CS261061B1 - A method for treating mixed cobalt oxide - Google Patents

A method for treating mixed cobalt oxide Download PDF

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CS261061B1
CS261061B1 CS867209A CS720986A CS261061B1 CS 261061 B1 CS261061 B1 CS 261061B1 CS 867209 A CS867209 A CS 867209A CS 720986 A CS720986 A CS 720986A CS 261061 B1 CS261061 B1 CS 261061B1
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Czechoslovakia
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cobalt
oxide
mixed
cobalt oxide
mixed cobalt
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CS867209A
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Czech (cs)
Slovak (sk)
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CS720986A1 (en
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Ondrej Jurovcak
Viktor Berezny
Jozef Lelko
Jan Ferencik
Paulina Baladova
Jozef Micak
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Ondrej Jurovcak
Viktor Berezny
Jozef Lelko
Jan Ferencik
Paulina Baladova
Jozef Micak
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Application filed by Ondrej Jurovcak, Viktor Berezny, Jozef Lelko, Jan Ferencik, Paulina Baladova, Jozef Micak filed Critical Ondrej Jurovcak
Priority to CS867209A priority Critical patent/CS261061B1/en
Publication of CS720986A1 publication Critical patent/CS720986A1/en
Publication of CS261061B1 publication Critical patent/CS261061B1/en

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Abstract

Spůsob spracovania zmesného oxidu kobaltu CO3O4 získaného z odpadov obsahujúcich kobalt, tvoriacich sa v procese výroby cyklohenónu rieši efektívne využitie drahého kovu. Zo zmesného oxidu kobaltu sa připravuje nosič katalyzátora oxidácie čpavku na oxid dusnatý.The method of processing mixed cobalt oxide CO3O4 obtained from cobalt-containing wastes formed in the cyclohenone production process solves the efficient use of the precious metal. The mixed cobalt oxide is used to prepare a catalyst carrier for the oxidation of ammonia to nitric oxide.

Description

Vynález sa týká sposobu spracovania zmesného oxidu kobaltu CO3O4 získaného z kalov obsahujúcich kobalt, tvoriacich sa v procese oxidácie cyklohexánu za použitia oxidačného katalyzátora na báze kobaltu.The invention relates to a process for the treatment of mixed cobalt oxide CO 3 O 4 obtained from cobalt-containing sludges formed in the cyclohexane oxidation process using a cobalt-based oxidation catalyst.

Pre selektívnu oxidáciu čpavku na oxid dusnatý, resp. pri výrobě kyseliny dusičnéj sa v poslednom čase s obfubou používajú katalyzátory na báze oxidov kobaltu. Tieto katalyzátory sú charakteristické vysokou mechanickou pevnosťou a životnosťou. Vyrábajú sa vytvořením katalyticky aktívnej vrstvy na nosičoch tvořených spinelovými zlúčeninami oxidov kobaltu a hliníka AO 177 220, AO 173 274. Použitie zmesného oxidu kobaltu CO3O4 na výrobu nosiča katalyzátora je potřebné, z důvodu dosiahnutia už vyššie spomínaných vlastností katalyzátora.For the selective oxidation of ammonia to nitric oxide, respectively. cobalt oxides catalysts have recently been used in the manufacture of nitric acid. These catalysts are characterized by high mechanical strength and durability. They are made by forming a catalytically active layer on cobalt-aluminum spinel compounds AO 177 220, AO 173 274. The use of mixed cobalt oxide CO 3 O 4 for the production of a catalyst support is required in order to achieve the above-mentioned catalyst properties.

Na výrobu nosiča sa používá CO3O4 získaný náročnými technologickými postupmi ako je spalovanie kovového kobaltu v atmosféře kyslíka, tepelným rozkladom dehydratovaného dusičnanu kobaltnatého AO 242 223.The carrier is produced using CO3O4 obtained by sophisticated technological processes such as the combustion of metallic cobalt in an oxygen atmosphere, by thermal decomposition of dehydrated cobalt nitrate AO 242 223.

Náhradou takto vyrobeného CO3O4 používaného pre výrobu nosiča katalyzátora za CO3O4 získaný z odpadov obsahujúcich kobalt v procese výroby cyklohexanonu je podstatné zjednodušená a zefektivněná výroba nosiča, ktorý má hlavně vplyv na mechanickú pevnost katalyzátora, resp. jeho životnost.Substituting the CO 3 O 4 thus used for the production of the catalyst support with CO 3 O 4 obtained from cobalt-containing wastes in the cyclohexanone production process is a substantially simplified and streamlined production of the support, which mainly affects the mechanical strength of the catalyst, respectively. its lifetime.

