182
Views
4
CrossRef citations to date
0
Altmetric
Original Articles

Adsorption of ammonium from wastewater treatment plant effluents onto the zeolite; A plug-flow column, optimisation, dynamic and isotherms studies

, , ORCID Icon, , , & show all
Pages 8445-8466 | Received 17 Sep 2020, Accepted 27 Oct 2020, Published online: 01 Dec 2020
 

ABSTRACT

The current work aimed to investigate the removal mechanism of NH4+ from wastewater treatment plant effluent (WWTPE) onto the zeolite in the plug-flow column reactor (PFCR). The adsorption process was optimised as a function of length (2–15), time (0.5–202 min), and accumulation (0.05–2.4 mg/g) using response surface methodology (RSM). The optimal operating parameters for the adsorption were recorded after 134.89 min with 1.52 mg/L of zeolite with 6.685 cm of the column length where the predicted and actual removal was 99.79 vs. 98.00% of NH4+ from WWTPE. The bed depth service time (BDST), Thomas, and Yoon-Nelson models were used to explain the adsorption behaviour. In contrast, the mass transfer factor (MTF) model was carried out to determine the internal and external removal mechanism. The findings revealed that PFCR exhibited an efficiency for removing NH4+ from WWTPE. The dynamic adsorption behaviour was satisfactorily described by the BDST, Thomas, and Yoon-Nelson models. These findings confirmed that the empirical models had verified the suitable of PFCR for removing NH4+ from WWTPE.

Symbols used

Acknowledgements

The authors acknowledge Ph.D thesis of Mohd Hairul Khamidun(Development and application of mass transfer model for adsorption of ammonium and phosphate from wastewater) at Faculty of Engineering, Universiti Teknologi Malaysia (UTM), which the manuscript is derived from the thesis. The authors also acknowledge the ,4,5,6,7) and ,2,3,4,7) and confirm that they used no third-party material in the manuscript. The research was funded by the technical & financial support from Academic Visitor Grant: Vot. 4D058, provided by Universiti Teknologi Malaysia.

Disclosure statement

The authors declare no conflicts of interest.

Supplementary material

Supplemental data for this article can be accessed here.

Reprints and Corporate Permissions

Please note: Selecting permissions does not provide access to the full text of the article, please see our help page How do I view content?

To request a reprint or corporate permissions for this article, please click on the relevant link below:

Academic Permissions

Please note: Selecting permissions does not provide access to the full text of the article, please see our help page How do I view content?

Obtain permissions instantly via Rightslink by clicking on the button below:

If you are unable to obtain permissions via Rightslink, please complete and submit this Permissions form. For more information, please visit our Permissions help page.