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Heat Transfer Studies in Ejector-induced Downflow Bubble Column

  • Rohit B. Meshram EMAIL logo , Gautam Kundu and Dibyendu Mukherjee
Published/Copyright: April 23, 2016

Abstract

Temperature control in bubble columns is of great importance, since chemical reactions in many of the chemical, pharmaceutical, fertilizer, etc. industries are usually accompanied by heat supply or heat removal operations. In the present research work, the heat transfer coefficient of a two-phase co-current vertical downflow bubble column (i.d. 0.05 m×1.6 m height) was evaluated. Experimental studies were carried out to calculate the heat transfer coefficient for operating temperature ranges from 60 °C to 90 °C. The effects of the superficial gas velocity (4.25×10–3 to 9.58×10–3 m/s), liquid velocity (8.50×10–2 to 16.98×10–2 m/s), gas holdup, and axial position were investigated. Empirical correlation was developed, based on a multiple regression analysis to calculate a heat transfer coefficient as a function of dimensionless numbers, including the Reynolds number, the Prandtl number, and the Froude number.

Funding statement: This research work was supported by the Chemical Engineering Department, Indian Institute of Technology, Kharagpur, India.

Nomenclature

Cpl

Specific heat of liquid (J/kg °C)

dc

Diameter of column (m)

Fr

Froude number Ug2gdc (-)

g

Acceleration due to gravity (m/s2)

h

Heat transfer coefficient (W/ m2  °C)

kl

Thermal conductivity of liquid (W/m  °C)

k1 to k5

Indices in eq. (2)

L

Length of contactor (m)

Pr

Prandtl number Cplμlkl (-)

Re

Reynolds number dcUgρlμl(-)

St

Stanton number hρlCplUg (-)

Ug

Superficial gas velocity (m/s)

Ul

Superficial liquid velocity (m/s)

Greek Letters
εg

Gas holdup (-)

μl

Viscosity of liquid (kg/m sec)

ρl

Density of liquid (kg/m3)

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Published Online: 2016-4-23
Published in Print: 2016-10-1

©2016 by De Gruyter

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