SU483126A1 - Method of preparing catalyst for methane conversion and ammonia dissociation - Google Patents
Method of preparing catalyst for methane conversion and ammonia dissociationInfo
- Publication number
- SU483126A1 SU483126A1 SU1998092A SU1998092A SU483126A1 SU 483126 A1 SU483126 A1 SU 483126A1 SU 1998092 A SU1998092 A SU 1998092A SU 1998092 A SU1998092 A SU 1998092A SU 483126 A1 SU483126 A1 SU 483126A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- methane conversion
- preparing catalyst
- ammonia dissociation
- ammonia
- dissociation
- Prior art date
Links
Landscapes
- Catalysts (AREA)
Description
ТаблицаTable
Остаточное содержание метана в сухом конвертируемом газе, об. %, при температуре, °СResidual methane content in dry convertible gas, about. %, at a temperature, ° С
СпособWay
Разработанный катализатор содержит (в %): 20-40 N40, 25-40 алюмината кальци ИЛИ 1высокоглиноземистого цемента, I-2 5 окиси бари и 10-20 окиси .мапни .The developed catalyst contains (in%): 20-40 N40, 25-40 calcium aluminate OR 1 high-alumina cement, I-2 5 barium oxide and 10-20 oxide.
Активность катализаторов определ ют по методике, ирин той дл .катализаторов дл конверсии метана (см. табл. 2) диосоциацин аммиака (см. табл. 3).The activity of the catalysts is determined by the method, irin that for catalysts for methane conversion (see Table 2), diosociacin ammonia (see Table 3).
Таблица 2table 2
Предмет изобретени Subject invention
Способ приготовлени катализатора дл кавверсии метана и диссоциации аммиака путем . смешени никель- и алюминийсодержащего соединени , окислов ил:и солей -магни ; бари и св зующего вещества с последующим прокаливанием и формованием каТаблица 3The method of preparation of the catalyst for the conversion of methane and the dissociation of ammonia by. mixing nickel- and aluminum-containing compounds, sludge oxides: and magnesium salts; barium and binder, followed by calcining and shaping the cABLE 3
тализаторнои массы, отличающийс тем, что, с целью цр.иготавлени «атализатора с более высокой активностью, в качестве никель- и алЮ|МИНйй.оодержащего 1соеди,нени берут отработанный .ни1кельалюминиевый катализатор гидрироваии , содержащий 10-45 вес. % окиси 1никел .catalyst mass, characterized in that, in order to disintegrate the analyzer with higher activity, Nickel and Alloy | MINY. % nickel oxide.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU1998092A SU483126A1 (en) | 1974-02-21 | 1974-02-21 | Method of preparing catalyst for methane conversion and ammonia dissociation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU1998092A SU483126A1 (en) | 1974-02-21 | 1974-02-21 | Method of preparing catalyst for methane conversion and ammonia dissociation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| SU483126A1 true SU483126A1 (en) | 1975-09-05 |
Family
ID=20576400
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SU1998092A SU483126A1 (en) | 1974-02-21 | 1974-02-21 | Method of preparing catalyst for methane conversion and ammonia dissociation |
Country Status (1)
| Country | Link |
|---|---|
| SU (1) | SU483126A1 (en) |
-
1974
- 1974-02-21 SU SU1998092A patent/SU483126A1/en active
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