@article {44528, title = {Mixed bacterial culture mediated direct conversion of bio-glycerol to diols}, journal = {Bioresource Technology}, volume = {250}, year = {2018}, month = {FEB}, pages = {86-93}, abstract = {

Direct and economic transformation of biodiesel derived crude glycerol is gaining more significance. During screening of bacterial cultures Klebsiella pneumoniae and Enterobacter aerogenes were able to convert crude bio-glycerol to 2,3-butanediol (2,3-BDO) and 1,3-propanediol (1,3-PDO), as major compounds, ethanol and acetoin as minor compounds, with a conversion of 69\% and 79\% respectively. Process optimization could achieve maximum conversion at pH 7.0, 37 degrees C, 30-40 g/L glycerol and 1.5 g of inoculum until 120 h. Mixed cultures led to complete glycerol conversion with optimal yield and productivity. An innovative approach of using crude glycerol for sustained growth and tolerance of bacteria as source of carbon and energy makes this study more significant. In addition to this, a mixed culture concept introduced here is expected to make impact in process economics for industrial scale synthesis for direct transformation of glycerol into C3 and specifically, C4 diols.

}, keywords = {1, 2, 3-Butanediol, 3-Propanediol, Bioconversion, Bioglycerol, Mixed culture}, issn = {0960-8524}, doi = {10.1016/j.biortech.2017.11.019}, author = {Parate, Roopa and Mane, Rasika and Dharne, Mahesh and Rode, Chandrashekhar} } @article {48156, title = {Influence of catalyst reduction temperature on autogenous glycerol hydrogenolysis over NiAl catalyst}, journal = {Asian Journal of Organic Chemistry}, volume = {11}, year = {2022}, month = {FEB}, pages = {e202100704}, type = {Article}, abstract = {

Autogenous glycerol hydrogenolysis to 1,2-propanediol by aqueous phase reforming (APR) was investigated over supported nickel catalysts. Effect of reduction temperature on physico-chemical properties of catalysts played a significant role in tuning conversion and product selectivities. The formation of nickel aluminate (NiAl2O4) spinel phase during catalyst reduction led to rearrangement of Ni species to obtain small and stable Ni particles. The catalyst activation temperature alters the extent of reduction of multivalent Ni species (Ni-0, Ni+2/+3) which facilitated glycerol dehydration and hydrogenation while suppressing C-C cleavage and thus avoiding undesirable side products. Additionally, presence of moderate Bronsted/Lewis acid ratio of the catalyst promoted higher 1,2-PDO selectivity. In-situ glycerol hydrogenolysis involves glycerol dehydration to acetol with simultaneous reforming to H-2 and CO2 and this hydrogen converts acetol to 1,2-PDO.

}, keywords = {APR, autogenous hydrogenolysis, Glycerol, Propanediols, reduction temperature, spinel}, issn = {2193-5807}, doi = {10.1002/ajoc.202100704}, author = {Pandya, Rajan and Mane, Rasika and Rode, Chandrashekhar} } @article {48053, title = {Review on non-noble metal catalysts for glycerol hydrodeoxygenation to 1,2-propanediol with and without external hydrogen}, journal = {Green Chemistry}, volume = {24}, year = {2022}, month = {SEP}, pages = {6751-6781}, type = {Review}, abstract = {

The depleting petroleum oil resources, political embargos, and global warming dilemma have made it mandatory to develop alternative green technologies for energy and chemical production. Glycerol is one of the top-12 building block chemicals that can be mainly obtained as a coproduct of biodiesel production. The value addition of glycerol is only possible through its conversion to commodity and fine chemicals. Glycerol hydrogenolysis is one of the crucial pathways to produce several value-added products, among which 1,2-propanediol (1,2-PDO), 1,3-propanediol (1,3-PDO), ethylene glycol (EG) and 1-and/or 2-propanols are hydrogenolysis products. Selective glycerol hydrogenolysis to the desired product 1,2-PDO is only possible through the catalyst having an optimum combination of acid/base and metal sites (metallic and mixed oxides). The present review mainly focuses on the critical assessment of the influence of different supports, catalyst preparation methods, and/or pretreatment on structural, and electronic properties and simultaneously on the activity and product selectivity of non-noble metal catalysts. The role of reaction parameters in this industrially important reaction on catalyst performance will also be presented. A rigorous survey of patented literature on non-noble metal-catalyzed glycerol hydrogenolysis to 1,2-PDO is also discussed. Further, the review covers recent progress on non-noble metal-catalyzed autogenous glycerol hydrogenolysis through glycerol aqueous phase reforming (APR) and/or catalytic transfer hydrogenolysis (CTH), to overcome the cost and handling issues of external hydrogen. Finally, techno-economic analysis is also presented which compares the glycerol hydrogenolysis with and without external hydrogen with the conventional process of 1,2-PDO production. This analysis indicated that CTH and glycerol hydrogenolysis under ambient hydrogen pressure have the potential for commercialization, however catalyst stability and elimination of co-product formation at higher glycerol concentration need to be considered critically.

}, issn = {1463-9262}, doi = {10.1039/d2gc01879a}, author = {Mane, Rasika and Jeon, Yukwon and Rode, Chandrashekhar} } @article {49448, title = {Calcination temperature impacting the structure and activity of CuAl catalyst in aqueous glycerol hydrogenolysis to 1,2-propanediol}, journal = {Topics in Catalysis}, year = {2024}, month = {NOV}, type = {Article}, abstract = {

This study investigated the impact of calcination temperature on the structural properties of CuAl catalyst which was found to be a robust nano-structured catalyst calcined directly without ramping at 400 {\textdegree}C and performed exceedingly well for aqueous phase hydrogenolysis of glycerol. Various samples of CuAl catalysts were prepared by co-precipitation at Cu: Al molar ratio 1:1 and were calcined at different temperatures (300{\textendash}1000 {\textdegree}C). The obtained catalysts were reduced at 200 {\textdegree}C before their activity testing for glycerol hydrogenolysis reaction. To correlate the structure-activity, the catalysts were thoroughly characterized by XRD, XPS, BET, TEM, H2-TPR, NH3-TPD, and pyridine FTIR. It was observed that with an increase in calcination temperature from 300 to 700\ {\textdegree}C, the glycerol conversion also increased from 47 to 55\% with 93\% selectivity to 1,2-PDO. The better performance of these catalysts was mainly related to the predominant presence of Br{\o}nsted acid sites, an appropriate ratio of the Cu0\ to CuAl2O4 + CuO (0.33) and CuAl2O4\ to CuO phases (0.35), the existence of Cu2O phase and the smaller Cu0\ particle size. It was shown that altering the ramping rate for the calcination temperature of 400\ {\textdegree}C impacted the catalytic activity. The CuAl-400 (DC) (direct calcined) catalyst exhibited a maximum glycerol conversion of 60\%.

}, doi = {https://doi.org/10.1007/s11244-024-02032-5}, author = {Mane, Rasika and Potdar, Aparna and Jeon, Yukwon and Rode, Chandrashekhar} }