.6
Li/WT	752.3	9.8	55.3	17.9	31.7	8.5	5.4	1.7
2Li-2Mn/WT	762.9	28.6	51.3	31.7	35.8	11.0	14.7	9.1
2Li-3Mn/WT	764.9	28.3	48.5	30.0	39.5	10.1	13.7	8.5

Catalyst	Li/Mn atomic ratio
Catalyst	fresh	used
Li-Mn/WT	1.01 /1	0.99/1
2Li-Mn/WT	2.00/1	1.98/1
3Li-Mn/WT	3.03/1	2.96/1
2Li-2Mn/WT	1.99/2	1.98/2
2Li-3Mn/WT	1.98/3	1.91/3

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[5]	侯思聪;刘凌涛;寇元. 低温甲烷氧化偶联Li- ZnO/La₂O₃催化剂[J]. 物理化学学报, 2006, 22(08): 1040 -1042 .
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[7]	李绪渊,张自萍,马建泰,朱宗祯,孟益民. 钙钛矿型La_1+X/2Sr_1-x/2Co_1-xCu_xO₃催化CO氧化活性与表征[J]. 物理化学学报, 1996, 12(06): 502 -507 .
[8]	王必勋,伏义路,方书农. Cu-ZSM-5分子筛上[Cu-O-Cu]²⁺物种的原位红外光谱研究[J]. 物理化学学报, 1995, 11(11): 974 -978 .
[9]	余林,徐奕德,郭燮贤. 红外光谱研究甲烷和氧与SrO-La₂O₃/CaO表面的相互作用[J]. 物理化学学报, 1995, 11(10): 902 -906 .
[10]	纪敏, 毕颖丽, 甄开吉, 徐立羽华, 魏诠. 利用Eu³⁺荧光特性研究CaO-La₂O₃催化剂结构[J]. 物理化学学报, 1995, 11(02): 175 -179 .
[11]	熊国兴, 夏新瑞, 陈恒荣, 郭燮贤. NaCl和B₂O₃在修饰FeO_χ催化剂中的协同作用[J]. 物理化学学报, 1994, 10(11): 971 -977 .
[12]	赵震, 远松月, 于作龙. 锂在甲烷氧化偶联多元氧化物催化剂中的作用[J]. 物理化学学报, 1994, 10(07): 616 -622 .
[13]	罗晓鸣;韩巧凤;陈懿;韩世莹;金通政;睦云霞. Na₂SnO₃系催化剂表面吸附氧的EPR研究[J]. 物理化学学报, 1993, 9(06): 746 -751 .
[14]	王江;甄开吉;魏诠;毕颖丽. ABO₃型稀土铝酸盐的表面状态及其催化性能[J]. 物理化学学报, 1992, 8(02): 247 -250 .

固体酸WO₃/TiO₂负载锂锰催化剂组成对其甲烷氧化偶联反应性能的影响

Influence of the Composition/Texture of Solid Acid WO₃/TiO₂-Supported Lithium-Manganese Catalysts on the Oxidative Coupling of Methane

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