Kinetics study of total organic carbon destruction during supercritical water gasification of glucose
Muhammad Badrul Islam Chowdhury
Natural Resources Canada, CanmetENERGY, Devon, Alberta, Canada
Search for more papers by this authorCorresponding Author
Md Zakir Hossain
Department of Chemical and Biochemical Engineering, Western University, London, Ontario, Canada
Department of Chemical Engineering and Polymer Science, Shahjalal University of Science and Technology, Sylhet, Bangladesh
Correspondence
Paul A. Charpentier and Md Zakir Hossain, Department of Chemical and Biochemical Engineering, Western University, London, Ontario N6A 5B9, Canada.
Email: [email protected] and [email protected]
Search for more papers by this authorCorresponding Author
Paul A. Charpentier
Department of Chemical and Biochemical Engineering, Western University, London, Ontario, Canada
Correspondence
Paul A. Charpentier and Md Zakir Hossain, Department of Chemical and Biochemical Engineering, Western University, London, Ontario N6A 5B9, Canada.
Email: [email protected] and [email protected]
Search for more papers by this authorMuhammad Badrul Islam Chowdhury
Natural Resources Canada, CanmetENERGY, Devon, Alberta, Canada
Search for more papers by this authorCorresponding Author
Md Zakir Hossain
Department of Chemical and Biochemical Engineering, Western University, London, Ontario, Canada
Department of Chemical Engineering and Polymer Science, Shahjalal University of Science and Technology, Sylhet, Bangladesh
Correspondence
Paul A. Charpentier and Md Zakir Hossain, Department of Chemical and Biochemical Engineering, Western University, London, Ontario N6A 5B9, Canada.
Email: [email protected] and [email protected]
Search for more papers by this authorCorresponding Author
Paul A. Charpentier
Department of Chemical and Biochemical Engineering, Western University, London, Ontario, Canada
Correspondence
Paul A. Charpentier and Md Zakir Hossain, Department of Chemical and Biochemical Engineering, Western University, London, Ontario N6A 5B9, Canada.
Email: [email protected] and [email protected]
Search for more papers by this authorAbstract
The kinetics of total organic carbon (TOC) destruction during supercritical water gasification (SCWG) of glucose were studied at 400–500°C and 25 MPa in a 600 mL batch reactor. Both TOC and water concentrations are critical for the conversion of TOC in supercritical water, especially at longer residence times. Initially, it was assumed that the TOC destruction reaction followed first-order kinetics ignoring the water concentration. However, experimental results showed that the feed-to-water ratio had a significant effect on TOC decomposition. Considering the water concentration in the reaction, the reaction orders of TOC (2.35) and water (1.45) were calculated using nonlinear regression analysis (the Runge-Kutta method). The estimated pre-exponential factor (k’) and activation energy (E) were calculated to be 8.1 ± 2/min and 90.37 ± 9.38 kJ/mol respectively.
CONFLICT OF INTEREST STATEMENT
There is no conflict of interest to disclose.
Open Research
DATA AVAILABILITY STATEMENT
The data that supports the findings of this study will be made available on request.
Supporting Information
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REFERENCES
- 1Shahbeik H, Peng W, Panahi HKS, et al. Synthesis of liquid biofuels from biomass by hydrothermal gasification: a critical review. Renew Sustain Energy Rev. 2022; 167:112833.
- 2Zhang F, Li Y, Liang Z, Wu T. Energy conversion and utilization in supercritical water oxidation systems: a review. Biomass Bioenergy. 2022; 156:106322.
- 3Chen Y, Yi L, Yin J, Jin H, Guo L. Sewage sludge gasification in supercritical water with fluidized bed reactor: reaction and product characteristics. Energy. 2022; 239:122115.
- 4Peterson AA, Vogel F, Lachance RP, Fröling M, Antal Jr MJ, Tester JW. Thermochemical biofuel production in hydrothermal media: a review of sub-and supercritical water technologies. Energy Environ Sci. 2008; 1: 32-65.
- 5Calzavara Y, Joussot-Dubien C, Boissonnet G, Sarrade S. Evaluation of biomass gasification in supercritical water process for hydrogen production. Energy Convers Manage. 2005; 46: 615-631.
