Removal of Remazol Brilliant Blue R From Aqueous Solution by Pirina Pretreated with Nitric Acid and Commercial Activated Carbon

2014 ◽  
Vol 225 (3) ◽  
Author(s):  
Sevgi Dağdelen ◽  
Bilal Acemioğlu ◽  
Evrim Baran ◽  
Oğuzhan Koçer
Keyword(s):  
Aqueous Solution ◽  
Activated Carbon ◽  
Nitric Acid ◽  
Brilliant Blue ◽  
Remazol Brilliant Blue R

Sorptive removal of Remazol Brilliant Blue R from aqueous solution by diethylenetriamine functionalized magnetic macro-reticular hybrid material

RSC Advances ◽  
2016 ◽  
Vol 6 (27) ◽  
pp. 22395-22410 ◽  
Author(s):  
K. Z. Elwakeel ◽  
A. A. El-Bindary ◽  
A. Ismail ◽  
A. M. Morshidy
Keyword(s):  
Aqueous Solution ◽  
Hybrid Material ◽  
Glycidyl Methacrylate ◽  
Synthetic Polymer ◽  
Brilliant Blue ◽  
Natural Materials ◽  
Remazol Brilliant Blue R ◽  
Sorptive Removal

Chitosan, glycidyl methacrylate (synthetic polymer) and magnetite are combined to produce novel magnetic macro-reticular hybrid synthetic–natural materials which are shown to be effective sorbents for RBBR ions.

Study on Treatment of Cr (VI)-Containing Wastewater with Nitric Acid Modified Activated Carbon

2011 ◽  
Vol 413 ◽  
pp. 38-41
Author(s):  
Xiu Ling Song ◽  
Hui Qian
Keyword(s):  
Aqueous Solution ◽  
Activated Carbon ◽  
Nitric Acid ◽  
Ph Value ◽  
Removal Rate ◽  
Freundlich Isotherm ◽  
Exchange Capacity ◽  
Modified Activated Carbon ◽  
Exchange Adsorption ◽  
Adsorption Curve

After activated carbon is oxidized and modified with nitric acid (1:1), its cation exchange capacity can amount to 1.840 mmol • g-1. The modified activated carbon is used as adsorbent for the treatment of Cr (Ⅵ)-containing wastewater at room temperature, and its removal mechanism is discussed in this paper. It is shown that: when the pH value of the aqueous solution being 2.5-3.0;the adsorption time being 3.0h, the removal rate of Cr (Ⅵ) in the aqueous solution can reach 97% and its adsorption capacity can amount to 45.66 mg • g-1. From the results, it can be also seen that the adsorption curve to chromium in wastewater by the modified activated carbon better meets the Freundlich isotherm, and ion exchange adsorption mainly does its work.

Statistical optimization of Remazol Brilliant Blue R dye adsorption onto activated carbon prepared from pomegranate fruit peel

2020 ◽  
Vol 28 ◽  
pp. 100426 ◽  
Author(s):  
Mohd Azmier Ahmad ◽  
Muhammad Aswar Eusoff ◽  
Peter Olusakin Oladoye ◽  
Kayode Adesina Adegoke ◽  
Olugbenga Solomon Bello
Keyword(s):  
Activated Carbon ◽  
Dye Adsorption ◽  
Statistical Optimization ◽  
Brilliant Blue ◽  
Fruit Peel ◽  
Remazol Brilliant Blue R ◽  
Pomegranate Fruit

Adsorption kinetics of Remazol Brilliant Blue R dye from liquid effluents by bovine bone charcoal

2020 ◽  
Vol 1 (1) ◽  
pp. 11717
Author(s):  
Lívia Katia Dos Santos Lima ◽  
Antônio Vilas Boas Quintiliano Júnior ◽  
André Henrique Zeferino ◽  
Ana Paula Duarte
Keyword(s):  
Activated Carbon ◽  
Adsorption Kinetics ◽  
Intraparticle Diffusion ◽  
Brilliant Blue ◽  
Bovine Bone ◽  
First Order ◽  
Remazol Brilliant Blue R ◽  
Pseudo Second Order ◽  
Pseudo First Order ◽  
Kinetics Of

The textile industry stands out for generating effluents with high levels of dyes, which have a high polluting potential. Among these dyes, the Remazol Brilliant Blue R azo dye, is one of the most used for dyeing wool and cotton, being released in excess on these effluents. Intended for the carcinogenic and mutagenic potential of this type of dyes, several researches are developed in search of economical technologies for their removal. An adsorption is a viable technique, since several materials can be used for this purpose. Bovine bone activated carbon, as it is a residue from the livestock industry that is easily obtained, has been studied as an adsorbent material in the removal of dyes. Therefore, the objective of this project was to evaluate the performance of the adsorption kinetics of the Remazol Brilliant Blue R dye from the effluents using bovine bone activated carbon. The experiments were carried out in batches, with solutions concentrations of 20, 50 and 100 ppm, and the mathematical models of pseudo-first order, pseudo-second order and intraparticle diffusion were adjusted to the experimental data. For concentrations of 20 and 50 ppm, the model that best fits was the pseudo-first order, while for the concentration of 100 ppm the pseudo-second order model obtained the best result with R2 of 0.992. The intraparticle diffusion model showed that the higher the concentration of the dye in solution, the greater the thickness of the boundary layer and that the intraparticle diffusion does not control the adsorption process in any of the study criteria.

Removal of Cr(VI) from aqueous solution using activated carbon modified with nitric acid

2009 ◽  
Vol 152 (2-3) ◽  
pp. 434-439 ◽  
Author(s):  
Guolin Huang ◽  
Jeffrey X. Shi ◽  
Tim A.G. Langrish
Keyword(s):  
Aqueous Solution ◽  
Activated Carbon ◽  
Nitric Acid
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