Conventional steam activation for conversion of oil palm kernel shell biomass into activated carbon via biochar product

Conventional steam activation pyrolysis of waste materials such as oil palm kernel shell for production of biochar was investigated using central composite design. Conventional steam activation was carried out via an initial carbonization of oil palm kernel shell to obtain biochar and thereafter ste...

Full description

Bibliographic Details
Main Author: A.C. Affam
Format: Article
Language:English
Published: GJESM Publisher 2020-01-01
Series:Global Journal of Environmental Science and Management
Subjects:
Online Access:https://www.gjesm.net/article_36539_57828dd0481f03ba4e25400f4ec0a2b3.pdf
id doaj-37762c755c5642d19968d9ac9729d5c9
record_format Article
spelling doaj-37762c755c5642d19968d9ac9729d5c92021-02-02T00:03:55ZengGJESM PublisherGlobal Journal of Environmental Science and Management2383-35722383-38662020-01-0161153010.22034/GJESM.2020.01.0236539Conventional steam activation for conversion of oil palm kernel shell biomass into activated carbon via biochar productA.C. Affam0Department for Management of Science and Technology Development, Ton Duc Thang University, Ho Chi Minh City, Vietnam|Faculty of Environment and Labour Safety, Ton Duc Thang University, Ho Chi Minh City, VietnamConventional steam activation pyrolysis of waste materials such as oil palm kernel shell for production of biochar was investigated using central composite design. Conventional steam activation was carried out via an initial carbonization of oil palm kernel shell to obtain biochar and thereafter steam activation of the biochar using the conventional heating to produce activated carbon. Additionally, removal of chemical oxygen demand and colour was studied alongside the production. Optimum yield was obtained at about 90 min and 725<sup>o</sup>C. Out of the time duration, 80 min was for carbonation and 10 min was for steam activation. Further extension of time was not significant whereas increasing temperature was able to increase the pores found on the biochar. Under the optimum condition, fixed carbon was 19.39%, chemical oxygen demand and colour removal were 32.02 and 61.15%, respectively at 90 min adsorption time. However, when time was extended to 120 min, chemical oxygen demand (48.2%) and colour (94.19%) removal were achieved. The Brunauer–Emmett–Teller surface area and micropore area of the oil palm kernel shell based activated carbon was 620.45 m<sup>2</sup>/g and 550.4 m<sup>2</sup>/g, respectively. The conventional steam activation is an effective method that can be employed in production of activated carbon from waste oil palm kernel shell.https://www.gjesm.net/article_36539_57828dd0481f03ba4e25400f4ec0a2b3.pdfcentral composite designconventional heatingoil palm kernel shellresponse surface methodologysteam activation
collection DOAJ
language English
format Article
sources DOAJ
author A.C. Affam
spellingShingle A.C. Affam
Conventional steam activation for conversion of oil palm kernel shell biomass into activated carbon via biochar product
Global Journal of Environmental Science and Management
central composite design
conventional heating
oil palm kernel shell
response surface methodology
steam activation
author_facet A.C. Affam
author_sort A.C. Affam
title Conventional steam activation for conversion of oil palm kernel shell biomass into activated carbon via biochar product
title_short Conventional steam activation for conversion of oil palm kernel shell biomass into activated carbon via biochar product
title_full Conventional steam activation for conversion of oil palm kernel shell biomass into activated carbon via biochar product
title_fullStr Conventional steam activation for conversion of oil palm kernel shell biomass into activated carbon via biochar product
title_full_unstemmed Conventional steam activation for conversion of oil palm kernel shell biomass into activated carbon via biochar product
title_sort conventional steam activation for conversion of oil palm kernel shell biomass into activated carbon via biochar product
publisher GJESM Publisher
series Global Journal of Environmental Science and Management
issn 2383-3572
2383-3866
publishDate 2020-01-01
description Conventional steam activation pyrolysis of waste materials such as oil palm kernel shell for production of biochar was investigated using central composite design. Conventional steam activation was carried out via an initial carbonization of oil palm kernel shell to obtain biochar and thereafter steam activation of the biochar using the conventional heating to produce activated carbon. Additionally, removal of chemical oxygen demand and colour was studied alongside the production. Optimum yield was obtained at about 90 min and 725<sup>o</sup>C. Out of the time duration, 80 min was for carbonation and 10 min was for steam activation. Further extension of time was not significant whereas increasing temperature was able to increase the pores found on the biochar. Under the optimum condition, fixed carbon was 19.39%, chemical oxygen demand and colour removal were 32.02 and 61.15%, respectively at 90 min adsorption time. However, when time was extended to 120 min, chemical oxygen demand (48.2%) and colour (94.19%) removal were achieved. The Brunauer–Emmett–Teller surface area and micropore area of the oil palm kernel shell based activated carbon was 620.45 m<sup>2</sup>/g and 550.4 m<sup>2</sup>/g, respectively. The conventional steam activation is an effective method that can be employed in production of activated carbon from waste oil palm kernel shell.
topic central composite design
conventional heating
oil palm kernel shell
response surface methodology
steam activation
url https://www.gjesm.net/article_36539_57828dd0481f03ba4e25400f4ec0a2b3.pdf
work_keys_str_mv AT acaffam conventionalsteamactivationforconversionofoilpalmkernelshellbiomassintoactivatedcarbonviabiocharproduct
_version_ 1724314689575321600