Evaluation of pressure and temperature effects on hydropyrolysis of pine sawdust: pyrolysate composition and kinetics studies

Hydropyrolysis is a vital step in IH 2® technology for the production of fungible drop-in biofuels from biomass and waste feedstocks. Hydrogen at high pressures in fast hydropyrolysis aids in improving the H/C ratio of bio-oil through deoxygenation pathways such as dehydration, decarboxylation and d...

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Veröffentlicht in:Reaction chemistry & engineering 2020-08, Vol.5 (8), p.1484-15
Hauptverfasser: Venkatesan, Kavimonica, Prashanth, Francis, Kaushik, Vinay, Choudhari, Harshavardhan, Mehta, Dhairya, Vinu, Ravikrishnan
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container_issue 8
container_start_page 1484
container_title Reaction chemistry & engineering
container_volume 5
creator Venkatesan, Kavimonica
Prashanth, Francis
Kaushik, Vinay
Choudhari, Harshavardhan
Mehta, Dhairya
Vinu, Ravikrishnan
description Hydropyrolysis is a vital step in IH 2® technology for the production of fungible drop-in biofuels from biomass and waste feedstocks. Hydrogen at high pressures in fast hydropyrolysis aids in improving the H/C ratio of bio-oil through deoxygenation pathways such as dehydration, decarboxylation and decarbonylation. The main objectives of this study are to understand the composition of organics and the time evolution of various functional groups during fast hydropyrolysis of pine sawdust at different temperatures, pressures, and in the presence of a catalyst. Analytical fast pyrolysis experiments were conducted in a Pyroprobe ® reactor interfaced with a gas chromatograph/mass spectrometer (GC/MS) and Fourier transform infrared (FTIR) spectrometer. At high hydrogen partial pressures (10 and 20 bar), significant production of hydrocarbons, in contrast to undesirable oxygen-containing compounds at low pressures, was observed. Moreover, it resulted in a minor increase in the yield of pyrolysates and char, while the yields of pyrolysates and char increased and decreased, respectively, as the temperature was increased at high hydrogen partial pressures. The overall yield of condensable pyrolysates from hydropyrolysis was notably higher as compared to that from pyrolysis in inert atmosphere. The use of a stainless steel catalyst tube in the Pyroprobe ® improved the formation of hydrocarbons as compared to that of a quartz tube at high pressures. Upgradation of pyrolysis vapors evolved from hydropyrolysis of pine sawdust at 500 °C and 20 bar over the catalyst bed maintained at 500 °C resulted in selective production of aromatic hydrocarbons (12% C 6 , 32% C 7 , 20% C 8 , 9% C 9 , 7% C 10 , and 4% C 11 ). The isothermal mass loss data at short residence times were obtained using the analytical Pyroprobe ® , and the apparent rate constants were determined using a 3D-diffusion model. Pyrolysis-FTIR data substantiate the significant increase in methane production with the increase in pressure. Pyrolysate composition data from Py-FTIR and Py-GC/MS techniques at various pressures were assimilated to develop a reaction scheme to describe non-catalytic and catalytic hydropyrolysis of biomass. Kinetics and product distribution from high pressure hydropyrolysis of biomass using Py-GC/MS and Py-FTIR.
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Moreover, it resulted in a minor increase in the yield of pyrolysates and char, while the yields of pyrolysates and char increased and decreased, respectively, as the temperature was increased at high hydrogen partial pressures. The overall yield of condensable pyrolysates from hydropyrolysis was notably higher as compared to that from pyrolysis in inert atmosphere. The use of a stainless steel catalyst tube in the Pyroprobe ® improved the formation of hydrocarbons as compared to that of a quartz tube at high pressures. Upgradation of pyrolysis vapors evolved from hydropyrolysis of pine sawdust at 500 °C and 20 bar over the catalyst bed maintained at 500 °C resulted in selective production of aromatic hydrocarbons (12% C 6 , 32% C 7 , 20% C 8 , 9% C 9 , 7% C 10 , and 4% C 11 ). The isothermal mass loss data at short residence times were obtained using the analytical Pyroprobe ® , and the apparent rate constants were determined using a 3D-diffusion model. Pyrolysis-FTIR data substantiate the significant increase in methane production with the increase in pressure. Pyrolysate composition data from Py-FTIR and Py-GC/MS techniques at various pressures were assimilated to develop a reaction scheme to describe non-catalytic and catalytic hydropyrolysis of biomass. 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Hydrogen at high pressures in fast hydropyrolysis aids in improving the H/C ratio of bio-oil through deoxygenation pathways such as dehydration, decarboxylation and decarbonylation. The main objectives of this study are to understand the composition of organics and the time evolution of various functional groups during fast hydropyrolysis of pine sawdust at different temperatures, pressures, and in the presence of a catalyst. Analytical fast pyrolysis experiments were conducted in a Pyroprobe ® reactor interfaced with a gas chromatograph/mass spectrometer (GC/MS) and Fourier transform infrared (FTIR) spectrometer. At high hydrogen partial pressures (10 and 20 bar), significant production of hydrocarbons, in contrast to undesirable oxygen-containing compounds at low pressures, was observed. Moreover, it resulted in a minor increase in the yield of pyrolysates and char, while the yields of pyrolysates and char increased and decreased, respectively, as the temperature was increased at high hydrogen partial pressures. The overall yield of condensable pyrolysates from hydropyrolysis was notably higher as compared to that from pyrolysis in inert atmosphere. The use of a stainless steel catalyst tube in the Pyroprobe ® improved the formation of hydrocarbons as compared to that of a quartz tube at high pressures. Upgradation of pyrolysis vapors evolved from hydropyrolysis of pine sawdust at 500 °C and 20 bar over the catalyst bed maintained at 500 °C resulted in selective production of aromatic hydrocarbons (12% C 6 , 32% C 7 , 20% C 8 , 9% C 9 , 7% C 10 , and 4% C 11 ). The isothermal mass loss data at short residence times were obtained using the analytical Pyroprobe ® , and the apparent rate constants were determined using a 3D-diffusion model. Pyrolysis-FTIR data substantiate the significant increase in methane production with the increase in pressure. Pyrolysate composition data from Py-FTIR and Py-GC/MS techniques at various pressures were assimilated to develop a reaction scheme to describe non-catalytic and catalytic hydropyrolysis of biomass. Kinetics and product distribution from high pressure hydropyrolysis of biomass using Py-GC/MS and Py-FTIR.</abstract><cop>CAMBRIDGE</cop><pub>Royal Soc Chemistry</pub><doi>10.1039/d0re00121j</doi><orcidid>https://orcid.org/0000-0003-3192-6108</orcidid><orcidid>https://orcid.org/0000-0002-9757-8225</orcidid></addata></record>
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subjects Aromatic hydrocarbons
Biofuels
Biomass
Catalysts
Chemistry
Chemistry, Multidisciplinary
Composition
Decarboxylation
Dehydration
Deoxygenation
Diffusion rate
Engineering
Engineering, Chemical
Evolution
Fourier transforms
Functional groups
Gas chromatography
Hydrocarbons
Hydrogen
Hydropyrolysis
Inert atmospheres
Infrared spectrometers
Infrared spectroscopy
Physical Sciences
Pressure effects
Rate constants
Reaction kinetics
Sawdust
Science & Technology
Stainless steels
Technology
Temperature effects
Three dimensional models
title Evaluation of pressure and temperature effects on hydropyrolysis of pine sawdust: pyrolysate composition and kinetics studies
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