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DE884639C - Recovery of the platinum which evaporates during ammonia combustion - Google Patents

Recovery of the platinum which evaporates during ammonia combustion

Info

Publication number
DE884639C
DE884639C DED5340D DED0005340D DE884639C DE 884639 C DE884639 C DE 884639C DE D5340 D DED5340 D DE D5340D DE D0005340 D DED0005340 D DE D0005340D DE 884639 C DE884639 C DE 884639C
Authority
DE
Germany
Prior art keywords
platinum
gold
alloys
corrosion
silver
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
DED5340D
Other languages
German (de)
Inventor
Hermann Dr Holzmann
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Evonik Operations GmbH
Original Assignee
Degussa GmbH
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Degussa GmbH filed Critical Degussa GmbH
Priority to DED5340D priority Critical patent/DE884639C/en
Application granted granted Critical
Publication of DE884639C publication Critical patent/DE884639C/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B11/00Obtaining noble metals
    • C22B11/02Obtaining noble metals by dry processes
    • C22B11/021Recovery of noble metals from waste materials
    • C22B11/026Recovery of noble metals from waste materials from spent catalysts
    • C22B11/028Recovery of noble metals from waste materials from spent catalysts using solid sorbents, e.g. getters or catchment gauzes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/90Regeneration or reactivation
    • B01J23/96Regeneration or reactivation of catalysts comprising metals, oxides or hydroxides of the noble metals
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B21/00Nitrogen; Compounds thereof
    • C01B21/20Nitrogen oxides; Oxyacids of nitrogen; Salts thereof
    • C01B21/24Nitric oxide (NO)
    • C01B21/26Preparation by catalytic or non-catalytic oxidation of ammonia
    • C01B21/267Means for preventing deterioration or loss of catalyst or for recovering lost catalyst
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/584Recycling of catalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Inorganic Chemistry (AREA)
  • Catalysts (AREA)
  • Filtering Of Dispersed Particles In Gases (AREA)

Description

Wiedergewinnung des bei der Ammoniakverbrennung sich verflüchtigenden Platins Gegenstand des Patents 747 120 ist ein Verfahren zur Wiedergewinnung des bei der Ammoniakverbrennung mit Hilfe von Katalysatoren aus Platin und Platinlegierungen sich verflüchtigenden Platins, darin bestehend, daß die heißen Verbrennungsgase durch eine gasdurchlässige Schicht geführt werden, die Gold in großer Oberfläche und/oder feiner Verteilung enthält. Die gasdurchlässige Schicht kann z. B. aus keramischem Trägermateria:1, wie Röhrchen, Hohlzylindern quadratischen Querschnitts od. dgl. bestehen, die mit einem dünnen, gegebenenfalls porösen Überzug aus Gold versehen sind, Die Ancrdnung der gasdurchlässigen Schicht erfolgt zweckmäßig in einer Temperatur-Zone, bei der leicht Verschweißung des in den Ab- gasen befindlichen feinverteilten Platins mit dem Gold stattfindet. Dies ist z. B. bei Temperaturen von 6oo bis 700' der Fall.Recovery of the platinum which evaporates during ammonia combustion The subject of patent 747 120 is a process for the recovery of the platinum which evaporates during ammonia combustion with the aid of catalysts made from platinum and platinum alloys, in that the hot combustion gases are passed through a gas-permeable layer, the gold contains in a large surface and / or fine distribution. The gas-permeable layer can, for. B. made of ceramic support material: 1, such as tubes, hollow cylinders with a square cross-section or the like, which are provided with a thin, possibly porous coating of gold of the finely divided platinum in the exhaust gas takes place with the gold. This is e.g. B. at temperatures of 600 to 700 ' the case.

Weitere Versuche haben ergeben, daß das Verfahren des genannten Patents auch derart durchgeführt werden kann, daß das Gold zum Teil oder auch ganz durch andere Edelmetalle oder Edeletallegierungen ersetzt ist. Man kann z. B. Platin oder Palladium verwenden, die ebenfalls wie Gold korrosionsbeständig -sind- und nicht oxydieren. Infolge des höheren Schmelzpunktes von Platin und Palladium erfolgt allerdings die V6rschweißung des verflüchtigten Platins weniger leicht. Es ist infolgedessen empfehlenswert, l#e,#--:,.V(#rWendu.ng von Platin und/oder Palladium den Schmelzpunkt dieser Metalle zu erniedrigen, was in einfachster Weise durch Zu-leg'ieren von Gold in den erforderlidhen Mengen geschehen kann.Further tests have shown that the method of the patent mentioned can also be carried out in such a way that the gold is partially or completely through other precious metals or precious metal alloys are replaced. You can z. B. platinum or Use palladium, which is also like gold corrosion resistant -are- and do not oxidize. Due to the higher melting point of platinum and palladium However, the pre-welding of the volatilized platinum is less easy. It is therefore advisable to use l # e, # -:,. V (# rWendu.ng of platinum and / or Palladium to lower the melting point of these metals, what in the simplest way can be done by alloying gold in the required quantities.

