Nickel-copper-chromia catalyst and the preparation thereof
A physically-stable performed catalytic composition resistant to softening by water, ammonia or mixtures thereof, comprises, on an oxidefree basis, 60-85 mole per cent of nickel, 14-37 mole per cent of copper and 1-5 mole per cent of chromium. The composition contains at least 30% by weight of reduc...
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creator | MOSS PHILIP H |
description | A physically-stable performed catalytic composition resistant to softening by water, ammonia or mixtures thereof, comprises, on an oxidefree basis, 60-85 mole per cent of nickel, 14-37 mole per cent of copper and 1-5 mole per cent of chromium. The composition contains at least 30% by weight of reduced nickel. The catalyst is produced by compressing or extruding into pellets a finely-divided mixture of the metal oxides, prepared according to known methods, in the required proportions with or without a dye lubricant, and passing hydrogen over or through the mixture at 250 DEG -400 DEG C. preferably 300 DEG -320 DEG C., until the weight per cent of metallic nickel therein is at least 30, preferably at least 35%. The catalyst is used to prepare heterocyclic nitrogen compounds, e.g. piperazine, morpholine and C- alkyl derivatives thereof. In the continuous preparation of such compounds, ammonia, with or without water or hydrogen, is passed over the catalyst at, e.g. 150 DEG -400 DEG C. and super-atmosphere pressure, together with compounds of formula where X is -OH or NH2, each R is hydrogen or a lower alkyl radical, and Y is X, ALSO:Heterocyclic nitrogen compounds, e.g. piperazine, morpholine and C-alkyl derivatives thereof are made by passing ammonia with or without water or hydrogen over a hydrogenation catalyst at raised temperature and superatmospheric pressure, together with compounds of formula where X is -OH or -NH2, R is -H or an alkyl radical containing 1-4 carbon atoms, and Y is X, , or In the preferred process, the temperature is 150-400 DEG C., hydrogen is used, and the proportion of ammonia is in excess of said compound in a mole ratio of up to 5:1. The catalyst (Group III) comprises, on an oxide-free basis, 60-85 mole per cent of nickel, 14-37 mole per cent of copper, 1-5 mole per cent of chromium, and contains at least 30% by weight of metallic nickel. Specified reactants which may be employed with ammonia are ethylene glycol, propylene glycol, diethylene glycol, dipropylene glycol, ethanolamine, diethanolamine, ethylenediamine, propylenediamine, isopropanolamine, 2-amino-propan-1-ol, 2,3-butylene glycol and 2-amino-3-hydroxy-butane. |
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fullrecord | <record><control><sourceid>epo_EVB</sourceid><recordid>TN_cdi_epo_espacenet_US3152998A</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>US3152998A</sourcerecordid><originalsourceid>FETCH-epo_espacenet_US3152998A3</originalsourceid><addsrcrecordid>eNrjZLDyy0zOTs3RTc4vKEgt0k3OKMrPzUxUSE4sScypLC5RSMxLUSjJSFUoKEotSCxKLMnMzwPxi1Lz03gYWNMSc4pTeaE0N4O8m2uIs4duakF-fGpxQWJyal5qSXxosLGhqZGlpYWjMWEVAOCfLrw</addsrcrecordid><sourcetype>Open Access Repository</sourcetype><iscdi>true</iscdi><recordtype>patent</recordtype></control><display><type>patent</type><title>Nickel-copper-chromia catalyst and the preparation thereof</title><source>esp@cenet</source><creator>MOSS PHILIP H</creator><creatorcontrib>MOSS PHILIP H</creatorcontrib><description>A physically-stable performed catalytic composition resistant to softening by water, ammonia or mixtures thereof, comprises, on an oxidefree basis, 60-85 mole per cent of nickel, 14-37 mole per cent of copper and 1-5 mole per cent of chromium. The composition contains at least 30% by weight of reduced nickel. The catalyst is produced by compressing or extruding into pellets a finely-divided mixture of the metal oxides, prepared according to known methods, in the required proportions with or without a dye lubricant, and passing hydrogen over or through the mixture at 250 DEG -400 DEG C. preferably 300 DEG -320 DEG C., until the weight per cent of metallic nickel therein is at least 30, preferably at least 35%. The catalyst is used to prepare heterocyclic nitrogen compounds, e.g. piperazine, morpholine and C- alkyl derivatives thereof. In the continuous preparation of such compounds, ammonia, with or without water or hydrogen, is passed over the catalyst at, e.g. 150 DEG -400 DEG C. and