DE1642999A1 - Copper catalyst and process for its manufacture - Google Patents
Copper catalyst and process for its manufactureInfo
- Publication number
- DE1642999A1 DE1642999A1 DE19671642999 DE1642999A DE1642999A1 DE 1642999 A1 DE1642999 A1 DE 1642999A1 DE 19671642999 DE19671642999 DE 19671642999 DE 1642999 A DE1642999 A DE 1642999A DE 1642999 A1 DE1642999 A1 DE 1642999A1
- Authority
- DE
- Germany
- Prior art keywords
- copper
- copper catalyst
- catalyst
- carrier
- manufacture
- 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.)
- Granted
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/72—Copper
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/89—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals
- B01J23/8926—Copper and noble metals
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/90—Regeneration or reactivation
- B01J23/94—Regeneration or reactivation of catalysts comprising metals, oxides or hydroxides of the iron group metals or copper
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Catalysts (AREA)
Description
Eupferkatalysator und Verfahren zu seiner Herstellung Die erfindugn bezieht sich auf einen Kupferkatalysator und auf ein Verfahren zu seiner Herstellung. Eupfer catalyst and process for its production The erfindugn relates to a copper catalyst and a process for its manufacture.
Kupferkatalysatoren dienen bekanntlich dazu, in Gasgemischen selektiv den Sauerstoff zu binden. Die für diese Zwecke in Betracht kommenden Kupferverbindungen werden auf dem vorsugsweise inerten Träger in unterschiedlicher Weise aufgetragen.It is known that copper catalysts are used selectively in gas mixtures to bind the oxygen. The copper compounds that can be used for these purposes are applied in different ways to the preventively inert carrier.
So ist es z. B. bekannt, Kupferhydroxyd aus Lösungen auszufällen, wobei dafür gesorgt wird, daß es sich auf den Träger absetzt.So it is z. B. known to precipitate copper hydroxide from solutions, causing it to settle on the carrier.
Es ist weiter bekannt, Kupferverbindungen und Träger gemeinsam aus Lösungen beider auszufällen. Es ist weiter bekannt, Kupfernitrat auf den Trägern zu zersetzen. So hergestellte aktive Verbindungen haben z. B. bei 1500 C eine maximale Aufnahmefähigkeit von 4 ltr. Sauerstoff pro ltr. Eatalysator, dynamisch gemessen Als Endwert für die Messung wurde dabei ein Wert < 1 ppm °2 im Endgas genommen.It is also known to make copper compounds and carriers together To fail solutions of both. It is also known to have copper nitrate on the supports to decompose. Active compounds so prepared have e.g. B. at 1500 C a maximum Capacity of 4 ltr. Oxygen per liter Eatalyst, measured dynamically as The final value for the measurement was taken to be <1 ppm ° 2 in the final gas.
Mit keinem der bekannten Träger konnte man einen in sich stabilen Katalysator erhalten. Vielmehr mußte man die getrocknete oder ungetrocknete Katalysaprmasse stabilisieren, wozu Wasserglas und Tablettierungshilfsmittel verschiedenster Art dienten.With none of the known carriers one could be stable in oneself Catalyst obtained. Rather, you had to use the dried or undried catalyst mass stabilize, including waterglass and tableting aids of various kinds served.
Alle diese Zusätze beeinflußten aber die Aktivität des Katalysators ungünstig.However, all of these additives affected the activity of the catalyst unfavorable.
Der Katalysator der Erfindung hat demgegenüber den Vorteil, daß er sich ohne Zusätze irgendwelcher Art zu einem abriebfesten Körper tablettieren läßt und auch den besten bekannten Katalysator an Wirksamkeit um mehr als das Doppelte übertrifft, beträgt doch Sauerstoffaufnahme eines Liters des Katalysators der Erfindung unter den Bedingungen des oben erwähnten Beispiels mehr als 8 1.The catalyst of the invention has the advantage that it can be tabletted into an abrasion-resistant body without additives of any kind and also the best known catalyst more than doubles in effectiveness exceeds, but is oxygen uptake of one liter of the catalyst of the invention under the conditions of the above example more than 8 1.
