Remediation of Saline Wastewater Producing a Fuel Gas Containing Alkanes and Hydrogen Using Zero Valent Iron (Fe0)

Zero valent iron (Fe0) water remediation studies, over the last 40 years, have periodically reported the discovery of CnH2n+2 in the product water or product gas, where n = 1 to 20. Various theories have been proposed for the presence of these hydrocarbons. These include: (i) reductive transformatio...

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Published in:Water
Main Author: David Dorab Jamshed Antia
Format: Text
Language:English
Published: Multidisciplinary Digital Publishing Institute 2022
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Online Access:https://doi.org/10.3390/w14121926
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spelling ftmdpi:oai:mdpi.com:/2073-4441/14/12/1926/ 2023-08-20T04:05:54+02:00 Remediation of Saline Wastewater Producing a Fuel Gas Containing Alkanes and Hydrogen Using Zero Valent Iron (Fe0) David Dorab Jamshed Antia agris 2022-06-15 application/pdf https://doi.org/10.3390/w14121926 EN eng Multidisciplinary Digital Publishing Institute Wastewater Treatment and Reuse https://dx.doi.org/10.3390/w14121926 https://creativecommons.org/licenses/by/4.0/ Water; Volume 14; Issue 12; Pages: 1926 aqueous Fischer–Tropsch carbonization catalysis fuel gas green chemistry hydrocarbon formation hydrogen formation municipal waste zero valent iron (ZVI Fe 0 ) Text 2022 ftmdpi https://doi.org/10.3390/w14121926 2023-08-01T05:23:06Z Zero valent iron (Fe0) water remediation studies, over the last 40 years, have periodically reported the discovery of CnH2n+2 in the product water or product gas, where n = 1 to 20. Various theories have been proposed for the presence of these hydrocarbons. These include: (i) reductive transformation of a more complex organic chemical; (ii) hydrogenation of an organic chemical, as part of a degradation process; (iii) catalytic hydrogenation and polymerisation of carbonic acid; and (iv) redox transformation. This study uses wastewater (pyroligneous acid, (pH = 0.5 to 4.5)) from a carbonization reactor processing municipal waste to define the controls for the formation of CnH2n+2 (where n = 3 to 9), C3H4, and C3H6. A sealed, static diffusion, batch flow reactor, containing zero-valent metals [181 g m-Fe0 + 29 g m-Al0 + 27 g m-Cu0 + 40 g NaCl] L−1, was operated at two temperatures, 273–298 K and 348 K, respectively. The reactions, reactant quotients, and rate constants for the catalytic formation of H2(g), CO2(g), C3H4(g), C3H6(g), C3H8(g), C4H10(g), C5H12(g), C6H14(g,l), and C7H16(g,l), are defined as function of zero valent metal concentration (g L−1), reactor pressure (MPa), and reactor temperature (K). The produced fuel gas (422–1050 kJ mole−1) contained hydrogen + CnHy(gas), where n = 3 to 7. The gas production rate was: [1058 moles CnHy + 132 moles H2] m−3 liquid d−1 (operating pressure = 0.1 MPa; temperature = 348 K). Increasing the operating pressure to 1 MPa increased the fuel gas production rate to [2208 moles CnHy + 1071 moles H2] m−3 liquid d−1. In order to achieve these results, the Fe0, operated as a “Smart Material”, simultaneously multi-tasking to create self-assembly, auto-activated catalysts for hydrogen production, hydrocarbon formation, and organic chemical degradation (degrading carboxylic acids and phenolic species to CO2 and CO). Text Carbonic acid MDPI Open Access Publishing Water 14 12 1926
institution Open Polar
collection MDPI Open Access Publishing
op_collection_id ftmdpi
language English
topic aqueous Fischer–Tropsch
carbonization
catalysis
fuel gas
green chemistry
hydrocarbon formation
hydrogen formation
municipal waste
zero valent iron (ZVI
Fe 0 )
spellingShingle aqueous Fischer–Tropsch
