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The effect of catalyst preparation on the performance of alumina-supported ruthenium catalysts: I. The impact of catalytic precursor on particle size and catalytic activity
The effect of preparation method and the choice of metallic precursor on the performance of a series of Ru Al 2O 3 catalysts were studied. Wet impregnation and incipient wetness were the methods employed; ruthenium nitrosylnitrate and ruthenium trichloride were the reagents. In the latter case, eith...
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Published in: | Journal of catalysis 1989-07, Vol.118 (1), p.203-217 |
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creator | Mieth, Jeffrey A. Schwarz, James A. |
description | The effect of preparation method and the choice of metallic precursor on the performance of a series of
Ru
Al
2O
3
catalysts were studied. Wet impregnation and incipient wetness were the methods employed; ruthenium nitrosylnitrate and ruthenium trichloride were the reagents. In the latter case, either
Ru(III)
Ru(IV)
chlorospecies or mixtures of Ru(II) hydrazine complexes were the catalytic precursors. The series of
Ru
Al
2O
3
catalysts, with metal loadings from 0.7–5% by weight, were subjected to a battery of performance tests: CO temperature-programmed reaction, steadystate CO hydrogenation, and temperature-programmed surface reaction. The methanation activity and carbon deposited during steady-state reaction varied systematically with the dispersion of Ru on the alumina. High rates of methane production were found on catalysts containing a large reservoir of carbon-containing reaction intermediates. The performance of these catalysts depended on the precursor used in their preparation. The effects of weight loading, method of preparation, and variations in the impregnant pH were small within a group prepared from a Common precursor. |
doi_str_mv | 10.1016/0021-9517(89)90311-4 |
format | article |
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Ru
Al
2O
3
catalysts were studied. Wet impregnation and incipient wetness were the methods employed; ruthenium nitrosylnitrate and ruthenium trichloride were the reagents. In the latter case, either
Ru(III)
Ru(IV)
chlorospecies or mixtures of Ru(II) hydrazine complexes were the catalytic precursors. The series of
Ru
Al
2O
3
catalysts, with metal loadings from 0.7–5% by weight, were subjected to a battery of performance tests: CO temperature-programmed reaction, steadystate CO hydrogenation, and temperature-programmed surface reaction. The methanation activity and carbon deposited during steady-state reaction varied systematically with the dispersion of Ru on the alumina. High rates of methane production were found on catalysts containing a large reservoir of carbon-containing reaction intermediates. The performance of these catalysts depended on the precursor used in their preparation. The effects of weight loading, method of preparation, and variations in the impregnant pH were small within a group prepared from a Common precursor.</description><identifier>ISSN: 0021-9517</identifier><identifier>EISSN: 1090-2694</identifier><identifier>DOI: 10.1016/0021-9517(89)90311-4</identifier><identifier>CODEN: JCTLA5</identifier><language>eng</language><publisher>Amsterdam: Elsevier Inc</publisher><subject>01 COAL, LIGNITE, AND PEAT ; 010408 - Coal, Lignite, & Peat- C1 Processes- (1987-) ; ALKANES ; ALUMINIUM COMPOUNDS ; ALUMINIUM OXIDES ; CARBON COMPOUNDS ; CARBON MONOXIDE ; CARBON OXIDES ; CATALYST SUPPORTS ; CATALYSTS ; CATALYTIC EFFECTS ; CHALCOGENIDES ; CHEMICAL PREPARATION ; CHEMICAL REACTIONS ; Chemistry ; COMPARATIVE EVALUATIONS ; COMPLEXES ; CONTROL ; ELEMENTS ; Exact sciences and technology ; FISCHER-TROPSCH SYNTHESIS ; General and physical chemistry ; HYDROCARBONS ; HYDROGENATION ; IMPREGNATION ; METALS ; METHANATION ; METHANE ; ORGANIC COMPOUNDS ; OXIDES ; OXYGEN COMPOUNDS ; PARTICLE SIZE ; PH VALUE ; PLATINUM METALS ; RUTHENIUM ; RUTHENIUM COMPLEXES ; SIZE ; SYNTHESIS ; TEMPERATURE CONTROL ; Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry ; TRANSITION ELEMENT COMPLEXES ; TRANSITION ELEMENTS</subject><ispartof>Journal of catalysis, 1989-07, Vol.118 (1), p.203-217</ispartof><rights>1989</rights><rights>1990 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c277t-bba80d3d56050c73587fcac3c16e655341a2b38e4ee37f44494cd34df02f34553</citedby></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://www.sciencedirect.com/science/article/pii/0021951789903114$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>230,314,776,780,881,3387,27901,27902,45958</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=6597638$$DView record in Pascal Francis$$Hfree_for_read</backlink><backlink>$$Uhttps://www.osti.gov/biblio/7161132$$D View this record in Osti.gov$$Hfree_for_read</backlink></links><search><creatorcontrib>Mieth, Jeffrey A.