crude glycerol
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Author(s):  
Naomi Murakawa ◽  
Takaiku Sakamoto ◽  
Mizuho Kanoh ◽  
Si-Bum Park ◽  
Shigenobu Kishino ◽  
...  

Catalysts ◽  
2021 ◽  
Vol 11 (12) ◽  
pp. 1537
Author(s):  
Gayathri Arun ◽  
Muhammad Ayoub ◽  
Zulqarnain Zulqarnain ◽  
Umesh Deshannavar ◽  
Mohd Hizami Mohd Mohd Yusoff ◽  
...  

Biodiesel production has gained considerable importance over the last few decades due to the increase in fossil fuel prices as well as toxic emissions of oxygen and nitrogen. The production of biodiesel via catalytic transesterification produces crude glycerol as a co-product along with biodiesel, amounting to 10% of the total biodiesel produced. Glycerol has a low value in its impure form, and the purification of glycerol requires sophisticated technologies and is an expensive process. The conversion of crude glycerol into value-added chemicals such as solketal is the best way to improve the sustainability of biodiesel synthesis using the transesterification reaction. Therefore, the conversion of crude glycerol into the solketal was investigated in a batch reactor simulation model developed by the Aspen Plus V11.0. The non-random two liquid theory (NRTL) method was used as a thermodynamic property package to study the effect of four input ketalization parameters. The model was validated with the findings of previous experimental studies of solketal synthesis using sulfuric acid as a catalyst. The influence of the following operating parameters was investigated: reaction time of 10,000 to 60,000 s, reaction temperature of 303 to 323 K, acetone to glycerol molar ratio of 2:1 to 10:1, and catalyst concentration of 0.005 to 0.03 wt %. The optimum solketal yield of 81.36% was obtained at the optimized conditions of 313 K, 9:1, 0.03 wt %, and 40,000 s. The effect of each input parameter on the ketalization process and interaction between input and output parameters was investigated by using the response surface methodology (RSM) optimizer. The relationship between independent and response variables developed by RSM fit most of the simulation data, which showed the accuracy of the model. A second-order differential equation fit the simulation data well and showed an R2 value of 0.99. According to the findings of RSM, the influence of catalyst amount, acetone to glycerol molar ratio, and reaction time were more significant on solketal yield. The effect of temperature on the performance of the reaction was not found to be significant because of the exothermic nature of the process. The findings of this study showed that biodiesel-derived glycerol can be effectively utilized to produce solketal, which can be used for a wider range of applications such as a fuel additive. However, further work is required to enhance the solketal yield by developing new heterogeneous catalysts so that the industrial implementation of its production can be made possible.


Reactions ◽  
2021 ◽  
Vol 2 (4) ◽  
pp. 499-513
Author(s):  
Eleni-Stavroula Vastaroucha ◽  
Sofia Maina ◽  
Savvoula Michou ◽  
Ourania Kalantzi ◽  
Chrysanthi Pateraki ◽  
...  

The utilization of crude glycerol, generated as a by-product from the biodiesel production process, for the production of high value-added products represents an opportunity to overcome the negative impact of low glycerol prices in the biodiesel industry. In this study, the biochemical behavior of Yarrowia lipolytica strains FMCC Y-74 and FMCC Y-75 was investigated using glycerol as a carbon source. Initially, the effect of pH value (3.0–7.0) was examined to produce polyols, intracellular lipids, and polysaccharides. At low pH values (initial pH 3.0–5.0), significant mannitol production was recorded. The highest mannitol production (19.64 g L−1) was obtained by Y. lipolytica FMCC Y-74 at pH = 3.0. At pH values ranging between 5.0 and 6.0, intracellular polysaccharides synthesis was favored, while polyols production was suppressed. Subsequently, the effect of crude glycerol and its concentration on polyols production was studied. Y. lipolytica FMCC Y-74 showed high tolerance to impurities of crude glycerol. Initial substrate concentrations influence polyols production and distribution with a metabolic shift toward erythritol production being observed when the initial glycerol concentration (Gly0) increased. The highest total polyols production (=56.64 g L−1) was obtained at Gly0 adjusted to ≈120 g L−1. The highest polyols conversion yield (0.59 g g−1) and productivity (4.36 g L−1 d−1) were reached at Gly0 = 80 g L−1. In fed-batch intermittent fermentation with glycerol concentration remaining ≤60 g L−1, the metabolism was shifted toward mannitol biosynthesis, which was the main polyol produced in significant quantities (=36.84 g L−1) with a corresponding conversion yield of 0.51 g g−1.


2021 ◽  
Vol 342 ◽  
pp. 125918
Author(s):  
Saehee Lee ◽  
Amith Abraham ◽  
Alan Christian S. Lim ◽  
Okkyoung Choi ◽  
Jeong Gil Seo ◽  
...  

2021 ◽  
Vol 945 (1) ◽  
pp. 012038
Author(s):  
Janice Sheow Tung Liew ◽  
Siew Yong Leong ◽  
Po Kim Lo

Abstract Valorisation of crude glycerol has gained much interest in the industry associated with the surplus of crude glycerol caused by the increase usage of biodiesel. Transesterification of crude glycerol using a heterogenous base catalyst is one of the effective ways to utilize the additional glycerol. Seawater clams commonly serve as a food source to us and the waste shells are a source of calcium carbonate that is abundantly available and can be converted into a heterogenous base catalyst for the transesterification process. Therefore, this study focuses on the utilization of catalyst synthesized from a species of seawater clam, Paratapes Undulatus in a transesterification reaction using crude glycerol (C.GLY) as a reactant together with dimethyl carbonate (DMC) to synthesize glycerol carbonate (GLYC). The catalysts are characterized using Field Emission Scanning Electron Microscope (FESEM), Attenuated Total Reflectance (ATR), Thermogravimetric Analysis (TGA), X-ray diffraction (XRD) and Particle Size Analyser (PSA). The product is characterized using Gas Chromatography (GC-FID). The performance of the synthesized shell catalyst with different calcination condition was studied. The reaction using the calcined shell catalyst is carried out at 75°C, molar ratio of 2 and 2wt% of catalyst for 1 hour. The catalyst that has the best performance is the shell catalyst that is calcined for 3h, which give the yield of 54.16%.


LWT ◽  
2021 ◽  
pp. 112951
Author(s):  
C. Quintelas ◽  
A. Braga ◽  
A. Cordeiro ◽  
E.C. Ferreira ◽  
I. Belo ◽  
...  

Chemosphere ◽  
2021 ◽  
pp. 133426
Author(s):  
Pragya Gupta ◽  
Manoj Kumar Upreti ◽  
Ravi Prakash Gupta ◽  
Suresh Kumar Puri ◽  
S.S.V. Ramakumar

Energy ◽  
2021 ◽  
pp. 122818
Author(s):  
Ingrid R.F.S. Alves ◽  
Claudio F. Mahler ◽  
Luciano B. Oliveira ◽  
Marcelo M. Reis ◽  
João P. Bassin

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