Biosorption of Malachite Green from Aqueous Phase by Tamarind Fruit Shells Using FBR

Author:

Murugesan Senthil Rajan1ORCID,Sivakumar Vivek2,Velusamy Sampathkumar3ORCID,Ravindiran Gokulan4ORCID,Sundararaj Premkumar5,Maruthasalam Veerapathran1ORCID,Thangavel Ravindaran6ORCID,Ramasamy Gowri Shankar6,Panneerselvam Mukesh7,Periyasamy Selvakumar8ORCID

Affiliation:

1. Department of Civil Engineering, Dr. N. G. P. Institute of Technology, Coimbatore 641035, Tamil Nadu, India

2. Department of Civil, Hindusthan College of Engineering & Technology, Coimbatore 641032, Tamil Nadu, India

3. Department of Civil Engineering, Kongu Engineering College, Perundurai-638060, Tamil Nadu, India

4. Department of Civil Engineering, GMR Institute of Technology, Rajam, Andhra Pradesh-532127, India

5. Department of Civil Engineering, University College of Engineering, Dindigul-624622, Tamil Nadu, India

6. Department of Civil Engineering, PA College of Engineering &Technology, Coimbatore-642002, Tamil Nadu, India

7. Department of Civil Engineering, M. Kumarasamy College of Engineering, Karur-639113, Tamil Nadu, India

8. Department of Chemical Engineering, School of Mechanical, Chemical and Materials Engineering, Adama Science and Technology University, Adama-1888, Ethiopia

Abstract

The aim of this research is to remove malachite green (MG) from a created water environment utilising tamarind fruit shell (TFS) and a fixed-bed reactor (FBR) technology at room temperature. Biosorption is the finest method for dye removal among the several approaches available. It produces excellent results and may be used to remove a wide range of colouring components. It is used to weigh different options for firm things. The option which balances other ones on various counts is the finest one. Various studies have found that eating malachite green-contaminated fish poses a major health risk to people. From the FBR studies, the effect of various factors such as flow rate, initial sorbate concentration, biosorbent size, and bed depth on breakthrough of MG is assessed. The study was carried out to fix the flow rates. This is done by varying the biosorbent size with constant bed depth of 30 cm. The trend in flow rate variation appears to be similar for 0.33 and 0.6 mm sizes, whereas for 0.13 mm size, it is slightly different. The head loss and swelling of TFS particles are insignificant, during the fixed-bed studies. It is estimated that 30.9 T of crude TFS is required to get 8300 kg of 0.6 mm size of TFS. The service time obtained from design was more than the experimental breakthrough time, and calculated bed efficiency was >90%. The biosorption of MG by TFS can be well explained by the BDST approach. Acid regenerants such as 0.5 N H2SO4 and 0.5 N HCl can satisfactorily regenerate the spent TFS in the FBR system, with 0.5 N HCl being a better one.

Publisher

Hindawi Limited

Subject

General Engineering,General Materials Science

Reference30 articles.

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