Vynález rieši sposob spracovania zmesného oxidu kobaltu CO3O4 získaného z kalov obsahujúcich kobalt, tvoriacich sa v procese oxidácie cyklohexánu za použitia oxidačného katalyzátora na báze kobaltu a je charakteristický tým, že zmesný oxid obsahujúci 0,001 až 2 % niklu, 0,001 až 2 % sodíka a maximálně po 1 % hmotnostnom vápnika, horčíka, kremíka a chrómu sa dezintegruje na částice velkosti 0,004 až 0,4 mm, s výhodou 0,01 až 0,04 mm a zapracuje do nosiča katalyzátora oxidácie čpavku na oxid dusnatý v množstve odpovedajúcom obsahu zmesného oxidu kobaltu v nosiči 5 až 60 % hmotnostných.The present invention provides a process for the treatment of mixed cobalt oxide CO 3 O 4 obtained from cobalt-containing sludges formed in the cyclohexane oxidation process using a cobalt-based oxidation catalyst and characterized in that the mixed oxide containing 0.001 to 2% nickel, 0.001 to 2% sodium and 1% by weight of calcium, magnesium, silicon and chromium is disintegrated to particles of 0.004-0.4 mm, preferably 0.01-0.04 mm, and incorporated into an ammonia to nitric oxide oxidation catalyst carrier in an amount corresponding to the content of mixed cobalt oxide in the 5 to 60% by weight.

Výhodou tohto vynálezu je efektívne využitie zmesného oxidu kobaltu získaného z odpadu. Pri zjednodušení a zefektivnění výroby nosiča katalyzátora oxidácie čpavku na oxid dusnatý sa zachovávajú jeho potřebné vlastnosti.An advantage of the present invention is the efficient use of mixed cobalt oxide obtained from waste. The simplified and more efficient production of the ammonia to nitric oxide catalyst support retains its required properties.

Spůsob spracovania zmesného oxidu na výrobu nosiča katalyzátora oxidácie čpavku je podrobné ilustrovaný v nasledujúcich príkladoch.The process of treating the mixed oxide to produce the ammonia oxidation catalyst support is illustrated in detail in the following examples.

Příklad 1Example 1

Na přípravu nosiča katalyzátora sa použije 50 dielov hmotnostných zmesného oxidu kobaltu získaného z odpadov výroby cyklohexanónu a obsaujúceho 1,3 diela železa, po jednom diele niklu a sodíka, 48 dielov oxidu hlinitého a 2 diely oxidu titaničitého, ktoré sa zhomogenizujú a po použití známých přísad lisováním vytvárajú do žiadaného tvaru nosiča katalyzátora.50 parts by weight of mixed cobalt oxide obtained from cyclohexanone production wastes and containing 1.3 parts of iron, one part of nickel and sodium, 48 parts of alumina and 2 parts of titanium dioxide to be homogenized and using known additives are used to prepare the catalyst support. molding to form the desired catalyst support.

Příklad 2Example 2

Na přípravu nosiča katalyzátora sa použije 25 dielov CO3O4 připraveného z dusičnanu kobaltnatého a 25 dielov zmesného oxidu získaného z odpadov výroby cyklohexanónu obsahujúceho 1,5 dielu železa a po 0,1 diele niklu, chrómu, horčíka a vápnika, 48 dielov oxidu hliníka a 2 diely oxidu titaničitého. Po homogenizácii takto získanej zmesi, následovnom tvarovaní a vypálení dostaneme nosič katalyzátora s obsahom 48 % hmotnostných C0304 vhodný pre dalšie spracovanie na výrobu katalyzátora.25 parts of CO 3 O 4 prepared from cobalt nitrate and 25 parts of mixed oxide obtained from cyclohexanone production wastes containing 1.5 parts of iron and 0.1 parts of nickel, chromium, magnesium and calcium, 48 parts of aluminum oxide and 2 parts are used to prepare the catalyst support. titanium dioxide. After homogenization of the thus obtained mixture, subsequent shaping and firing, a catalyst support with a content of 48% by weight of C0304 is suitable for further processing to produce the catalyst.

Claims (1)

Spůsob spracovania zmesného oxidu kobaltu CO3O4 získaného z kalov obsahujúcich kobalt, tvoriacich sa v procese oxidácie cyklohexánu za použitia oxidačného katalyzátora na báze kobaltu - vyznačujúci sa tým, že zmesný oxid s obsahom železa 0,01 až 6 %, niklu 0,001 až 2 %, sodíka 0,001 až 2 °/o, vápnika, horčíka, kremíka, chrómuProcess for the treatment of mixed cobalt oxide CO3O4 obtained from cobalt-containing sludges formed in the cyclohexane oxidation process using a cobalt-based oxidation catalyst - characterized in that the mixed oxide with an iron content of 0.01-6%, nickel 0.001-2%, sodium 0.001 to 2%, calcium, magnesium, silicon, chromium YNÁLEZU maximálně po 1 % hmotnostnom sa dezintegruje na částice velkosti 0,004 až 0,4 mm, s výhodou 0,01 až 0,04 mm, a zapracuje do nosiča katalyzátora oxidácie čpavku na oxid dusnatý v množstve odpovedajúcom obsahu zmesného oxidu kobaltu v nosciči 5 až 60 °/o hmotnostných.The invention is disintegrated to a particle size of 0.004 to 0.4 mm, preferably 0.01 to 0.04 mm, and incorporated into an ammonia to nitric oxide oxidation catalyst carrier in an amount corresponding to a content of mixed cobalt oxide in the carrier of 5 to 10%. 60% by weight.
CS867209A 1986-10-06 1986-10-06 A method for treating mixed cobalt oxide CS261061B1 (en)

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CS867209A CS261061B1 (en) 1986-10-06 1986-10-06 A method for treating mixed cobalt oxide

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CS261061B1 true CS261061B1 (en) 1989-01-12

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