Abstract
The goal of this study was to investigate the Cs-promoted Ni/Fe catalysts for high temperature shift reaction. The performance of all the catalysts was evaluated at 400 °C and 75,000 ml/gcat h under the reactant composition: 56.7% H2, 10% CO, 26.7% H2O, and 6.7% CO 2, assuming gas production from the steam methane reformer at a H2O/CH4 ratio = 3 with 100% CH4 conversion and with no extra steam added for the protection of the catalyst. The Cs/Ni/Fe (Ni:Fe = 34:66; weight ratio) catalysts of 3.9-6.0 Cs wt.% showed excellent CO removal activities and suppressed the progress of methanation effectively. This performance was related to the increment of amount in weakly basic sites through Cs promotion.
| Original language | English |
|---|---|
| Pages (from-to) | 37-40 |
| Number of pages | 4 |
| Journal | Catalysis Communications |
| Volume | 15 |
| Issue number | 1 |
| DOIs | |
| Publication status | Published - 2011 Nov 15 |
Fingerprint
Keywords
- Alkali-metal promoted catalyst
- High temperature shift
- Methanation
- Ni/Fe
- Water gas shift reaction
ASJC Scopus subject areas
- Catalysis
- Process Chemistry and Technology
- Chemistry(all)
Cite this
Cs-promoted Ni/Fe catalyst as a Cr-free, high temperature shift catalyst for steam methane reformate without additional supply of steam. / Lee, Joon Yeob; Lee, Dae Won; Lee, Myung Suk; Lee, Kwan Young.
In: Catalysis Communications, Vol. 15, No. 1, 15.11.2011, p. 37-40.Research output: Contribution to journal › Article
}
TY - JOUR
T1 - Cs-promoted Ni/Fe catalyst as a Cr-free, high temperature shift catalyst for steam methane reformate without additional supply of steam
AU - Lee, Joon Yeob
AU - Lee, Dae Won
AU - Lee, Myung Suk
AU - Lee, Kwan Young
PY - 2011/11/15
Y1 - 2011/11/15
N2 - The goal of this study was to investigate the Cs-promoted Ni/Fe catalysts for high temperature shift reaction. The performance of all the catalysts was evaluated at 400 °C and 75,000 ml/gcat h under the reactant composition: 56.7% H2, 10% CO, 26.7% H2O, and 6.7% CO 2, assuming gas production from the steam methane reformer at a H2O/CH4 ratio = 3 with 100% CH4 conversion and with no extra steam added for the protection of the catalyst. The Cs/Ni/Fe (Ni:Fe = 34:66; weight ratio) catalysts of 3.9-6.0 Cs wt.% showed excellent CO removal activities and suppressed the progress of methanation effectively. This performance was related to the increment of amount in weakly basic sites through Cs promotion.
AB - The goal of this study was to investigate the Cs-promoted Ni/Fe catalysts for high temperature shift reaction. The performance of all the catalysts was evaluated at 400 °C and 75,000 ml/gcat h under the reactant composition: 56.7% H2, 10% CO, 26.7% H2O, and 6.7% CO 2, assuming gas production from the steam methane reformer at a H2O/CH4 ratio = 3 with 100% CH4 conversion and with no extra steam added for the protection of the catalyst. The Cs/Ni/Fe (Ni:Fe = 34:66; weight ratio) catalysts of 3.9-6.0 Cs wt.% showed excellent CO removal activities and suppressed the progress of methanation effectively. This performance was related to the increment of amount in weakly basic sites through Cs promotion.
KW - Alkali-metal promoted catalyst
KW - High temperature shift
KW - Methanation
KW - Ni/Fe
KW - Water gas shift reaction
UR - http://www.scopus.com/inward/record.url?scp=80052548327&partnerID=8YFLogxK
UR - http://www.scopus.com/inward/citedby.url?scp=80052548327&partnerID=8YFLogxK
U2 - 10.1016/j.catcom.2011.08.010
DO - 10.1016/j.catcom.2011.08.010
M3 - Article
AN - SCOPUS:80052548327
VL - 15
SP - 37
EP - 40
JO - Catalysis Communications
JF - Catalysis Communications
SN - 1566-7367
IS - 1
ER -