Zobrazeno 1 - 10
of 25
pro vyhledávání: '"Saravanan R. Shanmugam"'
Autor:
Chungman Moon, Rajesh Singh, Sathyanarayan S. Veeravalli, Saravanan R. Shanmugam, Subba Rao Chaganti, Jerald A. Lalman, Daniel D. Heath
Publikováno v:
Water, Vol 7, Iss 5, Pp 2275-2292 (2015)
Biological sulfate (SO42−) reduction was examined in anaerobic sequential batch reactors (ASBRs) operated under different hydraulic retention times (HRTs) ranging from 12 to 36 h and COD (Chemical Oxygen Demand)/SO42−) ratios of 2.4, 1.6 and 0.8.
Externí odkaz:
https://doaj.org/article/a54207990fa847f99cd11979d98bedd4
Autor:
Rajesh Singh, Chungman Moon, Sathyanarayan S. Veeravalli, Saravanan R. Shanmugam, Subba Rao Chaganti, Jerald A. Lalman
Publikováno v:
Water, Vol 6, Iss 11, Pp 3478-3494 (2014)
Taguchi statistical design, an orthogonal array (OA) method, was used to study the impact of the COD/SO42− ratio, hydraulic retention time (HRT) and linoleic acid (LA) concentration on sulfate (SO42−) reduction in an anaerobic sequencing batch re
Externí odkaz:
https://doaj.org/article/45ddc4e542fa47fba25f8aea0d3a733f
Publikováno v:
Water, Vol 6, Iss 6, Pp 1785-1806 (2014)
Due to the toxicity effects and endocrine disrupting properties of phenolic compounds, their removal from water and wastewater has gained widespread global attention. In this study, the photocatalytic degradation of phenolic compounds in the presence
Externí odkaz:
https://doaj.org/article/e5a7bc472a244078a4e1952e4485ebac
Autor:
S. Subramaniyasharma, Saravanan R. Shanmugam, V. Bhuvaneswari, V. Ponnusami, S. Rangabhashiyam
Publikováno v:
Biomass Conversion and Biorefinery.
Autor:
Sreekala G. Bajwa, Jamileh Shojaeiarani, Sushil Adhikari, Saravanan R. Shanmugam, Pankaj Pandey, Dilpreet S. Bajwa
Publikováno v:
Construction and Building Materials. 204:193-202
Bio-composite samples were manufactured using poly (lactic acid) (PLA), high density polyethylene (HDPE), biochar, wood flour, and coupling agent. Biochar, a carbon rich and thermally stable material, derived from switchgrass under controlled pyrolys
Publikováno v:
Transactions of the ASABE. 62:1435-1445
HighlightsGlyphosate sorption using bio-based adsorbents was investigated in this study.Biochars showed poor sorption of glyphosate in comparison to the activated carbons.Total pore volume of bio-based adsorbents played a key role in sorption of glyp
Autor:
Nourredine Abdoulmoumine, Hyungseok Nam, Sushil Adhikari, Zhouhong Wang, Saravanan R. Shanmugam
Publikováno v:
International Journal of Hydrogen Energy. 43:18790-18800
Gasification tar during a fluidized bed operation impedes syngas utilization in downstream applications. Among tar constituents sampled during biomass gasification, benzene was the most abundant species. Thus, benzene was used as a model compound for
Publikováno v:
Biomass and Bioenergy. 108:479-486
Activated carbon is known to enhance methane formation in anaerobic reactors via interspecies electron transfer between fermentative bacteria and methanogenic archaea. Biochar, a by-product of biomass pyrolysis process, could also perform similar fun
Autor:
Srimanta Ray, Nihar Biswas, Jerald A. Lalman, Saravanan R. Shanmugam, Sathyanarayanan S. Veeravalli
Developing a global hydrogen (H2) economy is driven by the rapid evolution of solid-state fuel cells for the automotive sector. Approximately 95% of the currently produced H2 is derived from fossil fuels, natural gas, liquid hydrocarbons, coal, and e
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::ee8e2636634c127c4940d343d6d3f0f5
https://doi.org/10.1016/b978-0-12-817941-3.00015-2
https://doi.org/10.1016/b978-0-12-817941-3.00015-2
Autor:
Myung Won Seo, Hyungseok Nam, Doyeon Lee, Shuang Wang, Saravanan R. Shanmugam, Rajdeep Shakya, K.C. Sanjeev, Sushil Adhikari
Publikováno v:
Energy Conversion and Management. 225:113408
Gasification is one of the methods of generating biopower or biofuels from biomass waste. In this study, a bench-scale fluidized bed reactor was used for biomass air and air-steam gasification. Gasification was performed under constant operating cond