Siddharth Gadkari

Dr. Siddharth Gadkari

orcid

Research Focus & Metrics

Academic Career Length

14Years (2013-Present)

(Calculated once Scilit publication data is synced: current year − year of first publication + 1)

Representative Publications

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9 April 2019 in Green Chemistry
Verified
Journal Article
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Jhuma SadhukhanJhuma Sadhukhan
Jhuma Sadhukhan
SGSiddharth Gadkari
Siddharth Gadkari
EHELIAS MARTINEZ HERNANDEZ
ELIAS MARTINEZ HERNANDEZ
KNKok Siew Ng
Kok Siew Ng
MSMobolaji Shemfe
Mobolaji Shemfe
JLJim Lynch
Jim Lynch
Highly efficient macroalgae based chemical factories and environmental protection have been comprehensively studied for the first time to displace fossil resources to mitigate climate change impact. Wild macroalgae by (bio)phytoremediation and residual macroalgae by biosorption can be used to treat wastewaters, marine environment, soil and sludge. Cultured macroalgae can be processed through drying, milling, grinding, suspension in deionised water and filtration extracting sap of heavy metals; centrifugation of solids recovering nutrients; ion exchange resins of supernatants separating protein and polysaccharides; dialysis purifying protein from salts and pretreatment of polysaccharides producing a sugar platform. Protein profiling shows the presence of the essential amino acids as well as others as food additive, flavour enhancer and pharmaceutical ingredient. Sugars can be converted into a chemical: levulinic acid by controlled acid hydrolysis; 2,5-furandicarboxylic acid by heterogeneous catalytic reaction; succinic acid by tricarboxylic acid cycle; lactic acid by fermentation, with 3–5 times market value than bioethanol. Protein, sugar based chemical and inorganics give the highest to the lowest climate change impact savings of 12, 3 and 1 kg CO2 equivalent per kg product. Their cost of production is estimated at $2010 t−1, significantly lower than their market prices, making the integrated marine biorefinery system economically more attractive than lignocellulosic terrestrial biorefinery systems. Social life cycle assessment indicates that the highest to the lowest avoided social impacts will be from the displacements of animal based protein, sugars and minerals, in Indonesia, China and Philippines (producing 27 million tonnes per annum, 93% of global production).

1 May 2020 in Chemical Engineering Journal
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Journal Article
Open access
SGSiddharth Gadkari
Siddharth Gadkari
JFJean-Marie Fontmorin
Jean-Marie Fontmorin
EYEileen Yu
Eileen Yu
JSJhuma Sadhukhan
Jhuma Sadhukhan

1 November 2017 in Fuel Processing Technology
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Journal Article
Open access
SLS.Y. Liu
S.Y. Liu
DMD.H. Mei
D.H. Mei
MNM.A. Nahil
M.A. Nahil
SGSiddharth Gadkari
Siddharth Gadkari
SGS. Gu
S. Gu
XTX. Tu
X. Tu

1 July 2018 in Chemical Engineering Journal
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Journal Article
Open access
SGSiddharth Gadkari
Siddharth Gadkari
SGSai Gu
Sai Gu
JSJhuma Sadhukhan
Jhuma Sadhukhan

1 May 2018 in Bioresource Technology
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Journal Article
Open access
MSMobolaji Shemfe
Mobolaji Shemfe
SGSiddharth Gadkari
Siddharth Gadkari
EYEileen Yu
Eileen Yu
SRShahid Rasul
Shahid Rasul
KSKeith Scott
Keith Scott
Jhuma SadhukhanJhuma Sadhukhan
Jhuma Sadhukhan
A novel framework, integrating dynamic simulation (DS), life cycle assessment (LCA) and techno-economic assessment (TEA) of a bioelectrochemical system (BES), has been developed to study for the first time wastewater treatment by removal of chemical oxygen demand (COD) by oxidation in anode and thereby harvesting electron and proton for carbon dioxide reduction reaction or reuse to produce products in cathode. Increases in initial COD and applied potential increase COD removal and production (in this case formic acid) rates. DS correlations are used in LCA and TEA for holistic performance analyses. The cost of production of HCOOH is €0.015-0.005 g-1 for its production rate of 0.094-0.26 kg yr-1 and a COD removal rate of 0.038-0.106 kg yr-1. The life cycle (LC) benefits by avoiding fossil-based formic acid production (93%) and electricity for wastewater treatment (12%) outweigh LC costs of operation and assemblage of BES (-5%), giving a net 61MJkg-1 HCOOH saving.

1 May 2021 in Waste Management
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Journal Article
Open access
SGSiddharth Gadkari
Siddharth Gadkari
DKDeepak Kumar
Deepak Kumar
ZQZi-Hao Qin
Zi-Hao Qin
Carol Sze Ki LinCarol Sze Ki Lin
Carol Sze Ki Lin
VKVinod Kumar
Vinod Kumar
According to the US Department of Energy, succinic acid (SA) is a top platform chemical that can be produced from biomass. Bread waste, which has high starch content, is the second most wasted food in the UK and can serve as a potential low cost feedstock for the production of SA. This work evaluates the environmental performance of a proposed biorefinery concept for SA production by fermentation of waste bread using a cradle-to-factory gate life cycle assessment approach. The performance was assessed in terms of greenhouse gas (GHG) emissions and non-renewable energy use (NREU). Waste bread fermentation demonstrated a better environmental profile compared to the fossil-based system, however, GHG emissions were about 50% higher as compared to processes using other biomass feedstocks such as corn wet mill or sorghum grains. NREU for fermentative SA production using waste bread was significantly lower (~ 46%) than fossil-based system and about the same as that of established biomass-based processes, thus proving the great potential of waste bread as a valuable feedstock for bioproduction of useful chemicals. The results show that steam and heating oil used in the process were the biggest contributors to the NREU and GHG emissions. Sensitivity analyses highlighted the importance of the solid biomass waste generated in the process which can potentially be used as fish feed. The LCA analysis can be used for targeted optimization of SA production from bread waste, thereby enabling the utilization of an otherwise waste stream and leading to the establishment of a circular economy.