Cycle Time Minimization During Renewable Methane Production from H2O2 Enhanced Anaerobic Co-Digestion of Petrochemical Wastewater in Continuous Stirred Tank Reactor

Cycle Time Minimization During Renewable Methane Production from H2O2 Enhanced Anaerobic Co-Digestion of Petrochemical Wastewater in Continuous Stirred Tank Reactor

The latent of per-oxidation pretreatment to petrochemical wastewater prior to anaerobic co-digestion process was explored in continuous stirred tank reactor continually with dairy cattle and beef cattle manure. Hydrogen peroxide oxidation, elevated biodegradability index(BOD/COD) up to 35 %. While c...

Full description

Bibliographic Details
Main Authors: Siddique, Md. Nurul Islam, Zularisam, A. W.
Format: Article
Language:English
Published: Asian J. Chem. 2013
Subjects:
TA Engineering (General). Civil engineering (General)
Online Access:http://umpir.ump.edu.my/id/eprint/9398/
http://umpir.ump.edu.my/id/eprint/9398/
http://umpir.ump.edu.my/id/eprint/9398/1/Cycle%20Time%20Minimization%20During%20Renewable%20Methane%20Production%20from%20H2O2%20Enhanced%20Anaerobic%20Co-Digestion%20of%20Petrochemical%20Wastewater%20in%20Continuous%20Stirred%20Tank%20Reactor.pdf
id ump-9398
recordtype eprints
spelling ump-93982018-01-17T03:41:23Z http://umpir.ump.edu.my/id/eprint/9398/ Cycle Time Minimization During Renewable Methane Production from H2O2 Enhanced Anaerobic Co-Digestion of Petrochemical Wastewater in Continuous Stirred Tank Reactor Siddique, Md. Nurul Islam Zularisam, A. W. TA Engineering (General). Civil engineering (General) The latent of per-oxidation pretreatment to petrochemical wastewater prior to anaerobic co-digestion process was explored in continuous stirred tank reactor continually with dairy cattle and beef cattle manure. Hydrogen peroxide oxidation, elevated biodegradability index(BOD/COD) up to 35 %. While continuous stirred tank reactor operated with non-oxidation by hydrogen peroxide petrochemical waste water system was failed at organic loading of 6.5-12.99 kg COD/m3/d due to vigorous volatile fatty acid accumulation. Inversely, oxidation by hydrogen peroxide petrochemical waste water rendered sustainable superior total COD removal at 6.03-11.7 kg COD/m3/d organic loading with durable process stability at co-digestion period. As methane production is considered to be inhibited due to volatile fatty acid accumulation leading to instability of reactor operation during anaerobic digestion, co-digestion of oxidation by hydrogen peroxide pretreated petrochemical waste water resulted in exaggerated methane yield, followed by 98 ± 0.5 %, 95 ± 0.05 % and79 ± 0.06 % COD reduction at 9, 6 and 4 days hydraulic retention time. The concrete data revealed that prolonged hydraulic retention time and abridged cycle time caused continuous stirred tank reactor aggrandized total COD removal efficiency and methane yield. Asian J. Chem. 2013 Article PeerReviewed application/pdf en http://umpir.ump.edu.my/id/eprint/9398/1/Cycle%20Time%20Minimization%20During%20Renewable%20Methane%20Production%20from%20H2O2%20Enhanced%20Anaerobic%20Co-Digestion%20of%20Petrochemical%20Wastewater%20in%20Continuous%20Stirred%20Tank%20Reactor.pdf Siddique, Md. Nurul Islam and Zularisam, A. W. (2013) Cycle Time Minimization During Renewable Methane Production from H2O2 Enhanced Anaerobic Co-Digestion of Petrochemical Wastewater in Continuous Stirred Tank Reactor. Asian Journal of Chemistry, 25 (2). pp. 1140-1148. ISSN 0970-7077 http://dx.doi.org/10.14233/ajchem.2013.13867
repository_type Digital Repository
institution_category Local University
institution Universiti Malaysia Pahang
building UMP Institutional Repository
collection Online Access
language English
topic TA Engineering (General). Civil engineering (General)
spellingShingle TA Engineering (General). Civil engineering (General)
Siddique, Md. Nurul Islam
Zularisam, A. W.
Cycle Time Minimization During Renewable Methane Production from H2O2 Enhanced Anaerobic Co-Digestion of Petrochemical Wastewater in Continuous Stirred Tank Reactor
description The latent of per-oxidation pretreatment to petrochemical wastewater prior to anaerobic co-digestion process was explored in continuous stirred tank reactor continually with dairy cattle and beef cattle manure. Hydrogen peroxide oxidation, elevated biodegradability index(BOD/COD) up to 35 %. While continuous stirred tank reactor operated with non-oxidation by hydrogen peroxide petrochemical waste water system was failed at organic loading of 6.5-12.99 kg COD/m3/d due to vigorous volatile fatty acid accumulation. Inversely, oxidation by hydrogen peroxide petrochemical waste water rendered sustainable superior total COD removal at 6.03-11.7 kg COD/m3/d organic loading with durable process stability at co-digestion period. As methane production is considered to be inhibited due to volatile fatty acid accumulation leading to instability of reactor operation during anaerobic digestion, co-digestion of oxidation by hydrogen peroxide pretreated petrochemical waste water resulted in exaggerated methane yield, followed by 98 ± 0.5 %, 95 ± 0.05 % and79 ± 0.06 % COD reduction at 9, 6 and 4 days hydraulic retention time. The concrete data revealed that prolonged hydraulic retention time and abridged cycle time caused continuous stirred tank reactor aggrandized total COD removal efficiency and methane yield.
format Article
author Siddique, Md. Nurul Islam
Zularisam, A. W.
author_facet Siddique, Md. Nurul Islam
Zularisam, A. W.
author_sort Siddique, Md. Nurul Islam
title Cycle Time Minimization During Renewable Methane Production from H2O2 Enhanced Anaerobic Co-Digestion of Petrochemical Wastewater in Continuous Stirred Tank Reactor
title_short Cycle Time Minimization During Renewable Methane Production from H2O2 Enhanced Anaerobic Co-Digestion of Petrochemical Wastewater in Continuous Stirred Tank Reactor
title_full Cycle Time Minimization During Renewable Methane Production from H2O2 Enhanced Anaerobic Co-Digestion of Petrochemical Wastewater in Continuous Stirred Tank Reactor
title_fullStr Cycle Time Minimization During Renewable Methane Production from H2O2 Enhanced Anaerobic Co-Digestion of Petrochemical Wastewater in Continuous Stirred Tank Reactor
title_full_unstemmed Cycle Time Minimization During Renewable Methane Production from H2O2 Enhanced Anaerobic Co-Digestion of Petrochemical Wastewater in Continuous Stirred Tank Reactor
title_sort cycle time minimization during renewable methane production from h2o2 enhanced anaerobic co-digestion of petrochemical wastewater in continuous stirred tank reactor
publisher Asian J. Chem.
publishDate 2013
url http://umpir.ump.edu.my/id/eprint/9398/
http://umpir.ump.edu.my/id/eprint/9398/
http://umpir.ump.edu.my/id/eprint/9398/1/Cycle%20Time%20Minimization%20During%20Renewable%20Methane%20Production%20from%20H2O2%20Enhanced%20Anaerobic%20Co-Digestion%20of%20Petrochemical%20Wastewater%20in%20Continuous%20Stirred%20Tank%20Reactor.pdf
first_indexed 2023-09-18T22:07:56Z
last_indexed 2023-09-18T22:07:56Z
_version_ 1777414833598103552

Similar Items