Weiterhin wurde gefunden, daß man an Stelle von Gold auch Legierungen, welche Gold, Platin oder Palladium und noch Silber in bestim m-ten Mengenverhältnissen enthalten, mit Vorteil ver,-wenden kann. Da Silber nicht genügend korrosionsfest ist, darf sein Anteil zwecks Erhaltung der Korrosionsfestigkeit dieser Legierungen gewisse Grenzen nicht überschreiten. Gold soll im allgemeinen nicht mehr als etwa 5o, Platin nicht mehr als etwa 6o und Palladium nicht mehr als etwa, 5o Atomprozente Silber enthalten.Furthermore, it has been found that, instead of gold, alloys which contain gold, platinum or palladium and also silver in certain proportions can advantageously be used. Since silver is not sufficiently resistant to corrosion, its proportion must not exceed certain limits in order to maintain the corrosion resistance of these alloys. Gold should generally contain no more than about 50 atomic percent silver, platinum no more than about 60 atomic percent, and palladium no more than about. 50 atomic percent silver.

Palladium ist etwas weniger korroslonsbeständig als Platin und Gold und infolgedessen dem letzteren etwas unterlegen. Das gleiche gilt für Legierungen, die Palladium als Hauptkomponente enthalten. Selbstverständlich können auch Legierungen mit mehr als zwei Komponenten, z. B. Gold#-Platin-Si 1 ber, Gold-Palladium-Silber, Platin-Palladium-Silber, Gold-Platin-Palladium-Silber, verwendet werden.Palladium is somewhat less resistant to corrosion than platinum and gold and is therefore somewhat inferior to the latter. The same applies to alloys that contain palladium as a main component. Of course, alloys with more than two components, e.g. B. Gold # -Platinum-Si 1 ber, gold-palladium-silver, platinum-palladium-silver, gold-platinum-palladium-silver, can be used.

Die erfindungsgemäß anzuwendenden Edelmetalle und Edelmetallegierungen -können auch noch untergeofdnete Mengen von anderen Edelineta-Ii#n, in#b'esondere - solche - der Platingruppe, wie Ruthenium, Osmium, Rhodium, Iridium, einzeln oder zu mehreren, enthalten, Das Aufbringen der hier beanspruchten Edelmetalle oder Edelmetallegierungen auf Träger, wie feine Röhrchen, Hohlzylinder quadratischen Querschnitts oder Sattelkörper aus keramischem Material, kann in gleicher oder ähnlicher Weise wie bei dem Verfahren des Hauptpatentg, erfälgen. Legierungen können auf der Unterlage selbst erzeugt werdm Man kann z. B. zunächst Silber nach Art der (#äa-n-z-versilb-eru-ng- oder durch Kathodenzerstäubung auf die Unterlage aufbringen und äuf die Silbergrundlage einem Deckschicht aus korrosionsbeständigem Metall, z. B. Gold, galvanisch oder auf anderem Wege aufbringen. Durch Erwärmen auf geeignete Temperaturen findet Legierungsbildung durch Ineinanderdiffundieren der vorhandenen Metalle statt. Diese Legierungs-'bildung kann mit Vorteil bei der praktischen Anwendung der Gebilde -stattfinden. Beim Durchgang der Abgase der Ammoniakverbrennung durch die gasdurchlässige Schicht bei Temperaturen von etwa 6oo bis 700' findet die Legierungsbildung selbständig statt.The present invention applied precious metals and precious metal alloys -can also untergeofdnete amounts of other Edelineta-Ii # n, b'esondere in # - such - included such as ruthenium, osmium, rhodium, iridium individually, or more of the platinum group, applying the Noble metals or noble metal alloys claimed here on carriers, such as fine tubes, hollow cylinders with a square cross-section or saddle bodies made of ceramic material, can result in the same or a similar way as in the method of the main patent. Alloys can be produced on the base itself. B. first apply silver to the substrate in the manner of (# äa-nz-versilb-eru-ng- or by cathode sputtering and apply the silver base to a top layer of corrosion-resistant metal, e.g. gold, galvanically or in some other way heating to suitable temperatures will alloying by interdiffusion of the metals instead. This alloy'bildung may with advantage in the practical application of the formations -stattfinden. finds during the passage of the exhaust gases of the combustion of ammonia by the gas-permeable layer at temperatures of about 6oo to 700 ', the Alloy formation takes place independently.

