dc.contributor.author | Asimakopoulos, Georgios | |
dc.contributor.author | Baikousi, Maria | |
dc.contributor.author | Kostas, Vasilis | |
dc.contributor.author | Papantoniou, Marios | |
dc.contributor.author | Bourlinos, Athanasios B. | |
dc.contributor.author | Zbořil, Radek | |
dc.contributor.author | Karakassides, Michael A. | |
dc.contributor.author | Salmas, Constantinos E. | |
dc.date.accessioned | 2021-02-12T07:48:23Z | |
dc.date.available | 2021-02-12T07:48:23Z | |
dc.date.issued | 2020 | |
dc.identifier.citation | Applied Sciences. 2020, vol. 10, issue 24, art. no. 8812. | cs |
dc.identifier.issn | 2076-3417 | |
dc.identifier.uri | http://hdl.handle.net/10084/142820 | |
dc.description.abstract | Featured Application
This work deals with the development of an activated carbon adsorber via the exploitation of spent coffee waste. Economic and environmental benefits from such processes are extended. The application on hexavalent chromium removal was tested.
Hexavalent chromium (Cr(VI)) is a heavy metal that is highly soluble and exhibits toxic effects on biological systems. Nevertheless, it is used in many industrial applications. The adsorption process of Cr(VI), using activated carbon (AC), is under investigation globally. On the other hand, around six million tons of spent coffee is sent to landfill annually. In the spirit of cyclic economy, this research investigated the production of AC from spent coffee for the removal of Cr(VI) from wastewater. The AC was produced via pyrolysis process under a nitrogen atmosphere. Chemical activation using potassium hydroxide (KOH) occurred simultaneously with the pyrolysis process. The produced AC was tested as an absorber of Cr(VI). The best fitted kinetic model was the diffusion-chemisorption model. A 24-h adsorption experiment was carried out using a solution with a pH of 3 and an initial Cr(VI) concentration of 54.14 ppm. This resulted in an experimental maximum capacity of 109 mg/g, while the theoretical prediction was 137 mg/g. It also resulted in an initial adsorption rate (r(i)) of 110 (mg/(g h)). The Brunauer-Emmett-Teller surface area (S-gBET) was 1372 m(2)/g, the Langmuir surface area (S-gLang.) was 1875 m(2)/g, and the corrugated pore structure model surface area (S-gCPSM) was 1869 m(2)/g. The micropore volume was 84.6%, exhibiting micropores at D-micro1 = 1.28 and D-micro2 = 1.6 nm. The tortuosity factor (tau) was 4.65. | cs |
dc.language.iso | en | cs |
dc.publisher | MDPI | cs |
dc.relation.ispartofseries | Applied Sciences | cs |
dc.relation.uri | http://doi.org/10.3390/app10248812 | cs |
dc.rights | © 2020 by the authors. Licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution (CC BY) license. | cs |
dc.rights.uri | http://creativecommons.org/licenses/by/4.0/ | cs |
dc.subject | activated carbon | cs |
dc.subject | spent coffee | cs |
dc.subject | waste coffee | cs |
dc.subject | biowaste valorization | cs |
dc.subject | hexavalent chromium | cs |
dc.subject | chromium adsorption | cs |
dc.subject | chromium removal kinetics | cs |
dc.subject | biowaste activated carbon characterization | cs |
dc.title | Nanoporous activated carbon derived via pyrolysis process of spent coffee: Structural characterization. Investigation of its use for hexavalent chromium removal | cs |
dc.type | article | cs |
dc.identifier.doi | 10.3390/app10248812 | |
dc.rights.access | openAccess | cs |
dc.type.version | publishedVersion | cs |
dc.type.status | Peer-reviewed | cs |
dc.description.source | Web of Science | cs |
dc.description.volume | 10 | cs |
dc.description.issue | 24 | cs |
dc.description.firstpage | art. no. 8812 | cs |
dc.identifier.wos | 000602961100001 | |