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Chinese Journal of Materials Research  2018, Vol. 32 Issue (3): 225-232    DOI: 10.11901/1005.3093.2017.320
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Preparation of Foam Structured Catalyst ZnFe2O4-α-Fe2O3/SiC and its Performance in Oxidative Dehydrogenation of Butene
Renzheng JIANG1,2, Yilai JIAO1, Bo SUN1, Xiaodan YANG1, Zhenming YANG1, Jinsong ZHANG1()
1 Institute of Metal Research, Chinese Academy of Sciences, Shenyang 110016, China;
2 University of Chinese Academy of Sciences, Beijing 100049, China;
Cite this article: 

Renzheng JIANG, Yilai JIAO, Bo SUN, Xiaodan YANG, Zhenming YANG, Jinsong ZHANG. Preparation of Foam Structured Catalyst ZnFe2O4-α-Fe2O3/SiC and its Performance in Oxidative Dehydrogenation of Butene. Chinese Journal of Materials Research, 2018, 32(3): 225-232.

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Abstract  

A foam structured catalyst of ZnFe2O4-α-Fe2O3/SiC was prepared by a slurry-coating method with citric acid-nitrates as binder. Its phase composition, morphology and pore structure were characterized by XRD, SEM and BET. The influence of the concentration of citric acid-nitrates and the deposited amount of slurry on the morphology, pore structure and catalytic performance in the oxidative dehydrogenation of 1-butene of the prepared catalyst were investigated. The result show that the concentration of citric acid-nitrates hardly changed the phase composition; the as-prepared structured catalyst has a compact and neat coating with a wide range distribution of pore size; the concentration of citric acid-nitrates of the slurry or the most probable pore size of the as-prepared catalyst has a little influence on the peformance of the structured catalyst. The BET surface area and the catalytic performance of the structured catalyst gradually increased with the incresing the deposited amount of slurry. In case of gas firing hourly space velocity of bntene of 300 h-1, the conversion rate of 1-butene and selectivity of butadiene reache ca. 86% and 91%, respectively for the prepared structured catalyst with a deposited amount of 0.2 g/mL slurry, which are much higher than that for particulate catalysts, indicating superior oxidative dehydrogenation performance.

Key words:  inorganic non-metallic materials      ZnFe2O4-α-Fe2O3;      foam SiC      structured catalyst      1-butene oxidative dehydrogenation      slurry-coating     
Received:  17 May 2017     
ZTFLH:  TQ031  

URL: 

https://www.cjmr.org/EN/10.11901/1005.3093.2017.320     OR     https://www.cjmr.org/EN/Y2018/V32/I3/225

Fig.1  XRD patterns of ZF-0 particles, ZF-0.11 particles, ZFS-0.2 structured catalyst and foam SiC
Fig.2  SEM images of foam SiC and ZFS-0.2 structured catalyst (a) Foam SiC, (b) strut surface with Si, (c) strut surface without Si and (d) cross section of ZFS-0.2 structured catalyst
Fig.3  High (a, b, c, d) and low (a1, b1, c1, d1) magnification images of ZFS-0.2 structured catalysts CNS concentration of a, b, c and d is 0.11, 0.44, 0.88 and 1.32 mol/L, respectively
Coating powders BET surface
areaa / m2g-1
Pore volumeb
/ cm3g-1
ZF-0 7.69 0.074
ZF-0.11 9.77 0.234
ZF-0.44 8.96 0.144
ZF-0.88 8.40 0.071
ZF-1.32 9.69 0.078
binder c 19.51 0.229
Table 1  BET surface areas and total pore volumes of ZF-c coating particles
Fig.4  Pore diameter size distribution of ZF-c coating particles
Fig.5  Images of ZFS-w structured catalyst with coating loading amount 0.064, 0.082, 0.128, 0.164, 0.2 and 0.223
Coating powders BET surface
areaa/m2g-1
Pore volumeb
/cm3g-1
ZFS-0.064 0.96 0.012
ZFS-0.082 1.589 0.015
ZFS-0.128 1.703 0.019
ZFS-0.164 1.839 0.028
ZFS-0.2 2.29 0.03
ZFS-0.223 2.711 0.033
Table 2  BET surface areas and total pore volumes of ZFS-w structured catalysts
Fig.6  Pore diameter distribution of ZFS-w structured catalyst
Fig.7  Influence of citric acid-nitrates concentration on theperformanceof ZFS-0.2 structured catalyst reaction condition: 1-butene: oxygen: steam=1:0.85:12, 1-butene GHSV=300 h-1
Fig.8  Influence of coating loading on the performance of ZFS structured catalyst reaction condition: 1-butene: oxygen: steam=1:0.85:12, 1-butene GHSV=300 h-1
Fig.9  Performance of ZFS-0.2 structured catalyst, ZF-0.11 particulate catalyst and ZF-0 co-precipitated particulate catalyst reaction condition: 1-butene:oxygen:steam=1:0.85:12, 1-butene GHSV=300 h-1
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