</creatorcontrib><creatorcontrib>Schwarz, James A.</creatorcontrib><title>The effect of catalyst preparation on the performance of alumina-supported ruthenium catalysts: I. The impact of catalytic precursor on particle size and catalytic activity</title><title>Journal of catalysis</title><description>The effect of preparation method and the choice of metallic precursor on the performance of a series of
Ru
Al
2O
3
catalysts were studied. Wet impregnation and incipient wetness were the methods employed; ruthenium nitrosylnitrate and ruthenium trichloride were the reagents. In the latter case, either
Ru(III)
Ru(IV)
chlorospecies or mixtures of Ru(II) hydrazine complexes were the catalytic precursors. The series of
Ru
Al
2O
3
catalysts, with metal loadings from 0.7–5% by weight, were subjected to a battery of performance tests: CO temperature-programmed reaction, steadystate CO hydrogenation, and temperature-programmed surface reaction. The methanation activity and carbon deposited during steady-state reaction varied systematically with the dispersion of Ru on the alumina. High rates of methane production were found on catalysts containing a large reservoir of carbon-containing reaction intermediates. The performance of these catalysts depended on the precursor used in their preparation. The effects of weight loading, method of preparation, and variations in the impregnant pH were small within a group prepared from a Common precursor.</description><subject>01 COAL, LIGNITE, AND PEAT</subject><subject>010408 - Coal, Lignite, & Peat- C1 Processes- (1987-)</subject><subject>ALKANES</subject><subject>ALUMINIUM COMPOUNDS</subject><subject>ALUMINIUM OXIDES</subject><subject>CARBON COMPOUNDS</subject><subject>CARBON MONOXIDE</subject><subject>CARBON OXIDES</subject><subject>CATALYST SUPPORTS</subject><subject>CATALYSTS</subject><subject>CATALYTIC EFFECTS</subject><subject>CHALCOGENIDES</subject><subject>CHEMICAL PREPARATION</subject><subject>CHEMICAL REACTIONS</subject><subject>Chemistry</subject><subject>COMPARATIVE EVALUATIONS</subject><subject>COMPLEXES</subject><subject>CONTROL</subject><subject>ELEMENTS</subject><subject>Exact sciences and technology</subject><subject>FISCHER-TROPSCH SYNTHESIS</subject><subject>General and physical chemistry</subject><subject>HYDROCARBONS</subject><subject>HYDROGENATION</subject><subject>IMPREGNATION</subject><subject>METALS</subject><subject>METHANATION</subject><subject>METHANE</subject><subject>ORGANIC COMPOUNDS</subject><subject>OXIDES</subject><subject>OXYGEN COMPOUNDS</subject><subject>PARTICLE SIZE</subject><subject>PH VALUE</subject><subject>PLATINUM METALS</subject><subject>RUTHENIUM</subject><subject>RUTHENIUM COMPLEXES</subject><subject>SIZE</subject><subject>SYNTHESIS</subject><subject>TEMPERATURE CONTROL</subject><subject>Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry</subject><subject>TRANSITION ELEMENT COMPLEXES</subject><subject>TRANSITION ELEMENTS</subject><issn>0021-9517</issn><issn>1090-2694</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>1989</creationdate><recordtype>article</recordtype><recordid>eNp9kctKBDEQRYMoOD7-wEUQF7poTTpJP1wIIr5AcKPrkElXMNLdaZK0MH6TH2niyOBKKAgU59at3ELoiJJzSmh1QUhJi1bQ-rRpz1rCKC34FlpQ0pKirFq-jRYbZBfthfBOCKVCNAv09fIGGIwBHbEzWKuo-lWIePIwKa-idSNOFRM1gTfOD2rUkFHVz4MdVRHmaXI-Qof9nLDRzsNmTLjEj-c4W9hhUn8totXZQ88-OJ8dklvq9YCD_QSsxu4PmJT2w8bVAdoxqg9w-Pvuo9e725ebh-Lp-f7x5vqp0GVdx2K5VA3pWCcqIoiumWhqo5VmmlZQCcE4VeWSNcABWG045y3XHeOdIaVhPAH76Hg914VoZdA2gn7TbhxTSrKmFaWsTBBfQ9q7EDwYOXk7KL-SlMh8Fpkzlzlz2bTy5yySJ9nJWjapoFVvfMrTho22Em1dsSZhV2sM0j8_LPi8BqToO-vzFp2z__t8A1OIpIk</recordid><startdate>19890701</startdate><enddate>19890701</enddate><creator>Mieth, Jeffrey A.</creator><creator>Schwarz, James A.</creator><general>Elsevier Inc</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>OTOTI</scope></search><sort><creationdate>19890701</creationdate><title>The effect of catalyst preparation on the performance of alumina-supported ruthenium catalysts: I. The impact of catalytic precursor on particle size and catalytic activity</title><author>Mieth, Jeffrey A. ; Schwarz, James A.