DE603687C - Process for the production of catalysts for ammonia synthesis - Google Patents
Process for the production of catalysts for ammonia synthesisInfo
- Publication number
- DE603687C DE603687C DEG71130D DEG0071130D DE603687C DE 603687 C DE603687 C DE 603687C DE G71130 D DEG71130 D DE G71130D DE G0071130 D DEG0071130 D DE G0071130D DE 603687 C DE603687 C DE 603687C
- Authority
- DE
- Germany
- Prior art keywords
- alkaline earth
- alkali
- catalysts
- production
- evaporated
- 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
Links
Classifications
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01C—AMMONIA; CYANOGEN; COMPOUNDS THEREOF
- C01C1/00—Ammonia; Compounds thereof
- C01C1/02—Preparation, purification or separation of ammonia
- C01C1/04—Preparation of ammonia by synthesis in the gas phase
- C01C1/0405—Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst
- C01C1/0411—Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst characterised by the catalyst
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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
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/02—Boron or aluminium; Oxides or hydroxides thereof
-
- 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
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/24—Nitrogen compounds
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Analytical Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Catalysts (AREA)
Description
Verfahren zur Herstellung von Katalysatoren für die Ammoniaksynthese Das Patent 567 728 betrifft ein Verfahren zur Herstellung eines Katalysators für die Ammoniaksynthese, gemäß welchem Alkali-oder Erdalkalieisencyanverbindungen im Verhältnis von 1/4 bis zu i Äquivalent Säure auf i Äquivalent komplexe Cyanverbindung mit Säure versetzt und eingedampft werden. Gemäß einer -Ausführungsform dieses älteren Verfahrens werden den komplexen Cyaniden Stoffe, z. B. Alkalisilikate, zugesetzt, die bei der Säurebehandlung Trägersubstanzen für den aus den komplexen Cyaniden entstehenden Katalysatorgrundstoff ergeben. Gemäß der vorliegenden Erfindung sollen die als Trägersubstanzen wirkenden Stoffe, die zugleich die Wirksamkeit des Katalysators erhöhen, in Säure löslich, aber durch Hydrolyse fällbar sein und dabei schwer schmelzbare Metalloxyde ergeben, und sie sollen dadurch in den Katalysator eingeführt werden, daß man solche Stoffe enthaltende Säure auf die Alkali- oder Erdalkalicyanide zur Einwirkung bringt. Geeignete Stoffe sind Verbindungen des Zirkons, Aluminiums, Thoriums und der seltenen Erden. Die Verwendung von Zirkon, welches z. B. in Salzsäure gelöst sein kann, hat sich für die Durchführung des beanspruchten Verfahrens als sehr wirksam erwiesen. Mit der Salzsäurelösung von Zirkon werden die Alkali- oder Erdalkalieisencyanverbindungen zur Trockne gedampft. Gegebenenfalls setzt man zum Ausgleichen überschüssiger Säure dem eingedampften Niederschlag nochmals eine geringe Menge des Alkali- oder Erdalkalieisen.-cyansalzes, z. B. Kaliumferrocyanid, in wäßriger Lösung zu und wiederholt die Trocknung.Process for the preparation of catalysts for the synthesis of ammonia The patent 567 728 relates to a method of making a catalyst for the ammonia synthesis, according to which alkali or alkaline earth cyanogen compounds in the Ratio of 1/4 up to 1 equivalent of acid to 1 equivalent of complex cyano compound mixed with acid and evaporated. According to one embodiment of this older one Process are the complex cyanide substances such. B. alkali silicates, added, the carrier substances for the complex cyanides in the acid treatment resulting catalyst base material. According to the present invention the substances acting as carrier substances, which at the same time increase the effectiveness of the catalyst increase, soluble in acid, but precipitable by hydrolysis and difficult to melt Metal oxides, and they are supposed to be introduced into the catalyst as a result, that one acid containing such substances on the alkali or alkaline earth metal cyanides Brings influence. Suitable substances are compounds of zirconium, aluminum and thorium and the rare earths. The use of zircon, which z. B. dissolved in hydrochloric acid can be, has been found to be very effective for carrying out the claimed method proven. With the hydrochloric acid solution of zirconium, the alkali or alkaline earth iron cyan compounds steamed to dryness. If necessary, it is used to compensate for excess acid add a small amount of the alkali or alkaline earth iron cyan salt to the evaporated precipitate, z. B. potassium ferrocyanide, in aqueous solution and repeated the drying.
