Reduction of POME final discharge residual using activated bioadsorbent from oil palm kernel shell
A double insulated carbonisation-activation reactor was developed in order to produce activated carbon with high yield and surface area. This reactor was double insulated using low cement castable and covered around the internal space of the reactor with stainless steel plated and fibre glass jacket...
Main Authors: | , , , , , , , |
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Format: | Article |
Language: | English |
Published: |
Elsevier Ltd
2018
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Subjects: | |
Online Access: | View Fulltext in Publisher View Fulltext in Publisher View in Scopus |
LEADER | 03159nam a2200469Ia 4500 | ||
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001 | 10.1016-j.jclepro.2018.02.110 | ||
008 | 220120s2018 CNT 000 0 und d | ||
020 | |a 09596526 (ISSN) | ||
245 | 1 | 0 | |a Reduction of POME final discharge residual using activated bioadsorbent from oil palm kernel shell |
260 | 0 | |b Elsevier Ltd |c 2018 | |
490 | 1 | |t Journal of Cleaner Production | |
650 | 0 | 4 | |a Activated carbon |
650 | 0 | 4 | |a Bioadsorbent |
650 | 0 | 4 | |a Carbonisation |
650 | 0 | 4 | |a Carbonisation-activation |
650 | 0 | 4 | |a Carbonization |
650 | 0 | 4 | |a Chemical activation |
650 | 0 | 4 | |a Heat insulation layer |
650 | 0 | 4 | |a Heat transfer |
650 | 0 | 4 | |a Low-cement castables |
650 | 0 | 4 | |a Oil palm |
650 | 0 | 4 | |a Oil palm kernel shell |
650 | 0 | 4 | |a Palm oil |
650 | 0 | 4 | |a Retention time |
650 | 0 | 4 | |a Stainless steel |
650 | 0 | 4 | |a Steam |
650 | 0 | 4 | |a Steam activation |
650 | 0 | 4 | |a Steam flow rate |
650 | 0 | 4 | |a Steel fibers |
856 | |z View Fulltext in Publisher |u https://doi.org/10.1016/j.jclepro.2018.02.110 | ||
856 | |z View Fulltext in Publisher |u https://doi.org/Envi-Ronment Quality (Prescribed Premises) (Crude Palm Oil)(Amendment) Regulations 1982 (1982), http://www.doe.gov.my/portalv1/wp-content/plugins/download-attachments/include, (accessed 5.22.2017); Nor Faizah, J., Astimar, A., Noorshamsiana, A., Hassan, W., Nahrul Hayawin, Z., Application of palm kernel shell activated carbon for the removal of pollutant and color in palm oil mill effluent treatment (2016) J. Earth Environ. Heal. Sci., 2, pp. 15-20. , https://doi.org/10.4103/2423-7752.181802; | ||
856 | |z View in Scopus |u https://www.scopus.com/inward/record.uri?eid=2-s2.0-85043593770&doi=10.1016%2fj.jclepro.2018.02.110&partnerID=40&md5=f8cbeacc2d16656dd9bed3ea69b588d6 | ||
520 | 3 | |a A double insulated carbonisation-activation reactor was developed in order to produce activated carbon with high yield and surface area. This reactor was double insulated using low cement castable and covered around the internal space of the reactor with stainless steel plated and fibre glass jacketed heat insulation layer, which allow efficient heat transfer into the bed of material in the reactor. The carbonisation of oil palm kernel shell (OPKS) at 400 °C, followed by steam activation at 500–1000 °C continuously in the same reactor, with steam flow rate of 12.80–18.17 L/min had improved the activated carbon surface area from 305 ± 10.2 m2/g to 935 ± 36.7 m2/g and gave a high yield of 30% within 7 h retention time with a low gaseous emission. The activated carbon produced was successfully applied as bioadsorbent for the treatment of POME final discharge with the reduction of TSS, COD, colour and BOD up to 90%, 68%, 97% and 83%, respectively which met the standard set by Department of Environment Malaysia (DOE). © 2018 Elsevier Ltd | |
700 | 1 | 0 | |a Abd-Aziz, S. |e author |
700 | 1 | 0 | |a Aziz, A.A. |e author |
700 | 1 | 0 | |a Hassan, M.A. |e author |
700 | 1 | 0 | |a Ibrahim, M.F. |e author |
700 | 1 | 0 | |a Idris, J. |e author |
700 | 1 | 0 | |a Jalani, N.F. |e author |
700 | 1 | 0 | |a Mamat, R. |e author |
700 | 1 | 0 | |a Zainal, N.H. |e author |
773 | |t Journal of Cleaner Production |