Alle diese Vorteile sind bei dem Katalysator der Erfindung durch die Verwendung eines Trägers aus g-stabilisiertem Aluminiumoxyd und/oder Aluminiumsilikat erreicht. Das Kupfer wird auf diesem Träger reduktiv abgeschieden, indem eine Kupfer salzlösung, in der der Träger suspendiert ist, reduziert wird Kleinere Mengen von Verbindungen der Elemente der 1., 2. s4., 6., 7. und 8. Gruppe des periodischen Systems vor bzw. mach der Fällung einzeln oder im Gemisch zugegeben, erhöhen die Aufnahmekapazität weiter. Die Elemente Zink, Chrom, Mangan, Nickel und die Edelmetalle nehmen hierbei einen bevorzugten Platz ein.All of these advantages are evident in the catalyst of the invention Use of a carrier made of g-stabilized aluminum oxide and / or aluminum silicate achieved. The copper is deposited reductively on this carrier by adding a copper saline solution in which the carrier is suspended is reduced Smaller ones Sets of compounds of the elements of the 1st, 2nd, 4th, 6th, 7th and 8th groups of the periodic The system is added before or after the precipitation, individually or as a mixture, increase the Recording capacity further. The elements zinc, chromium, manganese, nickel and the precious metals take a preferred place here.
Der Katalysator kann durch Erhitzung auf 1500 - 1600 C in reduzierender Atmosphäre regeneriert werden.The catalyst can be reduced by heating to 1500 - 1600 C Atmosphere can be regenerated.
Ausführungsbeispiel 52 kg Kupfersulfat werden in 200 1 Wasser gelöst. 0,6 kg Nangansulfat werden als zusätzlicher Aktivator zugesetzt. Als Reduktionsmittel dienen 23 kg Dextrose. In dieser Lösung werden 31,5 kg aktiviertes stabilisiertes Aluminiumoxyd suspendiert. Die Suspension wird zum Sieden erhitzt und das Kupfer durch Eingabe von 30 1 50 %iger Natronlauge reduziert. Exemplary embodiment 52 kg of copper sulfate are dissolved in 200 l of water. 0.6 kg of nangan sulfate are added as an additional activator. As a reducing agent serve 23 kg of dextrose. In this solution, 31.5 kg of activated stabilized Aluminum oxide suspended. The suspension is heated to the boil and the copper reduced by adding 30 1 50% sodium hydroxide solution.
Claims (3)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DED0052720 | 1967-04-06 | ||
DED0052720 | 1967-04-06 |
Publications (3)
Publication Number | Publication Date |
---|---|
DE1642999A1 true DE1642999A1 (en) | 1971-05-06 |
DE1642999B2 DE1642999B2 (en) | 1975-10-09 |
DE1642999C3 DE1642999C3 (en) | 1976-05-20 |
Family
ID=
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0434062A1 (en) * | 1989-12-21 | 1991-06-26 | Union Carbide Chemicals And Plastics Company, Inc. | Hydrogenation with Cu-A1-X catalysts |
US5142067A (en) * | 1989-12-21 | 1992-08-25 | Union Carbide Chemicals & Plastics Technology Corporation | Hydrogenation with Cu-Al-X catalysts |
US5191091A (en) * | 1989-12-21 | 1993-03-02 | Union Carbide Chemicals & Plastics Technology Corporation | Hydrogenation with Cu-Al catalysts |
US5298472A (en) * | 1989-12-21 | 1994-03-29 | Union Carbide Chemicals & Plastics Technology Corporation | Hydrogenation with Cu-Al catalysts |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0434062A1 (en) * | 1989-12-21 | 1991-06-26 | Union Carbide Chemicals And Plastics Company, Inc. | Hydrogenation with Cu-A1-X catalysts |
US5142067A (en) * | 1989-12-21 | 1992-08-25 | Union Carbide Chemicals & Plastics Technology Corporation | Hydrogenation with Cu-Al-X catalysts |
US5191091A (en) * | 1989-12-21 | 1993-03-02 | Union Carbide Chemicals & Plastics Technology Corporation | Hydrogenation with Cu-Al catalysts |
US5298472A (en) * | 1989-12-21 | 1994-03-29 | Union Carbide Chemicals & Plastics Technology Corporation | Hydrogenation with Cu-Al catalysts |
Also Published As
Publication number | Publication date |
---|---|
DE1642999B2 (en) | 1975-10-09 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C3 | Grant after two publication steps (3rd publication) | ||
E77 | Valid patent as to the heymanns-index 1977 | ||
8339 | Ceased/non-payment of the annual fee |