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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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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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 &lt;FORM:0931633/III/1&gt; where X is -OH or NH2, each R is hydrogen or a lower alkyl radical, and Y is X, &lt;FORM:0931633/III/2&gt;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 &lt;FORM:0931633/IV(a)/1&gt; where X is -OH or -NH2, R is -H or an alkyl radical containing 1-4 carbon atoms, and Y is X, &lt;FORM:0931633/IV(a)/2&gt; , or &lt;FORM:0931633/IV(a)/3&gt; 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&amp;date=19641013&amp;DB=EPODOC&amp;CC=US&amp;NR=3152998A$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,776,881,25542,76516</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&amp;date=19641013&amp;DB=EPODOC&amp;CC=US&amp;NR=3152998A$$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 &lt;FORM:0931633/III/1&gt; where X is -OH or NH2, each R is hydrogen or a lower alkyl radical, and Y is X, &lt;FORM:0931633/III/2&gt;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 &lt;FORM:0931633/IV(a)/1&gt; where X is -OH or -NH2, R is -H or an alkyl radical containing 1-4 carbon atoms, and Y is X, &lt;FORM:0931633/IV(a)/2&gt; , or &lt;FORM:0931633/IV(a)/3&gt; 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. 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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 &lt;FORM:0931633/III/1&gt; where X is -OH or NH2, each R is hydrogen or a lower alkyl radical, and Y is X, &lt;FORM:0931633/III/2&gt;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 &lt;FORM:0931633/IV(a)/1&gt; where X is -OH or -NH2, R is -H or an alkyl radical containing 1-4 carbon atoms, and Y is X, &lt;FORM:0931633/IV(a)/2&gt; , or &lt;FORM:0931633/IV(a)/3&gt; 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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