SU910621A1 - Process for producing 4,5,6-triamino pyrimidine - Google Patents
Process for producing 4,5,6-triamino pyrimidine Download PDFInfo
- Publication number
- SU910621A1 SU910621A1 SU792847534A SU2847534A SU910621A1 SU 910621 A1 SU910621 A1 SU 910621A1 SU 792847534 A SU792847534 A SU 792847534A SU 2847534 A SU2847534 A SU 2847534A SU 910621 A1 SU910621 A1 SU 910621A1
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- SU
- USSR - Soviet Union
- Prior art keywords
- nickel
- aluminum
- alloy
- mixture
- catalyst
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- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
Изобретение относитс к тонкому органическому синтезу, а именно к способу получени 4,5/6-тpиaминoпиpшIИДИнa .This invention relates to fine organic synthesis, in particular to a method for producing 4,5 / 6-tri-aminopyryl IIDIN.
4,5,6-Триаминопиримидин может найти применение как промежуточный продукт синтеза аденина и новых лекарственных средств, таких, как этаден и мерадин.4,5,6-Triaminopyrimidine can be used as an intermediate product for the synthesis of adenine and new drugs, such as etaden and meradin.
Известен способ получени 4,5,6триаминопиримидина восстановлением 4,6-диамино-5-фенилазопиримидина водородом на никеле Рене при нагревании 1 .A known method for producing 4,5,6triaminopyrimidine is by reducing 4,6-diamino-5-phenylazopyrimidine with hydrogen on Rene nickel by heating 1.
Недостатками этого метода вл ютс применение пожаро- и взрывоопасных веществ, таких, как скелетный катализатор и водород, сложность и многостадийность процесса.The disadvantages of this method are the use of flammable and explosive substances, such as skeletal catalyst and hydrogen, the complexity and multistage of the process.
Наиболее близким к предлагаемому способу вл етс способ получени 4,5,6-триаминопиримидина восстановлением и десульфированием 2-тио-4,б-диамино-5-нитрозопиримидинав присутствии скелетного катализатора - никел Рене при нагревании вначале , до , затем при 80 - 120°С. Процесс протекает в течение 2 - .4 ч 2,The closest to the proposed method is the method of obtaining 4,5,6-triaminopyrimidine by reducing and desulfurizing 2-thio-4, b-diamino-5-nitrosopyrimidine in the presence of a skeletal catalyst, Rene nickel, heated first, before, then at 80-120 ° WITH. The process takes place within 2 - .4 h 2,
Недостатками этого способа вл ютс необходимость специального приготовлени огнеопасного никел Рене , расход которого составл ет 5 кг на 1 кг исходного продукта, взрывоопасность процесса при работе с водородом под давлением, необходимость соблюдени мер безопасности при хранении катализатора -и сложность его приготовлени , а также двухстадийность процесса, требующе .10 го изменени условий его проведени .The disadvantages of this method are the need for special preparation of flammable Rene nickel, the consumption of which is 5 kg per 1 kg of the initial product, the explosion hazard of the process when working with hydrogen under pressure, the need to observe safety measures when storing the catalyst and the complexity of its preparation, as well as the two-stage process requiring a .10 change in its conditions.
Целью изобретени вл етс упрощение технологии процесса.The aim of the invention is to simplify the process technology.
Поставленна цель достигаетс The goal is achieved
15 тем, что при осуществлении способа получени 4,5,6-триаминопиримидина восстановлением и десульфированием 2-ТИО-4,6-диамино-5-нитрозопиримидина при нагревании в присутствии ка20 тализатора в качестве последнего используют сплав никел с алюминием, содержащий 45 - 53 вес. % никел и 47 - 55 вес.% алюмини , и процесс ведут в одну стадию в присутствии 15 by the fact that, when carrying out the method for producing 4,5,6-triaminopyrimidine by reducing and desulfurizing 2-TIO-4,6-diamino-5-nitrosopyrimidine when heated in the presence of a catalytic converter, the latter uses a nickel-aluminum alloy containing 45 - 53 weight. % Nickel and 47 - 55 wt.% aluminum, and the process is conducted in one stage in the presence of
25 водного раствора едкого натра или едкого кали. .25 aqueous solution of caustic soda or caustic potash. .
Примен емый сплав никел с гшюминием вл етс промышленным продуктом , выпускаемым отечественной и The nickel alloy with gsuminium used is an industrial product produced domestically and
Claims (2)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU792847534A SU910621A1 (en) | 1979-12-04 | 1979-12-04 | Process for producing 4,5,6-triamino pyrimidine |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU792847534A SU910621A1 (en) | 1979-12-04 | 1979-12-04 | Process for producing 4,5,6-triamino pyrimidine |
Publications (1)
Publication Number | Publication Date |
---|---|
SU910621A1 true SU910621A1 (en) | 1982-03-07 |
Family
ID=20862682
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU792847534A SU910621A1 (en) | 1979-12-04 | 1979-12-04 | Process for producing 4,5,6-triamino pyrimidine |
Country Status (1)
Country | Link |
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SU (1) | SU910621A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2001089587A3 (en) * | 2000-05-19 | 2002-04-18 | Henkel Kgaa | Agents for dyeing fibres containing keratin |
-
1979
- 1979-12-04 SU SU792847534A patent/SU910621A1/en active
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2001089587A3 (en) * | 2000-05-19 | 2002-04-18 | Henkel Kgaa | Agents for dyeing fibres containing keratin |
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