Adsorption performance of packed bed column for benzylformic acid removal using CaO2 nanoparticles

2019 ◽  
Vol 23 ◽  
pp. 100267 ◽  
Author(s):  
Sapana S. Madan ◽  
Biswajit S. De ◽  
Kailas L. Wasewar
Keyword(s):  
Packed Bed ◽  
Packed Bed Column ◽  
Adsorption Performance

Adsorption performance of packed bed column for the removal of perchlorate using modified activated carbon

2018 ◽  
Vol 117 ◽  
pp. 350-362 ◽  
Author(s):  
Radhika R. ◽  
Jayalatha T. ◽  
Rekha Krishnan G. ◽  
Salu Jacob ◽  
Rajeev R. ◽  
...  
Keyword(s):  
Activated Carbon ◽  
Packed Bed ◽  
Modified Activated Carbon ◽  
Packed Bed Column ◽  
Adsorption Performance

Preparative Separation of Xanthophylls from Corn Gluten Meal by Macoroporous Adsorption Resins in Biochemical Engineering

2012 ◽  
Vol 577 ◽  
pp. 105-108
Author(s):  
Mei Huang ◽  
Ling Zhi Jiang ◽  
Yan Fei Wei
Keyword(s):  
Sorption Isotherms ◽  
Packed Bed ◽  
Separation Process ◽  
Corn Gluten Meal ◽  
Biochemical Engineering ◽  
Packed Bed Column ◽  
Recovery Yield ◽  
Adsorption Performance ◽  
Freundlich Equation ◽  
Corn Gluten

To purify xanthophylls from corn gluten meal by macoroporous resins, the static adsorption performance and dynamic separation characteristics of different resins have been evaluated. And SD300 resin offers the best adsorption capacity for xanthophylls than the other resins as HZ816, S8, AB8 and D630. Based on sorption isotherms of SD300, the Freundlich equation was found to fit the experimental data more adequately. Then packed bed column with SD300 resin was used to perform dynamic adsorption and desorption tests to optimize the separation process of xanthophylls. Parameters for adsorption were sample solution xanthophylls concentration 128.9μg/ml, processing volume 11 BV, flow rate 1.0 BV/h, temperature 25°C. After being treated with ethyl acetate, the xanthophylls content in the product was increased to 6.1%, with a recovery yield of 74.0%.

Theoretical analysis of counter-current absorption of a poorly soluble gas based on the PDE-AD model

1986 ◽  
Vol 51 (6) ◽  
pp. 1222-1239 ◽  
Author(s):  
Pavel Moravec ◽  
Vladimír Staněk
Keyword(s):  
Experimental Data ◽  
Liquid Phase ◽  
Gas Phase ◽  
Transfer Functions ◽  
Packed Bed ◽  
Packed Bed Column ◽  
Interfacial Transport ◽  
Gaseous Component ◽  
Poorly Soluble ◽  
Counter Current

Expression have been derived in the paper for all four possible transfer functions between the inlet and the outlet gas and liquid steams under the counter-current absorption of a poorly soluble gas in a packed bed column. The transfer functions have been derived for the axially dispersed model with stagnant zone in the liquid phase and the axially dispersed model for the gas phase with interfacial transport of a gaseous component (PDE - AD). calculations with practical values of parameters suggest that only two of these transfer functions are applicable for experimental data evaluation.

Analysis of observability of model parameters for physical absorption of poorly soluble gases in packed beds

1982 ◽  
Vol 47 (10) ◽  
pp. 2639-2653 ◽  
Author(s):  
Pavel Moravec ◽  
Vladimír Staněk
Keyword(s):  
Transfer Functions ◽  
Plug Flow ◽  
Packed Bed ◽  
Model Parameters ◽  
Packed Bed Column ◽  
Interfacial Transport ◽  
Complex Arithmetic ◽  
Physical Absorption ◽  
Poorly Soluble ◽  
Phase Lags

Expressions have been derived for four possible transfer functions of a model of physical absorption of a poorly soluble gas in a packed bed column. The model has been based on axially dispersed flow of gas, plug flow of liquid through stagnant and dynamic regions and interfacial transport of the absorbed component. The obtained transfer functions have been transformed into the frequency domain and their amplitude ratios and phase lags have been evaluated using the complex arithmetic feature of the EC-1033 computer. Two of the derived transfer functions have been found directly applicable for processing of experimental data. Of the remaining two one is useable with the limitations to absorption on a shallow layer of packing, the other is entirely worthless for the case of poorly soluble gases.

An experimental dynamic method of investigation of counter-current absorption of oxygen in water in a packed bed column

1987 ◽  
Vol 52 (7) ◽  
pp. 1715-1729 ◽  
Author(s):  
Pavel Moravec ◽  
Vladimír Staněk
Keyword(s):  
Transfer Functions ◽  
Simultaneous Detection ◽  
Harmonic Component ◽  
Packed Bed ◽  
Packed Bed Column ◽  
Oxygen Electrodes ◽  
Simultaneous Evaluation ◽  
Physical Absorption ◽  
On Line ◽  
Counter Current

An experimental method and technique are described in the paper of simultaneous detection of the transfer functions outlet-gas-stream-to-inlet-gas-stream and outlet-liquid-stream-to-inlet-gas-stream for the absorption of oxygen into water in a counter-current packed bed column. Both transfer functions were simultaneously monitored by means of three oxygen electrodes operating on the polarographic principle. The signals of these electrodes were processed in three steps to yield parameters of the model of physical absorption of gas. The first step was on-line evaluation of the Fourier coefficients of the principal harmonic component in all three monitored streams. The second step was the calculation of the frequency characteristics of both transfer functions while the third step yielded parameters of the model by optimization in the frequency domain. The method permits simultaneous evaluation of the parameters of the flow of both phases in the column and the interfacial transfer of oxygen.

Column Study for Adsorption of Methylene Blue Dye using Azadirachta indica Adsorbent

2020 ◽  
Vol 17 (4) ◽  
pp. 47-52
Author(s):  
Vibha Goswami ◽  
Renu Upadhyaya ◽  
Sumanta Kumar Meher
Keyword(s):  
Methylene Blue ◽  
Flow Rate ◽  
Azadirachta Indica ◽  
Packed Bed ◽  
Blue Dye ◽  
Feed Flow Rate ◽  
Methylene Blue Dye ◽  
Packed Bed Column ◽  
Bed Height ◽  
Percentage Removal

In this study, synthesised Azadirachta indica adsorbent was used for the removal of methylene blue dye using a packed bed column. The effect of feed flow rate, feed methylene blue dye concentration, and bed height of column on percentage removal of dye was studied. It was observed that the column bed exhausted rapidly at a higher flow rate and therefore, a breakthrough occurred faster. However, it was observed that bed exhaustion time increases on increasing the bed height from 2 to 10 inch at 10 mg/L feed dye concentration and feed flow rate of 40 ml/min. It was also found that the breakthrough curve is more dispersed and the percentage removal of dye increases on decreasing the feed methylene dye concentration from 150 to 10 mg/L. The percentage removal was found to be 96.89% at 20 ml/min of feed flow rate under 10 inch of bed height and 10 mg/L of feed dye concentration. The atomic absorption spectrophotometer and scanning electron microscope were used for estimating the effluent dye concentration from the column and morphological study, respectively.

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