- 6Demirel E, Erkey C, Ayas N. Supercritical water gasification of fruit pulp for hydrogen production: effect of reaction parameters. J Supercrit Fluids. 2021; 177:105329.
- 7Wang C, Li L, Chen Y, Ge Z, Jin H. Supercritical water gasification of wheat straw: composition of reaction products and kinetic study. Energy. 2021; 227:120449.
- 8Adar E, Ince M, Bilgili MS. Supercritical water gasification of sewage sludge by continuous flow tubular reactor: a pilot scale study. Chem Eng J. 2020; 391:123499.
- 9Su W, Cai C, Liu P, et al. Supercritical water gasification of food waste: effect of parameters on hydrogen production. Int J Hydrogen Energy. 2020; 45: 14744-14755.
- 10Hossain MZ, Karim MR, Sutradhar S, Chowdhury MBI, Charpentier PA. Hydrothermal gasification of glucose for H2 production using Ni–Al2O3 nanocatalyst. Int J Hydrogen Energy. 2023; 48(100): 39791-39804.
- 11Hao X, Guo L, Xa Mao, Zhang X, Chen X. Hydrogen production from glucose used as a model compound of biomass gasified in supercritical water. Int J Hydrogen Energy. 2003; 28: 55-64.
- 12Bai B, Liu Y, Wang Q, et al. Experimental investigation on gasification characteristics of plastic wastes in supercritical water. Renewable Energy. 2019; 135: 32-40.
- 13Lu B, Bai B, Zhang R, et al. Study on gasification characteristics and kinetics of polyformaldehyde plastics in supercritical water. J Cleaner Prod. 2023; 383:135459.
- 14Hossain MZ, Chowdhury MB, Charpentier PA. Effect of surface acidity of Al2O3 supported metal catalysts on catalytic activity and carbon deposition during SCWG of glucose. Biomass Bioenergy. 2019; 124: 142-150.
- 15Hossain MZ, Chowdhury MB, Alsharari Q, Jhawar AK, Charpentier PA. Effect of mesoporosity of bimetallic Ni-Ru-Al2O3 catalysts for hydrogen production during supercritical water gasification of glucose. Fuel Process Technol. 2017; 159: 55-66.
- 16Chowdhury MB, Hossain MZ, Mazumder J, Jhawar AK, Charpentier PA. La-based catalysts to enhance hydrogen production during supercritical water gasification of glucose. Fuel. 2018; 217: 166-174.
- 17Chowdhury MB, Hossain MM, Charpentier PA. Effect of supercritical water gasification treatment on Ni/La2O3-Al2O3-based catalysts. Appl Catal, A. 2011; 405: 84-92.
- 18Abdpour S, Santos RM. Recent advances in heterogeneous catalysis for supercritical water oxidation/gasification processes: insight into catalyst development. Process Saf Environ Prot. 2021; 149: 169-184.
- 19Lu Y, Li S, Guo L. Catalysis in supercritical water gasification of biomass: status and prospects. In: Z Fang, C Xu, eds. Near-critical and Supercritical Water and Their Applications for Biorefineries. Biofuels Biorefin; 2014: 343-371.
10.1007/978-94-017-8923-3_13 Google Scholar
- 20Oshima Y, Tomita K, Koda S. Kinetics of the catalytic oxidation of phenol over manganese oxide in supercritical water. Ind Eng Chem Res. 1999; 38: 4183-4188.
- 21D'Jesús P, Boukis N, Kraushaar-Czarnetzki B, Dinjus E. Gasification of corn and clover grass in supercritical water. Fuel. 2006; 85: 1032-1038.
- 22Lee I-G, Kim M-S, Ihm S-K. Gasification of glucose in supercritical water. Ind Eng Chem Res. 2002; 41: 1182-1188.
- 23Yu Y, Wu H. Kinetics and mechanism of glucose decomposition in hot-compressed water: effect of initial glucose concentration. Ind Eng Chem Res. 2011; 50: 10500-10508.
