Hydrodechlorination of Carbon Tetrachloride over Pt/MgO

Hydrodechlorination of carbon tetrachloride (CCl4) has been studied at various reaction temperatures, mole ratios (H2/CCl4), and WHSVs over 1% Pt/MgO. The main factors determining conversion of CCl4and deactivation of the catalyst were reaction temperature and H2/CCl4mole ratio. The optimum reaction...

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Veröffentlicht in:Journal of Catalysis 1996-07, Vol.161 (2), p.790-797
Hauptverfasser: Chul Choi, Hyun, Choi, Sun Hee, Yang, O Bong, Lee, Jae Sung, Lee, Kyung Hee, Kim, Young Gul
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container_issue 2
container_start_page 790
container_title Journal of Catalysis
container_volume 161
creator Chul Choi, Hyun
Choi, Sun Hee
Yang, O Bong
Lee, Jae Sung
Lee, Kyung Hee
Kim, Young Gul
description Hydrodechlorination of carbon tetrachloride (CCl4) has been studied at various reaction temperatures, mole ratios (H2/CCl4), and WHSVs over 1% Pt/MgO. The main factors determining conversion of CCl4and deactivation of the catalyst were reaction temperature and H2/CCl4mole ratio. The optimum reaction conditions for obtaining stable and high conversions of CCl4above 90% were the reaction temperature of 413 K, H2/CCl4mole ratio of 9, and WHSV of 9000 liters/kg/h. The surface area of catalyst decreased due to phase change of MgO to MgCl2·xH2O during reaction. Relative to fresh catalyst, the amounts of carbon and chlorine increased and that of oxygen decreased in used catalyst, especially in deactivated catalyst. The catalyst used for the steady-state reaction did not chemisorb H2at room temperature, but chemisorbed nearly the same amounts of H2as those observed for the fresh catalyst at 373 K. From the XPS and XAFS measurements the active phase of Pt during hydrodechlorination appeared to be a surface Pt(II) species with Cl ligands, while the bulk remained as Pt metal.
doi_str_mv 10.1006/jcat.1996.0242
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The main factors determining conversion of CCl4and deactivation of the catalyst were reaction temperature and H2/CCl4mole ratio. The optimum reaction conditions for obtaining stable and high conversions of CCl4above 90% were the reaction temperature of 413 K, H2/CCl4mole ratio of 9, and WHSV of 9000 liters/kg/h. The surface area of catalyst decreased due to phase change of MgO to MgCl2·xH2O during reaction. Relative to fresh catalyst, the amounts of carbon and chlorine increased and that of oxygen decreased in used catalyst, especially in deactivated catalyst. The catalyst used for the steady-state reaction did not chemisorb H2at room temperature, but chemisorbed nearly the same amounts of H2as those observed for the fresh catalyst at 373 K. 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The main factors determining conversion of CCl4and deactivation of the catalyst were reaction temperature and H2/CCl4mole ratio. The optimum reaction conditions for obtaining stable and high conversions of CCl4above 90% were the reaction temperature of 413 K, H2/CCl4mole ratio of 9, and WHSV of 9000 liters/kg/h. The surface area of catalyst decreased due to phase change of MgO to MgCl2·xH2O during reaction. Relative to fresh catalyst, the amounts of carbon and chlorine increased and that of oxygen decreased in used catalyst, especially in deactivated catalyst. The catalyst used for the steady-state reaction did not chemisorb H2at room temperature, but chemisorbed nearly the same amounts of H2as those observed for the fresh catalyst at 373 K. 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The main factors determining conversion of CCl4and deactivation of the catalyst were reaction temperature and H2/CCl4mole ratio. The optimum reaction conditions for obtaining stable and high conversions of CCl4above 90% were the reaction temperature of 413 K, H2/CCl4mole ratio of 9, and WHSV of 9000 liters/kg/h. The surface area of catalyst decreased due to phase change of MgO to MgCl2·xH2O during reaction. Relative to fresh catalyst, the amounts of carbon and chlorine increased and that of oxygen decreased in used catalyst, especially in deactivated catalyst. The catalyst used for the steady-state reaction did not chemisorb H2at room temperature, but chemisorbed nearly the same amounts of H2as those observed for the fresh catalyst at 373 K. From the XPS and XAFS measurements the active phase of Pt during hydrodechlorination appeared to be a surface Pt(II) species with Cl ligands, while the bulk remained as Pt metal.</abstract><cop>Amsterdam</cop><pub>Elsevier Inc</pub><doi>10.1006/jcat.1996.0242</doi><tpages>8</tpages></addata></record>
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subjects 40 CHEMISTRY
CARBON TETRACHLORIDE
Catalysis
CATALYST SUPPORTS
CATALYSTS
CATALYTIC EFFECTS
Catalytic reactions
Chemistry
DECHLORINATION
Exact sciences and technology
General and physical chemistry
HYDROGENATION
MAGNESIUM OXIDES
PHOTOELECTRON SPECTROSCOPY
PLATINUM
Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry
title Hydrodechlorination of Carbon Tetrachloride over Pt/MgO
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