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c277t-bba80d3d56050c73587fcac3c16e655341a2b38e4ee37f44494cd34df02f34553</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>1989</creationdate><topic>01 COAL, LIGNITE, AND PEAT</topic><topic>010408 - Coal, Lignite, & Peat- C1 Processes- (1987-)</topic><topic>ALKANES</topic><topic>ALUMINIUM COMPOUNDS</topic><topic>ALUMINIUM OXIDES</topic><topic>CARBON COMPOUNDS</topic><topic>CARBON MONOXIDE</topic><topic>CARBON OXIDES</topic><topic>CATALYST SUPPORTS</topic><topic>CATALYSTS</topic><topic>CATALYTIC EFFECTS</topic><topic>CHALCOGENIDES</topic><topic>CHEMICAL PREPARATION</topic><topic>CHEMICAL REACTIONS</topic><topic>Chemistry</topic><topic>COMPARATIVE EVALUATIONS</topic><topic>COMPLEXES</topic><topic>CONTROL</topic><topic>ELEMENTS</topic><topic>Exact sciences and technology</topic><topic>FISCHER-TROPSCH SYNTHESIS</topic><topic>General and physical chemistry</topic><topic>HYDROCARBONS</topic><topic>HYDROGENATION</topic><topic>IMPREGNATION</topic><topic>METALS</topic><topic>METHANATION</topic><topic>METHANE</topic><topic>ORGANIC COMPOUNDS</topic><topic>OXIDES</topic><topic>OXYGEN COMPOUNDS</topic><topic>PARTICLE SIZE</topic><topic>PH VALUE</topic><topic>PLATINUM METALS</topic><topic>RUTHENIUM</topic><topic>RUTHENIUM COMPLEXES</topic><topic>SIZE</topic><topic>SYNTHESIS</topic><topic>TEMPERATURE CONTROL</topic><topic>Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry</topic><topic>TRANSITION ELEMENT COMPLEXES</topic><topic>TRANSITION ELEMENTS</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Mieth, Jeffrey A.</creatorcontrib><creatorcontrib>Schwarz, James A.</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>OSTI.GOV</collection><jtitle>Journal of catalysis</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Mieth, Jeffrey A.</au><au>Schwarz, James A.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>The effect of catalyst preparation on the performance of alumina-supported ruthenium catalysts: I. The impact of catalytic precursor on particle size and catalytic activity</atitle><jtitle>Journal of catalysis</jtitle><date>1989-07-01</date><risdate>1989</risdate><volume>118</volume><issue>1</issue><spage>203</spage><epage>217</epage><pages>203-217</pages><issn>0021-9517</issn><eissn>1090-2694</eissn><coden>JCTLA5</coden><abstract>The effect of preparation method and the choice of metallic precursor on the performance of a series of
Ru
Al
2O
3
catalysts were studied. Wet impregnation and incipient wetness were the methods employed; ruthenium nitrosylnitrate and ruthenium trichloride were the reagents. In the latter case, either
Ru(III)
Ru(IV)
chlorospecies or mixtures of Ru(II) hydrazine complexes were the catalytic precursors. The series of
Ru
Al
2O
3
catalysts, with metal loadings from 0.7–5% by weight, were subjected to a battery of performance tests: CO temperature-programmed reaction, steadystate CO hydrogenation, and temperature-programmed surface reaction. The methanation activity and carbon deposited during steady-state reaction varied systematically with the dispersion of Ru on the alumina. High rates of methane production were found on catalysts containing a large reservoir of carbon-containing reaction intermediates. The performance of these catalysts depended on the precursor used in their preparation. The effects of weight loading, method of preparation, and variations in the impregnant pH were small within a group prepared from a Common precursor.</abstract><cop>Amsterdam</cop><pub>Elsevier Inc</pub><doi>10.1016/0021-9517(89)90311-4</doi><tpages>15</tpages></addata></record> |
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subjects | 01 COAL, LIGNITE, AND PEAT 010408 - Coal, Lignite, & Peat- C1 Processes- (1987-) ALKANES ALUMINIUM COMPOUNDS ALUMINIUM OXIDES CARBON COMPOUNDS CARBON MONOXIDE CARBON OXIDES CATALYST SUPPORTS CATALYSTS CATALYTIC EFFECTS CHALCOGENIDES CHEMICAL PREPARATION CHEMICAL REACTIONS Chemistry COMPARATIVE EVALUATIONS COMPLEXES CONTROL ELEMENTS Exact sciences and technology FISCHER-TROPSCH SYNTHESIS General and physical chemistry HYDROCARBONS HYDROGENATION IMPREGNATION METALS METHANATION METHANE ORGANIC COMPOUNDS OXIDES OXYGEN COMPOUNDS PARTICLE SIZE PH VALUE PLATINUM METALS RUTHENIUM RUTHENIUM COMPLEXES SIZE SYNTHESIS TEMPERATURE CONTROL Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry TRANSITION ELEMENT COMPLEXES TRANSITION ELEMENTS |
title | The effect of catalyst preparation on the performance of alumina-supported ruthenium catalysts: I. The impact of catalytic precursor on particle size and catalytic activity |
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