- 24Kabyemela BM, Adschiri T, Malaluan RM, Arai K. Glucose and fructose decomposition in subcritical and supercritical water: detailed reaction pathway, mechanisms, and kinetics. Ind Eng Chem Res. 1999; 38: 2888-2895.
- 25Qi J, Xiuyang L. Kinetics of non-catalyzed decomposition of glucose in high-temperature liquid water. Chin J Chem Eng. 2008; 16: 890-894.
- 26Ramli NAS, Amin NAS. Kinetic study of glucose conversion to levulinic acid over Fe/HY zeolite catalyst. Chem Eng J. 2016; 283: 150-159.
- 27Lu Y, Guo L, Ji C, Zhang X, Hao X, Yan Q. Hydrogen production by biomass gasification in supercritical water: a parametric study. Int J of Hydrogen Energy. 2006; 31: 822-831.
- 28Kruse A, Gawlik A. Biomass conversion in water at 330− 410 C and 30− 50 MPa. Identification of key compounds for indicating different chemical reaction pathways. Ind Eng Chem Res. 2003; 42: 267-279.
- 29Kabyemela BM, Adschiri T, Malaluan RM, Arai K. Kinetics of glucose epimerization and decomposition in subcritical and supercritical water. Ind Eng Chem Res. 1997; 36: 1552-1558.
- 30Holgate HR, Meyer JC, Tester JW. Glucose hydrolysis and oxidation in supercritical water. AICHE J. 1995; 41: 637-648.
- 31Williams PT, Onwudili J. Composition of products from the supercritical water gasification of glucose: a model biomass compound. Ind Eng Chem Res. 2005; 44: 8739-8749.
- 32Youssef EA, Chowdhury MB, Nakhla G, Charpentier P. Effect of nickel loading on hydrogen production and chemical oxygen demand (COD) destruction from glucose oxidation and gasification in supercritical water. Int J Hydrogen Energy. 2010; 35: 5034-5042.
- 33Hossain MZ, Chowdhury MB, Jhawar AK, Charpentier PA. Supercritical water gasification of glucose using bimetallic aerogel Ru-Ni-Al2O3 catalyst for H2 production. Biomass Bioenergy. 2017; 107: 39-51.
- 34Yan Q, Guo L, Lu Y. Thermodynamic analysis of hydrogen production from biomass gasification in supercritical water. Energy Convers Manage. 2006; 47: 1515-1528.
- 35Harris C, Roekaerts D, Rosendal F, et al. Computational fluid dynamics for chemical reactor engineering. Chem Eng Sci. 1996; 51: 1569-1594.
- 36Kim HS, Park N-K, Lee TJ, Um M-H, Kang M. Preparation of Nanosized α-Al2O3 Particles Using a Microwave Pretreatment at Mild Temperature. Adv Mater Sci Eng. 2012; 2012:920105.
- 37Qiao H, Wei Z, Yang H, Zhu L, Yan X. Preparation and characterization of NiO nanoparticles by anodic arc plasma method. J Nanomater. 2009; 2009: 1-5.
- 38Melchor-Hernández C, Gómez-Cortés A, Díaz G. Hydrogen production by steam reforming of ethanol over nickel supported on La-modified alumina catalysts prepared by sol–gel. Fuel. 2013; 107: 828-835.
- 39Ribeiro J, De Andrade AR. Characterization of RuO2 Ta2O5 Coated Titanium Electrode: microstructure, Morphology, and Electrochemical Investigation. J Electrochem Soc. 2004; 151: D106.
- 40Biswas A, Paul S, Banerjee A. Carbon nanodots, Ru nanodots and hybrid nanodots: preparation and catalytic properties. J Mater Chem A. 2015; 3: 15074-15081.
- 41Jiang Z, Xie J, Jiang D, Wei X, Chen M. Modifiers-assisted formation of nickel nanoparticles and their catalytic application to p-nitrophenol reduction. CrystEngComm. 2013; 15: 560-569.
- 42Samkaria R, Sharma V. Effect of rare earth yttrium substitution on the structural, dielectric and electrical properties of nanosized nickel aluminate. Mater Sci Eng, B. 2013; 178: 1410-1415.