Direct synthesis of dimethyl ether from CO2 and H2 over novel bifunctional catalysts containing CuO-ZnO-ZrO2 catalyst admixed with WOx/ZrO2 catalysts

被引:41
作者
Witoon, Thongthai [1 ,2 ,3 ]
Kidkhunthod, Pinit [4 ]
Chareonpanich, Metta [1 ,2 ,3 ]
Limtrakul, Jumras [5 ]
机构
[1] Kasetsart Univ, Dept Chem Engn, Fac Engn, Ctr Excellence Petrochem & Mat Technol, Bangkok 10900, Thailand
[2] Kasetsart Univ, NANOTEC Ctr Nanoscale Mat Design Green Nanotechno, Bangkok 10900, Thailand
[3] Kasetsart Univ, Ctr Adv Studies Nanotechnol Chem Food & Agr Ind, Bangkok 10900, Thailand
[4] Synchrotron Light Res Inst Publ Org, Nakhon Ratchasima 30000, Thailand
[5] Vidyasirimedhi Inst Sci & Technol, Dept Mat Sci & Engn, Inst Mol Sci & Engn, Rayong 21210, Thailand
关键词
CO(2)hydrogenation; Dimethyl ether; Cu-based catalysts; Methanol; Dehydration; Tungsten-zirconia; METHANOL DEHYDRATION; SULFATED ZIRCONIA; HYBRID CATALYSTS; TO-OLEFINS; HYDROGENATION; ACID; OXIDE; PERFORMANCE; DME; ZEOLITE;
D O I
10.1016/j.cej.2018.05.057
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The present work examined the performance of WOx/ZrO2 catalysts calcined at different temperatures admixed with a Cu-ZnO-ZrO2 catalyst for CO2-to-dimethyl ether (DME) hydrogenation. The effect of operating conditions including reaction temperature, pressure and space velocity was also investigated. The calcination temperature was found to play a crucial role on the physicochemical properties of the WOx/ZrO2 catalysts as well as their catalytic performance. Increasing calcination temperature from 600 to 800 degrees C led to a gradual increase of W surface density (2.82-4.82 W nm(-2)) which was accompanied by an increase of both quantity and strength of acid sites. The WOx/ZrO2 catalyst calcined at 900 degrees C showed W surface density of 9.63 W nm(-2) which was higher than theoretical monolayer surface coverage of W (similar to 8 W nm(-2)), indicating the saturation coverage of WOx species coexisted with a small portion of nanocrystalline WO3. At calcination temperature of 1000 degrees C, the monoclinic ZrO2, bulk WO3 particles and ZrW2O8 phase were formed because of a drastic reduction in BET surface area (similar to 5 m(2)g(-1)). The CuO-ZnO-ZrO2 catalyst admixed with WOx/ZrO2 catalyst calcined at 900 degrees C exhibited the highest space-time yield of DME of 271.2 g(DME) kg(cat)(-1) h(-1) during a 48-h test at 260 degrees C, 30 bars and a space velocity of 4333.33 mL g(cat)(-1) h(-1).
引用
收藏
页码:713 / 722
页数:10
相关论文
共 55 条
[1]   Methanol dehydration to dimethylether over Al2O3 catalysts [J].
Akarmazyan, Siranush S. ;
Panagiotopoulou, Paraskevi ;
Kambolis, Anastasios ;
Papadopoulou, Christina ;
Kondarides, Dimitris I. .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2014, 145 :136-148
[2]   Challenges in the Greener Production of Formates/Formic Acid, Methanol, and DME by Heterogeneously Catalyzed CO2 Hydrogenation Processes [J].
Alvarez, Andrea ;
Bansode, Atul ;
Urakawa, Atsushi ;
Bavykina, Anastasiya V. ;
Wezendonk, Tim A. ;
Makkee, Michiel ;
Gascon, Jorge ;
Kapteijn, Freek .
CHEMICAL REVIEWS, 2017, 117 (14) :9804-9838
[3]   Dimethyl ether synthesis from CO2 hydrogenation on a CuO-ZnO-Al2O3-ZrO2/HZSM-5 bifunctional catalyst [J].
An, Xin ;
Zuo, Yi-Zan ;
Zhang, Qiang ;
Wang, De-zheng ;
Wang, Jin-Fu .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2008, 47 (17) :6547-6554
[4]   Performance of CuO-ZnO-ZrO2 and CuO-ZnO-MnO as metallic functions and SAPO-18 as acid function of the catalyst for the synthesis of DME co-feeding CO2 [J].
Ateka, Ainara ;
Sierra, Irene ;
Erena, Javier ;
Bilbao, Javier ;
Aguayo, Andres T. .
FUEL PROCESSING TECHNOLOGY, 2016, 152 :34-45
[5]   WATER-GAS SHIFT REACTION - EFFECT OF PRESSURE ON RATE OVER AN IRON OXIDE CHROMIUM OXIDE CATALYST [J].
ATWOOD, K ;
ARNOLD, MR ;
APPEL, EG .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1950, 42 (08) :1600-1602
[6]   Genesis of Bronsted acid sites during dehydration of 2-butanol on tungsten oxide catalysts [J].
Baertsch, CD ;
Komala, KT ;
Chua, YH ;
Iglesia, E .
JOURNAL OF CATALYSIS, 2002, 205 (01) :44-57
[7]   Dimethyl ether-to-olefins over aluminum rich ZSM-5: The role of Ca and La as modifiers [J].
Bakare, Idris A. ;
Muraza, Oki ;
Sanhoob, Mohammed A. ;
Miyake, Koji ;
Hirota, Yuichiro ;
Yamani, Zain H. ;
Nishiyama, Norikazu .
FUEL, 2018, 211 :18-26
[8]   Solid acid catalysts based on supported tungsten oxides [J].
Barton, DG ;
Soled, SL ;
Iglesia, E .
TOPICS IN CATALYSIS, 1998, 6 (1-4) :87-99
[9]   Structure and electronic properties of solid acids based on tungsten oxide nanostructures [J].
Barton, DG ;
Shtein, M ;
Wilson, RD ;
Soled, SL ;
Iglesia, E .
JOURNAL OF PHYSICAL CHEMISTRY B, 1999, 103 (04) :630-640
[10]   The influence of different promoter oxides on the functionality of hybrid CuZn-ferrierite systems for the production of DME from CO2-H2 mixtures [J].
Bonura, G. ;
Cannilla, C. ;
Frusteri, L. ;
Frusteri, F. .
APPLIED CATALYSIS A-GENERAL, 2017, 544 :21-29