carbonization
catalysis
fuel gas
green chemistry
hydrocarbon formation
hydrogen formation
municipal waste
zero valent iron (ZVI
Fe 0 )
David Dorab Jamshed Antia
Remediation of Saline Wastewater Producing a Fuel Gas Containing Alkanes and Hydrogen Using Zero Valent Iron (Fe0)
topic_facet aqueous Fischer–Tropsch
carbonization
catalysis
fuel gas
green chemistry
hydrocarbon formation
hydrogen formation
municipal waste
zero valent iron (ZVI
Fe 0 )
description Zero valent iron (Fe0) water remediation studies, over the last 40 years, have periodically reported the discovery of CnH2n+2 in the product water or product gas, where n = 1 to 20. Various theories have been proposed for the presence of these hydrocarbons. These include: (i) reductive transformation of a more complex organic chemical; (ii) hydrogenation of an organic chemical, as part of a degradation process; (iii) catalytic hydrogenation and polymerisation of carbonic acid; and (iv) redox transformation. This study uses wastewater (pyroligneous acid, (pH = 0.5 to 4.5)) from a carbonization reactor processing municipal waste to define the controls for the formation of CnH2n+2 (where n = 3 to 9), C3H4, and C3H6. A sealed, static diffusion, batch flow reactor, containing zero-valent metals [181 g m-Fe0 + 29 g m-Al0 + 27 g m-Cu0 + 40 g NaCl] L−1, was operated at two temperatures, 273–298 K and 348 K, respectively. The reactions, reactant quotients, and rate constants for the catalytic formation of H2(g), CO2(g), C3H4(g), C3H6(g), C3H8(g), C4H10(g), C5H12(g), C6H14(g,l), and C7H16(g,l), are defined as function of zero valent metal concentration (g L−1), reactor pressure (MPa), and reactor temperature (K). The produced fuel gas (422–1050 kJ mole−1) contained hydrogen + CnHy(gas), where n = 3 to 7. The gas production rate was: [1058 moles CnHy + 132 moles H2] m−3 liquid d−1 (operating pressure = 0.1 MPa; temperature = 348 K). Increasing the operating pressure to 1 MPa increased the fuel gas production rate to [2208 moles CnHy + 1071 moles H2] m−3 liquid d−1. In order to achieve these results, the Fe0, operated as a “Smart Material”, simultaneously multi-tasking to create self-assembly, auto-activated catalysts for hydrogen production, hydrocarbon formation, and organic chemical degradation (degrading carboxylic acids and phenolic species to CO2 and CO).
format Text
author David Dorab Jamshed Antia
author_facet David Dorab Jamshed Antia
author_sort David Dorab Jamshed Antia
title Remediation of Saline Wastewater Producing a Fuel Gas Containing Alkanes and Hydrogen Using Zero Valent Iron (Fe0)
title_short Remediation of Saline Wastewater Producing a Fuel Gas Containing Alkanes and Hydrogen Using Zero Valent Iron (Fe0)
title_full Remediation of Saline Wastewater Producing a Fuel Gas Containing Alkanes and Hydrogen Using Zero Valent Iron (Fe0)
title_fullStr Remediation of Saline Wastewater Producing a Fuel Gas Containing Alkanes and Hydrogen Using Zero Valent Iron (Fe0)
title_full_unstemmed Remediation of Saline Wastewater Producing a Fuel Gas Containing Alkanes and Hydrogen Using Zero Valent Iron (Fe0)
title_sort remediation of saline wastewater producing a fuel gas containing alkanes and hydrogen using zero valent iron (fe0)
publisher Multidisciplinary Digital Publishing Institute
publishDate 2022
url https://doi.org/10.3390/w14121926
op_coverage agris
genre Carbonic acid
genre_facet Carbonic acid
op_source Water; Volume 14; Issue 12; Pages: 1926
op_relation Wastewater Treatment and Reuse
https://dx.doi.org/10.3390/w14121926
op_rights https://creativecommons.org/licenses/by/4.0/
op_doi https://doi.org/10.3390/w14121926
container_title Water
container_volume 14
container_issue 12
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