Heat transfer on a vertical tube bundle immersed in a 0.70 m fluidized bed

H.W. Piepers; P. Wiewiorski; K. Rietema

Heat transfer on a vertical tube bundle immersed in a 0.70 m fluidized bed

H.W. Piepers, P. Wiewiorski, K. Rietema

Chemical Engineering and Chemistry

Research output: Chapter in Book/Report/Conference proceeding › Conference contribution › Academic › peer-review

Abstract

The heat transfer was studied on a large vertical tube bundle (19 tubes) immersed in spent cracking catalyst fluidized bed. Heat transfer measurements were performed with only 1 tube, in which 10 elec. heating elements were mounted, at 3 different positions and at superficial gas velocity of 0.40 m/s. The heat transfer is not only detd. by the bubble activity but is strongly affected by the dense phase overall circulation induced by the rising bubbles which tend to move to the center of the bed

Original language	English
Title of host publication	Fluidization IV ; Proceedings of the 4th International Conference on Fluidization, Kashikojima, Japan
Place of Publication	New York
Publisher	Engineering Foundation
Pages	339-346
Publication status	Published - 1983

Cite this

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title = "Heat transfer on a vertical tube bundle immersed in a 0.70 m fluidized bed",

abstract = "The heat transfer was studied on a large vertical tube bundle (19 tubes) immersed in spent cracking catalyst fluidized bed. Heat transfer measurements were performed with only 1 tube, in which 10 elec. heating elements were mounted, at 3 different positions and at superficial gas velocity of 0.40 m/s. The heat transfer is not only detd. by the bubble activity but is strongly affected by the dense phase overall circulation induced by the rising bubbles which tend to move to the center of the bed",

author = "H.W. Piepers and P. Wiewiorski and K. Rietema",

year = "1983",

language = "English",

pages = "339--346",

booktitle = "Fluidization IV ; Proceedings of the 4th International Conference on Fluidization, Kashikojima, Japan",

publisher = "Engineering Foundation",

}

Heat transfer on a vertical tube bundle immersed in a 0.70 m fluidized bed. / Piepers, H.W.; Wiewiorski, P.; Rietema, K.
Fluidization IV ; Proceedings of the 4th International Conference on Fluidization, Kashikojima, Japan. New York: Engineering Foundation, 1983. p. 339-346.

Research output: Chapter in Book/Report/Conference proceeding › Conference contribution › Academic › peer-review

TY - GEN

T1 - Heat transfer on a vertical tube bundle immersed in a 0.70 m fluidized bed

AU - Piepers, H.W.

AU - Wiewiorski, P.

AU - Rietema, K.

PY - 1983

Y1 - 1983

N2 - The heat transfer was studied on a large vertical tube bundle (19 tubes) immersed in spent cracking catalyst fluidized bed. Heat transfer measurements were performed with only 1 tube, in which 10 elec. heating elements were mounted, at 3 different positions and at superficial gas velocity of 0.40 m/s. The heat transfer is not only detd. by the bubble activity but is strongly affected by the dense phase overall circulation induced by the rising bubbles which tend to move to the center of the bed

AB - The heat transfer was studied on a large vertical tube bundle (19 tubes) immersed in spent cracking catalyst fluidized bed. Heat transfer measurements were performed with only 1 tube, in which 10 elec. heating elements were mounted, at 3 different positions and at superficial gas velocity of 0.40 m/s. The heat transfer is not only detd. by the bubble activity but is strongly affected by the dense phase overall circulation induced by the rising bubbles which tend to move to the center of the bed

M3 - Conference contribution

SP - 339

EP - 346

BT - Fluidization IV ; Proceedings of the 4th International Conference on Fluidization, Kashikojima, Japan

PB - Engineering Foundation

CY - New York

ER -

Heat transfer on a vertical tube bundle immersed in a 0.70 m fluidized bed

Abstract

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