Volume 45, Issue 3 pp. 479-488
Research Article

Comparative Study of Two Identical Industrial Digesters Using Radiotracer-Based Residence Time Distribution Measurement

Meenakshi Sheoran

Meenakshi Sheoran

Thapar Institute of Engineering and Technology, Department of Chemical Engineering, 147004 Patiala, Punjab, India

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Avinash Chandra

Corresponding Author

Avinash Chandra

Thapar Institute of Engineering and Technology, Department of Chemical Engineering, 147004 Patiala, Punjab, India

Correspondence: Avinash Chandra ([email protected]), Department of Chemical Engineering, Thapar Institute of Engineering and Technology, Patiala, Punjab, 147004, India.Search for more papers by this author
Arvind Kumar Gautam

Arvind Kumar Gautam

National Institute of Technology Hamirpur, Department of Chemical Engineering, 177005 Himachal Pradesh, India

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Raj Kumar Arya

Raj Kumar Arya

Dr. B. R. Ambedkar National Institute of Technology, Department of Chemical Engineering, 144011 Jalandhar, Punjab, India

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Haripada Bhunia

Haripada Bhunia

Thapar Institute of Engineering and Technology, Department of Chemical Engineering, 147004 Patiala, Punjab, India

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Harish J. Pant

Harish J. Pant

Bhabha Atomic Research Centre, Isotope Production and Applications Division, 400085 Mumbai, India

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First published: 05 January 2022
Citations: 1

Abstract

Radiotracer-based residence time distribution (RTD) measurements were performed for two identical wheat straw pulping digesters to evaluate and compare their performances. The radiotracer technetium (99mTc) as sodium pertechnetate was used to follow the liquid phase inside the digester. The product quality of both digesters was not identical for similar sets of operating conditions. Temperature, pressure, and mass flow rates were the influencing parameters, and the experimental and theoretical mean residence time (MRT) were compared. A significant amount of flow abnormalities was observed in the second digester as compared to the first one, including channeling, dead volume, scaling, and bypassing. The axial dispersion model and tank in series with the back-mixing model were suitable for modeling the obtained RTD data.

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