✦ LIBER ✦

Effect of column inclination on the performance of three-phase fluidized beds

✍ Scribed by M. Del Pozo; C. L. Briens; G. Wild

Publisher: American Institute of Chemical Engineers
Year: 1992
Tongue: English
Weight: 524 KB
Volume: 38
Category: Article
ISSN: 0001-1541
DOI: 10.1002/aic.690380808

No coin nor oath required. For personal study only.

📜 SIMILAR VOLUMES

Effect of particle stratification on the

Effect of particle stratification on the performance of fluidized adsorption beds

✍ V. S. Patwardhan; Chi Tien 📂 Article 📅 1986 🏛 American Institute of Chemical Engineers 🌐 English ⚖ 339 KB 👁 2 views

Effect of reactor diameter on gas-liquid

Effect of reactor diameter on gas-liquid mass transfer in three-phase fluidized beds

✍ K. Nguyen-Tien; A. Schumpe; W.-D. Deckwer 📂 Article 📅 1985 🏛 American Institute of Chemical Engineers 🌐 English ⚖ 250 KB 👁 2 views

Performance of a three-phase fluidized b

Performance of a three-phase fluidized bed as a reactive distillation device

✍ Dr. Wugeng Liang; Prof. Zhanwen Wang; Prof. Yong Jin; Prof. Zhiqing Yu; Mr. Shen 📂 Article 📅 1996 🏛 John Wiley and Sons 🌐 English ⚖ 589 KB

Flow regimes of the three-phase circulat

Flow regimes of the three-phase circulating fluidized bed

✍ W. G. Liang; Q. W. Wu; Z. Q. Yu; Y. Jin; H. T. Bi 📂 Article 📅 1995 🏛 American Institute of Chemical Engineers 🌐 English ⚖ 389 KB 👁 2 views

The effect of column diameter and bed he

The effect of column diameter and bed height on minimum fluidization velocity

✍ Akhil Rao; Jennifer S. Curtis; Bruno C. Hancock; Carl Wassgren 📂 Article 📅 2010 🏛 American Institute of Chemical Engineers 🌐 English ⚖ 493 KB 👁 2 views

Baffle effects on performance of catalyt

Baffle effects on performance of catalytic circulating fluidized bed reactor

✍ Peijun Jiang; Hsiaotao Bi; Rong-Her Jean; Liang-Shih Fan 📂 Article 📅 1991 🏛 American Institute of Chemical Engineers 🌐 English ⚖ 756 KB

Baffle effects on the performance of a catalytic circulating fluidized bed reactor were examined experimentally. The circulating fluidized bed reactor or riser was 102 mm in diameter and 6.32 m in height. Reaction was the catalytic decomposition of ozone using FCCparticles with a mean diameter of 89