✦ LIBER ✦

Heat transfer in a continuous bubble column

✍ Scribed by B. H. Chen

Book ID: 112056547
Publisher: John Wiley and Sons
Year: 1989
Tongue: English
Weight: 337 KB
Volume: 67
Category: Article
ISSN: 0008-4034
DOI: 10.1002/cjce.5450670422

No coin nor oath required. For personal study only.

📜 SIMILAR VOLUMES

Heat transfer mechanism in bubble column

Heat transfer mechanism in bubble columns

✍ A.K. Verma 📂 Article 📅 1989 🏛 Elsevier Science ⚖ 259 KB

Heat transfer from a tube bundle in a bu

Heat transfer from a tube bundle in a bubble column

✍ S.C. Saxena; R. Vadivel 📂 Article 📅 1988 🏛 Elsevier Science 🌐 English ⚖ 399 KB

Mass transfer in continuous bubble colum

Mass transfer in continuous bubble columns with floating bubble breakers

✍ Y. Kang; B. T. Min; J. B. Nah; S. D. Kim 📂 Article 📅 1990 🏛 American Institute of Chemical Engineers 🌐 English ⚖ 355 KB 👁 2 views

Bubble column reactors are widely used in the fields of petrochemical, biochemical, and chemical engineering processes. They are comparable to other multiphase reactors because of their simplicity, low operating costs, and higher heat and mass transfer coefficients between phases. Since a continuous

Survey of heat transfer mechanisms in a

Survey of heat transfer mechanisms in a slurry bubble column

✍ Hanning Li; Anand Prakash 📂 Article 📅 2001 🏛 John Wiley and Sons 🌐 English ⚖ 838 KB

Heat transfer study in a pilot-plant sca

Heat transfer study in a pilot-plant scale bubble column

✍ Rahman S. Abdulmohsin; Balasim A. Abid; Muthanna H. Al-Dahhan 📂 Article 📅 2011 🏛 Institution of Chemical Engineers 🌐 English ⚖ 528 KB

Heat transfer from a cylindrical probe i

Heat transfer from a cylindrical probe in a slurry bubble column

✍ S.C. Saxena; A.K. Verma; R. Vadivel; A.C. Saxena 📂 Article 📅 1989 🏛 Elsevier Science 🌐 English ⚖ 463 KB

Heat transfer coefficient between an electrically heated 19 0 mm diameter vertical probe and slurries of glass beads of different sizes (50.0, 117.6 and 143.3 I~m) and concentrations (108-312 kg/m 3) is determined in a 10.8 cm diameter bubble column as a function of superficial air velocity (0.103-0