SU143388A1 - Method for producing alpha-hydroxyisobutyric acid - Google Patents

Method for producing alpha-hydroxyisobutyric acid

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Publication number
SU143388A1
SU143388A1 SU723002A SU723002A SU143388A1 SU 143388 A1 SU143388 A1 SU 143388A1 SU 723002 A SU723002 A SU 723002A SU 723002 A SU723002 A SU 723002A SU 143388 A1 SU143388 A1 SU 143388A1
Authority
SU
USSR - Soviet Union
Prior art keywords
isobutylene
hydroxyisobutyric acid
producing alpha
oxidation
acid
Prior art date
Application number
SU723002A
Other languages
Russian (ru)
Inventor
В.А. Подгорнова
Р.Ф. Коршунова
Б.Ф. Уставщиков
М.И. Фарберов
А.Ф. Фролов
Original Assignee
В.А. Подгорнова
Р.Ф. Коршунова
Б.Ф. Уставщиков
М.И. Фарберов
А.Ф. Фролов
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 В.А. Подгорнова, Р.Ф. Коршунова, Б.Ф. Уставщиков, М.И. Фарберов, А.Ф. Фролов filed Critical В.А. Подгорнова
Priority to SU723002K priority Critical patent/SU143389A1/en
Priority to SU723002L priority patent/SU143390A1/en
Priority to SU723002A priority patent/SU143388A1/en
Application granted granted Critical
Publication of SU143388A1 publication Critical patent/SU143388A1/en

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  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

Известны способы получени  сх-оксиизомасл ной кислоты путем окислени  изобутилена окислами азота. При этом нар ду с образую1цеГ|СЯ с.-нитратоизол:асл ной кислотой получаетс  сложна  смесь ннтропронзводных изобутилена, которые представл ют определенную опасность, особенно в момент отгонки, так как часто привод т к самопроизвольному неуправл емому окислению и взрыву.Methods for the preparation of c-hydroxy-isobutyric acid by oxidation of isobutylene with nitrogen oxides are known. At the same time, along with the formation of CeH | SJ s.-nitratoisol: with hydrochloric acid, a complex mixture of isoputylene isobutylene is obtained, which present a certain danger, especially at the moment of distillation, since they often lead to spontaneous uncontrollable oxidation and explosion.

Кроме того, Э1И способы предусматривают отгонку избыточной четырехокиси азота в вакууме при температуре +5°, а гидролиз продуктов окислени  изобутилена четырехокисного азота производитс  азотной кислотой различной коннентрапии при температуре +15°.In addition, the E1I methods provide for the distillation of excess nitrogen tetroxide in vacuum at + 5 ° C, and the oxidation products of tetroxide nitrogen isobutylene are produced by nitric acid of various concentrations at + 15 ° C.

Предлагаемый способ позвол ет устранить указанные недостатки пухе.м проведени  гладкого и полного окислени  изобутилена четырехокисью азота в а-нитратоизомасл ную кислоту без образовани  сопутствующих нитропроизводных изобутилена. Это достигаетс  путем введени  в процесс окислени  изобутилена четырехокисью азота катализаторов , например, К2СОз, KNOs, MgO, NaNOa, Ха2СОз и др. Лучшие результаты получены с К2СОз.The proposed method makes it possible to eliminate the indicated disadvantages of fluffing of smooth and complete oxidation of isobutylene with nitrogen tetroxide to α-nitratoisobutyric acid without the formation of accompanying nitro derivatives of isobutylene. This is achieved by introducing catalysts such as K2CO3, KNOs, MgO, NaNOa, Xa2CO3, etc., into the oxidation of isobutylene with nitrogen tetroxide. The best results are obtained with K2CO3.

В предлагаемом способе избыточную четырехокись азота удал ют воздухо.м при температуре Н-15 ;- -30°, а гидролиз продуктов окислени  изобутилена производ т вод ным паром при температуре 100 без применени  азотной кислоты. Весьма значительным преимуществом гидролиза вод ным паром  вл етс  то, что при этом получаетс  только а-оксиизомасл на  кислота без примеси а-нитратоизомасл ной кислоты.In the proposed method, excess nitrogen tetroxide is removed by air m at a temperature of H-15; -30 °, and hydrolysis of the products of isobutylene oxidation is performed by water vapor at a temperature of 100 without using nitric acid. A very significant advantage of steam hydrolysis is that it only produces a-hydroxy-butyric acid without the admixture of a-nitrato-isobutyric acid.

Процесс получени  а-оксиизомасл ной кислоты окислением изобутилена четырехокисью азота можно изобразить следующими упавнеии ми:The process of a-hydroxy-isobutyric acid production by oxidation of isobutylene with nitrogen tetroxide can be represented as follows:

SU723002A 1961-03-23 1961-03-23 Method for producing alpha-hydroxyisobutyric acid SU143388A1 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
SU723002K SU143389A1 (en) 1961-03-23 1961-03-23 Method for producing methacrylic acid and its derivatives
SU723002L SU143390A1 (en) 1961-03-23 1961-03-23 Method for producing methacrylamide
SU723002A SU143388A1 (en) 1961-03-23 1961-03-23 Method for producing alpha-hydroxyisobutyric acid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SU723002A SU143388A1 (en) 1961-03-23 1961-03-23 Method for producing alpha-hydroxyisobutyric acid

Publications (1)

Publication Number Publication Date
SU143388A1 true SU143388A1 (en) 1961-11-30

Family

ID=48299157

Family Applications (3)

Application Number Title Priority Date Filing Date
SU723002K SU143389A1 (en) 1961-03-23 1961-03-23 Method for producing methacrylic acid and its derivatives
SU723002L SU143390A1 (en) 1961-03-23 1961-03-23 Method for producing methacrylamide
SU723002A SU143388A1 (en) 1961-03-23 1961-03-23 Method for producing alpha-hydroxyisobutyric acid

Family Applications Before (2)

Application Number Title Priority Date Filing Date
SU723002K SU143389A1 (en) 1961-03-23 1961-03-23 Method for producing methacrylic acid and its derivatives
SU723002L SU143390A1 (en) 1961-03-23 1961-03-23 Method for producing methacrylamide

Country Status (1)

Country Link
SU (3) SU143389A1 (en)

Also Published As

Publication number Publication date
SU143389A1 (en) 1961-11-30
SU143390A1 (en) 1961-11-30

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