Claims (2)

PATENTANSPRücHE. i. Abänderung des Verfahrens zur Wiedergewinnung des bei der Ammoniak:verbrennung mittels Katalysatoren aus Platin oder Platinlegierungen sich verflüchtigenden Platins durch Leiten der heißen Verhrennungsgase durch oberflächlich Gold enthaltende gasdurchlässige Schichten gemäß Patent 747 i2o, dadurch gekennzeichnet, daß zur Bindung des Platins an Stelle von Gold oder neben Gold andere Edelmetalle, die bei den in Betracht kommenden Temperaturen, z. B. 6oo bis 7000, korrosions-und oxydationsbeständig sind, wie Palladium oder Platin, einzeln oder in Form ihrer Legierungen verwendet werden. PATENT CLAIMS. i. Modification of the process for the recovery of the platinum which is volatilized during ammonia combustion by means of catalysts made of platinum or platinum alloys by guiding the hot combustion gases through gas-permeable layers containing gold on the surface according to patent 747 i2o, characterized in that to bind the platinum in place of gold or in addition to Gold other precious metals that are present at the temperatures in question, e.g. B. 600 to 7000, are corrosion and oxidation resistant, such as palladium or platinum, can be used individually or in the form of their alloys. 2. Verfahren nach Anspruch i, gekennzeichnet durch Anwendung von korrosions- und oxydationsbeständigen Legierungen von Silber mit korrüsionsbeständigen Edelmetallen, wie Gold, Palladium, Silber. 3. Verfahren nach Ansprüchen i und 2, gekennzeichnet durch Anwendung von korrosions-und oxydationsbeständigen Legierungen, die auf den Unterlagen, z. B. keramischen Trägerkörpern, durch getrenntes Aufbringen der Bestandteile und Diffusion durch Wärmewirkung vor oder bei der Anwendung entstanden sind. 4. Verfahren nach Ansprüchen i bis 3, gekennzeichnet durch Anwendung von Legierungen, die dadurch entstanden sind, daß zunächst Silber auf die Trägerkörper aufgebracht,' der Silberüberzug mit einer Decks#hicht aus korrosionsbeständigen Edelmetallen überzogen und durch Wärmewirkung vor oder bei der Anwendung damit legiert ist.2. The method according to claim i, characterized by the use of corrosion- and oxidation-resistant alloys of silver with corrosion-resistant noble metals such as gold, palladium, silver. 3. The method according to claims i and 2, characterized by the use of corrosion- and oxidation-resistant alloys that are on the documents, for. B. ceramic support bodies, by separate application of the components and diffusion by the effect of heat before or during the application. 4. The method according to claims i to 3, characterized by the use of alloys which have arisen in that silver is first applied to the carrier body, the silver coating is coated with a cover layer of corrosion-resistant noble metals and alloyed with it by the action of heat before or during use is.
DED5340D 1942-04-24 1943-04-02 Recovery of the platinum which evaporates during ammonia combustion Expired DE884639C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DED5340D DE884639C (en) 1942-04-24 1943-04-02 Recovery of the platinum which evaporates during ammonia combustion

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE450179X 1942-04-24
DED5340D DE884639C (en) 1942-04-24 1943-04-02 Recovery of the platinum which evaporates during ammonia combustion

Publications (1)

Publication Number Publication Date
DE884639C true DE884639C (en) 1953-07-27

Family

ID=6538366

Family Applications (3)

Application Number Title Priority Date Filing Date
DED87647D Expired DE747120C (en) 1942-04-24 1942-04-25 Recovery of the platinum which evaporates during ammonia combustion
DED5340D Expired DE884639C (en) 1942-04-24 1943-04-02 Recovery of the platinum which evaporates during ammonia combustion
DED5337D Expired DE878799C (en) 1942-04-24 1943-06-09 Process for the recovery of the platinum which evaporates during ammonia combustion

Family Applications Before (1)

Application Number Title Priority Date Filing Date
DED87647D Expired DE747120C (en) 1942-04-24 1942-04-25 Recovery of the platinum which evaporates during ammonia combustion

Family Applications After (1)

Application Number Title Priority Date Filing Date
DED5337D Expired DE878799C (en) 1942-04-24 1943-06-09 Process for the recovery of the platinum which evaporates during ammonia combustion

Country Status (5)

Country Link
BE (2) BE452298A (en)
CH (1) CH235560A (en)
DE (3) DE747120C (en)
FR (2) FR892074A (en)
NL (2) NL64418C (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE972472C (en) * 1944-12-19 1959-07-30 Lonza Werke Elektrochemische F Process for the recovery of platinum metals volatilized from platinum or platinum alloy catalysts
DE938908C (en) * 1953-09-17 1956-02-09 Basf Ag Process for the recovery of noble metals, in particular metals of the platinum group, from the reaction gases formed during catalytic conversions of such metals
US3515541A (en) * 1967-05-03 1970-06-02 Chemie Linz Ag Process for the recovery of noble metals
ES388847A1 (en) * 1970-03-05 1973-06-01 Engelhard Min & Chem Recovery of platinum group metals
GB8516333D0 (en) * 1985-06-28 1985-07-31 Johnson Matthey Plc Nitric oxide

Also Published As

Publication number Publication date
BE452298A (en) 1943-10-30
DE878799C (en) 1953-06-05
NL64335C (en) 1900-01-01
FR53120E (en) 1945-09-19
CH235560A (en) 1944-12-15
NL64418C (en) 1900-01-01
FR892074A (en) 1944-03-28
DE747120C (en) 1944-02-22
BE450179A (en) 1900-01-01

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