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Effect of Si/Al ratio of the starting NaY on hydro-upgrading catalyst performance  
×÷Õß: Wang, FC (Wang, Fucun)1,2; Wang, LA (Wang, Liang)3; Zhu, JL (Zhu, Jinling)2; Zhang, XJ (Zhang, Xuejun)2; Yan, ZF (Yan, Zifeng)1; Fang, F (Fang, Fang)3; Tian, R (Tian, Ran)2; Zhang, ZH (Zhang, Zhihua)2; Shen, BJ (Shen, Baojian)3  
À´Ô´³ö°æÎï: CATALYSIS TODAY  ¾í: 158   ÆÚ: 3-4   Ò³: 409-414   DOI: 10.1016/j.cattod.2010.05.041   ³ö°æÄê: DEC 22 2010  
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ÎÄÏ×ÀàÐÍ: Article  
ÓïÖÖ: English  
ͨѶ×÷ÕßµØÖ·: Yan, ZF (ͨѶ×÷Õß),China Univ Petr, CNPC Key Lab Catalysis, State Key Lab Heavy Oil Proc, Qingdao 266555, Peoples R China  
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1. China Univ Petr, CNPC Key Lab Catalysis, State Key Lab Heavy Oil Proc, Qingdao 266555, Peoples R China
2. Daqing Petrochem Res Ctr PetroChina, Daqing 163714, Peoples R China
3. China Univ Petr, CNPC Key Lab Catalysis, State Key Lab Heavy Oil Proc, Beijing 102249, Peoples R China
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Accession number:  20104813434957

Title:  Effect of Si/Al ratio of the starting NaY on hydro-upgrading catalyst performance

Authors:  Wang, Fucun1, 2 ; Wang, Liang3 ; Zhu, Jinling2 ; Zhang, Xuejun2 ; Yan, Zifeng1 ; Fang, Fang3 ; Tian, Ran2 ; Zhang, Zhihua2 ; Shen, Baojian3   

Author affiliation:  1  State Key Laboratory of Heavy Oil Processing, CNPC Key Laboratory of Catalysis, China University of Petroleum, Qingdao 266555, China

2  Daqing Petrochemical Research Center of PetroChina, Daqing 163714, China

3  State Key Laboratory of Heavy Oil Processing, CNPC Key Laboratory of Catalysis, China University of Petroleum, Beijing 102249, China


Corresponding author:  Shen, B. (baojian@cup.edu.cn)  

Source title:  Catalysis Today

Abbreviated source title:  Catal Today

Volume:  158

Issue:  3-4

Issue date:  December 22, 2010

Publication year:  2010

Pages:  409-414

Language:  English

ISSN:  09205861

CODEN:  CATTEA

Document type:  Conference article (CA)

Publisher:  Elsevier, P.O. Box 211, Amsterdam, 1000 AE, Netherlands

Abstract:  The effect of Si/Al ratio of the starting NaY on hydro-upgrading catalyst performance for LCO was studied. Y type zeolite modified from higher Si/Al ratio of the starting NaY also had higher framework Si/Al ratio. Three catalysts of W-Ni supported on different modified Y type zeolites and Al2O 3 were prepared by impregnation method. The catalysts were characterized by XRD, BET, DRS and HRTEM, and evaluated with a micro-reactor using tetralin as a model compound and a 100 ml hydrogenation test unit using FCC LCO as feedstocks. By contrast, tungsten supported on Y type zeolite modified from higher Si/Al ratio of the starting NaY zeolite had more type II active phase and WS2 is highly stacked, exhibiting the weak interaction with Al2O3 and should have higher activity. The revaluation results revealed that the catalyst prepared by higher Si/Al ratio of the starting NaY zeolite has higher tetralin conversion and better hydro-upgrading performance for FCC LCO. © 2010 Elsevier B.V.

Number of references:  32

Main heading:  Catalysts

Controlled terms:  Aromatic hydrocarbons  -  Silicate minerals  -  Tungsten

Uncontrolled terms:  Catalyst performance  -  Hydro-upgrading catalyst  -  Impregnation methods  -  Micro-reactor  -  Model compound  -  NaY  -  NaY zeolite  -  Si/Al ratio  -  Test unit  -  Tetralin conversions   -  Tetralins  -  Type II  -  Weak interactions  -  XRD  -  Y-type zeolites

Classification code:  482.2 Minerals  -  543.5 Tungsten and Alloys  -  803 Chemical Agents and Basic Industrial Chemicals  -  804 Chemical Products Generally  -  804.1 Organic Compounds

