Industrial Scale RTD Measurement Using Gold Radiotracer

被引:5
作者
Sheoran, Meenakshi [1 ]
Chandra, Avinash [2 ]
Bhunia, Haripada [2 ]
Bajpai, Pramod K. [2 ]
Pant, Harish J. [3 ]
机构
[1] Chandigarh Univ, Dept Chem Engn, Mohali 140413, Punjab, India
[2] Thapar Inst Engn & Technol, Dept Chem Engn, Patiala 147004, Punjab, India
[3] Bhabha Atom Res Ctr, Isotope Applicat Div, Mumbai 400085, Maharashtra, India
来源
IRANIAN JOURNAL OF CHEMISTRY & CHEMICAL ENGINEERING-INTERNATIONAL ENGLISH EDITION | 2021年 / 40卷 / 01期
关键词
Au-198; Axial dispersion model; Convolution; Pulp digester; Radiotracer; Tank in series with a back-mixing model; RESIDENCE TIME DISTRIBUTION; PHASE; MODEL;
D O I
10.30492/IJCCE.2020.39047
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Residence Time Distribution (RTD) is a suitable method to find out the hydrodynamics of any industrial or lab-scale reactor. Radiotracer Au-198 was used to trace the liquid phase of the industrial scale continuous three tube pulp digester. The radiotracer was injected instantaneously as an impulse input in the liquid phase and concentration versus time data were collected at the inlet and outlet of each tube using a data acquisition system. The flow modeling of continuous pulp digester has been done in two ways. Firstly, the whole digester was considered a single reactor. Secondly, each tube of the digester was considered a single reactor separately. For the second case, the convolution procedure was opted to deal with a non-ideal input signal for the second and third tubes. Axial dispersion model and tank in series with a back-mixing model were used to simulate the experimental data. Mean residence time and Peclet numbers were calculated for each tube and the whole digester.
引用
收藏
页码:313 / 321
页数:9
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