✦ LIBER ✦

Kinetic Modeling of Fischer-Tropsch Synthesis over Fe/Ce/Al2O3

✍ Scribed by Atashi, Hossein; Fazlollahi, Farhad; Sarkari, Majid; Mirzaei, Ali A.; Allahyari Shahrasb, Mohsen

Book ID: 125846074
Publisher: Walter de Gruyter GmbH & Co. KG
Year: 2011
Tongue: English
Weight: 1018 KB
Volume: 9
Category: Article
ISSN: 2194-5748
DOI: 10.2202/1542-6580.2608

No coin nor oath required. For personal study only.

📜 SIMILAR VOLUMES

Fischer-Tropsch synthesis over Ru/Al2O3

Fischer-Tropsch synthesis over Ru/Al2O3 catalysts

✍ Murata, Kazuhisa ;Okabe, Kiyomi ;Takahara, Isao ;Inaba, Megumu ;Saito, Masahiro 📂 Article 📅 2007 🏛 Springer 🌐 English ⚖ 78 KB

Kinetic Model of Product Distribution ov

Kinetic Model of Product Distribution over Fe Catalyst for Fischer−Tropsch Synthesis †

✍ Zhang, Rongle; Chang, Jie; Xu, Yuanyuan; Cao, Liren; Li, Yongwang; Zhou, Jinglai 📂 Article 📅 2009 🏛 American Chemical Society 🌐 English ⚖ 818 KB

Study on Fe–Al2O3 interaction over preci

Study on Fe–Al2O3 interaction over precipitated iron catalyst for Fischer–Tropsch synthesis

✍ Hai-Jun Wan; Bao-Shan Wu; Cheng-Hua Zhang; Hong-Wei Xiang; Yong-Wang Li; Bin-Fu 📂 Article 📅 2007 🏛 Elsevier Science 🌐 English ⚖ 406 KB

Fischer–Tropsch synthesis: Kinetics and

Fischer–Tropsch synthesis: Kinetics and water effect study over 25%Co/Al2O3 catalysts

✍ Ma, Wenping; Jacobs, Gary; Sparks, Dennis E.; Spicer, Robert L.; Davis, Burtron 📂 Article 📅 2014 🏛 Elsevier Science 🌐 English ⚖ 716 KB

Kinetics modelling of Fischer–Tropsch sy

Kinetics modelling of Fischer–Tropsch synthesis over an industrial Fe–Cu–K catalyst

✍ Yi-Ning Wang; Wen-Ping Ma; Yi-Jun Lu; Jun Yang; Yuan-Yuan Xu; Hong-Wei Xiang; Yo 📂 Article 📅 2003 🏛 Elsevier Science 🌐 English ⚖ 284 KB

Kinetics modelling of Fischer–Tropsch sy

Kinetics modelling of Fischer–Tropsch synthesis over an industrial Fe–Cu–K catalyst

✍ Yi-Ning Wang; Wen-Ping Ma; Yi-Jun Lu; Jun Yang; Yuan-Yuan Xu; Hong-Wei Xiang; Yo 📂 Article 📅 2003 🏛 Elsevier Science 🌐 English ⚖ 284 KB

The kinetic experiments of Fischer -Tropsch synthesis (FTS) over an industrial Fe -Cu-K catalyst are carried out in a micro-fixed-bed reactor under the conditions as follows: temperature of 493-542 K, pressure of 10.9 -30.9 bar, H 2 /CO feed ratio of 0.98 -2.99, and space velocity of 4000-10 000 h 2