DOI:  10.1016/j.cattod.2010.05.041

Database:  Compendex



   Compilation and indexing terms, © 2012 Elsevier Inc.
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Accession number:  20104813434957
  Title:  Effect of Si/Al ratio of the starting NaY on hydro-upgrading catalyst performance
  Authors:  Wang, Fucun1, 2 ; Wang, Liang3 ; Zhu, Jinling2 ; Zhang, Xuejun2 ; Yan, Zifeng1 ; Fang, Fang3 ; Tian, Ran2 ; Zhang, Zhihua2 ; Shen, Baojian3   

Author affiliation:  1  State Key Laboratory of Heavy Oil Processing, CNPC Key Laboratory of Catalysis, China University of Petroleum, Qingdao 266555, China
2  Daqing Petrochemical Research Center of PetroChina, Daqing 163714, China
3  State Key Laboratory of Heavy Oil Processing, CNPC Key Laboratory of Catalysis, China University of Petroleum, Beijing 102249, China
   Corresponding author:  Shen, B. (baojian@cup.edu.cn)  
  Source title:  Catalysis Today
  Abbreviated source title:  Catal Today
  Volume:  158
  Issue:  3-4

Issue date:  December 22, 2010

Pblication year:  2010
  Pages:  409-414
  Language:  English
  ISSN:  09205861
  CODEN:  CATTEA
  Document type:  Conference article (CA)
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FN Thomson Reuters Web of Knowledge
VR 1.0
PT  J
AU  Wang, FC
Wang, LA
Zhu, JL
Zhang, XJ
Yan, ZF
Fang, F
Tian, R
Zhang, ZH
Shen, BJ
AF  Wang, Fucun
Wang, Liang
Zhu, Jinling
Zhang, Xuejun
Yan, Zifeng
Fang, Fang
Tian, Ran
Zhang, Zhihua
Shen, Baojian
TI  Effect of Si/Al ratio of the starting NaY on hydro-upgrading catalyst performance
SO  CATALYSIS TODAY
LA  English
DT  Article
DE  Si/Al ratio; NaY; Type II phase; Hydro-upgrading catalyst
ID  PT-PD CATALYSTS; HYDROTREATING CATALYSTS; Y-ZEOLITE; GAS OIL; HYDRODESULFURIZATION; HYDROGENATION; SUPPORT; MO; TETRALIN; ALUMINUM
AB  The effect of Si/Al ratio of the starting NaY on hydro-upgrading catalyst performance for LCO was studied. Y type zeolite modified from higher Si/Al ratio of the starting NaY also had higher framework Si/Al ratio. Three catalysts of W-Ni supported on different modified Y type zeolites and Al2O3 were prepared by impregnation method. The catalysts were characterized by XRD, BET, DRS and HRTEM, and evaluated with a micro-reactor using tetralin as a model compound and a 100 ml hydrogenation test unit using FCC LCO as feedstocks. By contrast, tungsten supported on Y type zeolite modified from higher Si/Al ratio of the starting NaY zeolite had more type II active phase and WS2 is highly stacked, exhibiting the weak interaction with Al2O3 and should have higher activity. The revaluation results revealed that the catalyst prepared by higher Si/Al ratio of the starting NaY zeolite has higher tetralin conversion and better hydro-upgrading performance for FCC LCO. (C) 2010 Elsevier B.V. All rights reserved.
C1  [Wang, Fucun; Yan, Zifeng] China Univ Petr, CNPC Key Lab Catalysis, State Key Lab Heavy Oil Proc, Qingdao 266555, Peoples R China.
[Wang, Fucun; Zhu, Jinling; Zhang, Xuejun; Tian, Ran; Zhang, Zhihua] Daqing Petrochem Res Ctr PetroChina, Daqing 163714, Peoples R China.
[Wang, Liang; Fang, Fang; Shen, Baojian] China Univ Petr, CNPC Key Lab Catalysis, State Key Lab Heavy Oil Proc, Beijing 102249, Peoples R China.
RP  Yan, ZF (reprint author), China Univ Petr, CNPC Key Lab Catalysis, State Key Lab Heavy Oil Proc, Qingdao 266555, Peoples R China
EM  zfyancat@upc.edu.cn baojian@cup.edu.cn
FU  PetroChina[06-03A-01-05]
FX  The authors gratefully acknowledge the funding of the research project under contract number 06-03A-01-05 by PetroChina for financial support.
NR  32
TC  1
Z9  1
PU  ELSEVIER SCIENCE BV
PI  AMSTERDAM
PA  PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS
SN  0920-5861
J9  CATAL TODAY
JI  Catal. Today
PD  DEC 22
PY  2010
VL  158
IS  3-4
BP  409
EP  414
DI  10.1016/j.cattod.2010.05.041
PG  6
WC  Chemistry, Applied; Chemistry, Physical; Engineering, Chemical
SC  Chemistry; Engineering
GA  684VW
UT  WOS:000284583300034
ER  

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