super-atmosphere pressure, together with compounds of formula <FORM:0931633/III/1> where X is -OH or NH2, each R is hydrogen or a lower alkyl radical, and Y is X, <FORM:0931633/III/2>ALSO:Heterocyclic nitrogen compounds, e.g. piperazine, morpholine and C-alkyl derivatives thereof are made by passing ammonia with or without water or hydrogen over a hydrogenation catalyst at raised temperature and superatmospheric pressure, together with compounds of formula <FORM:0931633/IV(a)/1> where X is -OH or -NH2, R is -H or an alkyl radical containing 1-4 carbon atoms, and Y is X, <FORM:0931633/IV(a)/2> , or <FORM:0931633/IV(a)/3> In the preferred process, the temperature is 150-400 DEG C., hydrogen is used, and the proportion of ammonia is in excess of said compound in a mole ratio of up to 5:1. The catalyst (Group III) comprises, on an oxide-free basis, 60-85 mole per cent of nickel, 14-37 mole per cent of copper, 1-5 mole per cent of chromium, and contains at least 30% by weight of metallic nickel. Specified reactants which may be employed with ammonia are ethylene glycol, propylene glycol, diethylene glycol, dipropylene glycol, ethanolamine, diethanolamine, ethylenediamine, propylenediamine, isopropanolamine, 2-amino-propan-1-ol, 2,3-butylene glycol and 2-amino-3-hydroxy-butane.</description><language>eng</language><subject>CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY ; CHEMISTRY ; HETEROCYCLIC COMPOUNDS ; METALLURGY ; ORGANIC CHEMISTRY ; PERFORMING OPERATIONS ; PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL ; THEIR RELEVANT APPARATUS ; TRANSPORTING</subject><creationdate>1964</creationdate><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=19641013&DB=EPODOC&CC=US&NR=3152998A$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,776,881,25542,76516</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=19641013&DB=EPODOC&CC=US&NR=3152998A$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>MOSS PHILIP H</creatorcontrib><title>Nickel-copper-chromia catalyst and the preparation thereof</title><description>A physically-stable performed catalytic composition resistant to softening by water, ammonia or mixtures thereof, comprises, on an oxidefree basis, 60-85 mole per cent of nickel, 14-37 mole per cent of copper and 1-5 mole per cent of chromium. The composition contains at least 30% by weight of reduced nickel. The catalyst is produced by compressing or extruding into pellets a finely-divided mixture of the metal oxides, prepared according to known methods, in the required proportions with or without a dye lubricant, and passing hydrogen over or through the mixture at 250 DEG -400 DEG C. preferably 300 DEG -320 DEG C., until the weight per cent of metallic nickel therein is at least 30, preferably at least 35%. The catalyst is used to prepare heterocyclic nitrogen compounds, e.g. piperazine, morpholine and C- alkyl derivatives thereof. In the continuous preparation of such compounds, ammonia, with or without water or hydrogen, is passed over the catalyst at, e.g. 150 DEG -400 DEG C. and super-atmosphere pressure, together with compounds of formula <FORM:0931633/III/1> where X is -OH or NH2, each R is hydrogen or a lower alkyl radical, and Y is X, <FORM:0931633/III/2>ALSO:Heterocyclic nitrogen compounds, e.g. piperazine, morpholine and C-alkyl derivatives thereof are made by passing ammonia with or without water or hydrogen over a hydrogenation catalyst at raised temperature and superatmospheric pressure, together with compounds of formula <FORM:0931633/IV(a)/1> where X is -OH or -NH2, R is -H or an alkyl radical containing 1-4 carbon atoms, and Y is X, <FORM:0931633/IV(a)/2> , or <FORM:0931633/IV(a)/3> In the preferred process, the temperature is 150-400 DEG C., hydrogen is used, and the proportion of ammonia is in excess of said compound in a mole ratio of up to 5:1. The catalyst (Group III) comprises, on an oxide-free basis, 60-85 mole per cent of nickel, 14-37 mole per cent of copper, 1-5 mole per cent of chromium, and contains at least 30% by weight of metallic nickel. Specified reactants which may be employed with ammonia are ethylene glycol, propylene glycol, diethylene glycol, dipropylene glycol, ethanolamine, diethanolamine, ethylenediamine, propylenediamine, isopropanolamine, 2-amino-propan-1-ol, 2,3-butylene glycol and 2-amino-3-hydroxy-butane.