Beispiel Man löst 42 g Kaliumferrocyanid in 150 ccm warmen Wassers auf und versetzt mit 309 konzentrierter Salzsäure, die 59 Zirkondioxyd oder die äquivalente Menge Zirkonhydroxyd oder Zirkonoxychlorid enthält. Nach dem Eindampfen der Mischung verrührt man den Rückstand mit etwa 5 g Kaliumferrocyamid, das in einer genügenden Menge Wasser gelöst ist, und trocknet ihn nochmals. Nach dem vorherigen Behandeln mit einem reinen Stickstoff-Wasserstoff-Gemisch bei 4oo° kann er als Katalysator benutzt werden und ergibt eine Ausbeute von 13 Volumprozent Ammoniak.EXAMPLE 42 g of potassium ferrocyanide are dissolved in 150 cc of warm water and 309 g of concentrated hydrochloric acid containing 59 zirconium dioxide or the equivalent amount of zirconium hydroxide or zirconium oxychloride are added. After the mixture has been evaporated, the residue is stirred with about 5 g of potassium ferrocyamide dissolved in a sufficient amount of water and dried again. After previous treatment with a pure nitrogen-hydrogen mixture at 400 °, it can be used as a catalyst and gives a yield of 13 percent by volume of ammonia.
Zum Vergleich wurde folgender Versuch angestellt, der nur eine Ausbeute von 7 Volumprozent Ammoniak ergab.For comparison, the following experiment was carried out, which only yielded one yield of 7 volume percent ammonia.
42g Kaliumferrocyanid wurden in i 5o ccm Wasser aufgelöst und mit 309 konzentrierter Salzsäure versetzt und eingedampft. Dem Eindampfrückstand wurden 5 g Zirkondioxyd in festem Zustand hinzugemischt. Diese Mischung wurde mit etwa 5 g Kaliumferrocyanid; das in genügender Menge Wasser gelöst war, verrieben. Nach Trocknung wurde der Trockenrückstand vorsichtig auf eine Temperatur von q.00° unter Hindurchleiten eines reinen Stickstoff-Wasserstoff-Gemisches erhitzt und unter folgenden Arbeitsbedizigungen zur Katalyse benutzt: Druck: 8o bis 9o atm, , Temperatur: 40o° C, Strömungsgeschwindigkeit: 6 1/g/ Stunde.42 g of potassium ferrocyanide were dissolved in 150 cc of water, 309 g of concentrated hydrochloric acid were added and the mixture was evaporated. 5 g of solid zirconium dioxide were added to the evaporation residue. This mixture was made with about 5 g of potassium ferrocyanide; which was dissolved in sufficient amount of water, rubbed in. After drying, the dry residue was carefully heated to a temperature of q.00 ° while a pure nitrogen-hydrogen mixture was passed through and used for catalysis under the following operating conditions: pressure: 80 to 90 atm, temperature: 40 ° C., flow rate: 6 l / g / hour.
Es ergab sich eine Ausbeute von etwa 7 V0= lumprozent Ammoniak.The result was a yield of about 7 vol% ammonia.
Claims (1)
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL29903D NL29903C (en) | 1927-08-28 | ||
DEG71130D DE603687C (en) | 1927-08-28 | 1927-08-28 | Process for the production of catalysts for ammonia synthesis |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEG71130D DE603687C (en) | 1927-08-28 | 1927-08-28 | Process for the production of catalysts for ammonia synthesis |
Publications (1)
Publication Number | Publication Date |
---|---|
DE603687C true DE603687C (en) | 1934-10-06 |
Family
ID=7135032
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DEG71130D Expired DE603687C (en) | 1927-08-28 | 1927-08-28 | Process for the production of catalysts for ammonia synthesis |
Country Status (2)
Country | Link |
---|---|
DE (1) | DE603687C (en) |
NL (1) | NL29903C (en) |
-
0
- NL NL29903D patent/NL29903C/xx active
-
1927
- 1927-08-28 DE DEG71130D patent/DE603687C/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
NL29903C (en) |
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