</description><subject>CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY</subject><subject>CHEMISTRY</subject><subject>HETEROCYCLIC COMPOUNDS</subject><subject>METALLURGY</subject><subject>ORGANIC CHEMISTRY</subject><subject>PERFORMING OPERATIONS</subject><subject>PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL</subject><subject>THEIR RELEVANT APPARATUS</subject><subject>TRANSPORTING</subject><fulltext>true</fulltext><rsrctype>patent</rsrctype><creationdate>1964</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNrjZLDyy0zOTs3RTc4vKEgt0k3OKMrPzUxUSE4sScypLC5RSMxLUSjJSFUoKEotSCxKLMnMzwPxi1Lz03gYWNMSc4pTeaE0N4O8m2uIs4duakF-fGpxQWJyal5qSXxosLGhqZGlpYWjMWEVAOCfLrw</recordid><startdate>19641013</startdate><enddate>19641013</enddate><creator>MOSS PHILIP H</creator><scope>EVB</scope></search><sort><creationdate>19641013</creationdate><title>Nickel-copper-chromia catalyst and the preparation thereof</title><author>MOSS PHILIP H</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_US3152998A3</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng</language><creationdate>1964</creationdate><topic>CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY</topic><topic>CHEMISTRY</topic><topic>HETEROCYCLIC COMPOUNDS</topic><topic>METALLURGY</topic><topic>ORGANIC CHEMISTRY</topic><topic>PERFORMING OPERATIONS</topic><topic>PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL</topic><topic>THEIR RELEVANT APPARATUS</topic><topic>TRANSPORTING</topic><toplevel>online_resources</toplevel><creatorcontrib>MOSS PHILIP H</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>MOSS PHILIP H</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>Nickel-copper-chromia catalyst and the preparation thereof</title><date>1964-10-13</date><risdate>1964</risdate><abstract>A physically-stable performed catalytic composition resistant to softening by water, ammonia or mixtures thereof, comprises, on an oxidefree basis, 60-85 mole per cent of nickel, 14-37 mole per cent of copper and 1-5 mole per cent of chromium. The composition contains at least 30% by weight of reduced nickel. The catalyst is produced by compressing or extruding into pellets a finely-divided mixture of the metal oxides, prepared according to known methods, in the required proportions with or without a dye lubricant, and passing hydrogen over or through the mixture at 250 DEG -400 DEG C. preferably 300 DEG -320 DEG C., until the weight per cent of metallic nickel therein is at least 30, preferably at least 35%. The catalyst is used to prepare heterocyclic nitrogen compounds, e.g. piperazine, morpholine and C- alkyl derivatives thereof. In the continuous preparation of such compounds, ammonia, with or without water or hydrogen, is passed over the catalyst at, e.g. 150 DEG -400 DEG C. and super-atmosphere pressure, together with compounds of formula <FORM:0931633/III/1> where X is -OH or NH2, each R is hydrogen or a lower alkyl radical, and Y is X, <FORM:0931633/III/2>ALSO:Heterocyclic nitrogen compounds, e.g. piperazine, morpholine and C-alkyl derivatives thereof are made by passing ammonia with or without water or hydrogen over a hydrogenation catalyst at raised temperature and superatmospheric pressure, together with compounds of formula <FORM:0931633/IV(a)/1> where X is -OH or -NH2, R is -H or an alkyl radical containing 1-4 carbon atoms, and Y is X, <FORM:0931633/IV(a)/2> , or <FORM:0931633/IV(a)/3> In the preferred process, the temperature is 150-400 DEG C., hydrogen is used, and the proportion of ammonia is in excess of said compound in a mole ratio of up to 5:1. The catalyst (Group III) comprises, on an oxide-free basis, 60-85 mole per cent of nickel, 14-37 mole per cent of copper, 1-5 mole per cent of chromium, and contains at least 30% by weight of metallic nickel. Specified reactants which may be employed with ammonia are ethylene glycol, propylene glycol, diethylene glycol, dipropylene glycol, ethanolamine, diethanolamine, ethylenediamine, propylenediamine, isopropanolamine, 2-amino-propan-1-ol, 2,3-butylene glycol and 2-amino-3-hydroxy-butane.</abstract><oa>free_for_read</oa></addata></record> |
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subjects | CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY CHEMISTRY HETEROCYCLIC COMPOUNDS METALLURGY ORGANIC CHEMISTRY PERFORMING OPERATIONS PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL THEIR RELEVANT APPARATUS TRANSPORTING |
title | Nickel-copper-chromia catalyst and the preparation thereof |
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