SU427728A1 - - Google Patents

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Publication number
SU427728A1
SU427728A1 SU1823250A SU1823250A SU427728A1 SU 427728 A1 SU427728 A1 SU 427728A1 SU 1823250 A SU1823250 A SU 1823250A SU 1823250 A SU1823250 A SU 1823250A SU 427728 A1 SU427728 A1 SU 427728A1
Authority
SU
USSR - Soviet Union
Prior art keywords
catalyst
ketones
fatty acids
decarboxylation
manganese oxide
Prior art date
Application number
SU1823250A
Other languages
Russian (ru)
Original Assignee
В. И. Дышловой , Ф. В. Линчевский
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Publication date
Application filed by В. И. Дышловой , Ф. В. Линчевский filed Critical В. И. Дышловой , Ф. В. Линчевский
Priority to SU1823250A priority Critical patent/SU427728A1/ru
Application granted granted Critical
Publication of SU427728A1 publication Critical patent/SU427728A1/ru

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Description

(54) КАТАЛИЗАТОР ДЛЯ ДЕКАРБОКСИЛИРОВАНИЯ ЖИРНЫХ(54) CATALYST FOR DECARBOXYLATION OF FATY

КИСЛОТACID

1one

Изобретение относитс  к области производства катализаторов, примен емых в промышленности дл  получени  кетонов.The invention relates to the manufacture of catalysts used in industry for the production of ketones.

Известен катализатор дл  декарбоксилировани  жирных кислот (натуральных и синтетических ) на основе окиси марганца.A catalyst for the decarboxylation of fatty acids (natural and synthetic) based on manganese oxide is known.

Однако известный катализатор обладает недостаточно высокой активностью и селективностью в процессе декарбоксилировани  жирных кислот.However, the known catalyst has insufficiently high activity and selectivity in the process of decarboxylation of fatty acids.

Повышение активности и селективности катализатора обеспечиваетс  за счет того, что катализатор сод,ержит (вес.%) окиси марганца- от 1,0 до 10,0, манганата кали  от 2,0 до 20,0 и активной окиси алюмини  - от 71,0 до 97,0.The increase in the activity and selectivity of the catalyst is ensured by the fact that the catalyst soda, stainless (wt.%) Manganese oxide is from 1.0 to 10.0, potassium manganate from 2.0 to 20.0 and active alumina from 71, 0 to 97.0.

Предлагаемый катализатор позвол ет ускорить реакцию кетонизации жирных кислот.The proposed catalyst allows for the acceleration of the fatty acid ketonization reaction.

Декарбоксилирование синтетических жирных кислот проходит с большей объемной скоростью (0,3-;-0,8 л/л катализатора/час) и в более м гких температурных услови х (370°С) на предлагаемом катализаторе. Степень превращени  кислот в кетоны достигает 99,6%.Decarboxylation of synthetic fatty acids takes place at a higher volumetric rate (0.3 -; - 0.8 l / l of catalyst / hour) and in milder temperature conditions (370 ° C) on the proposed catalyst. The degree of conversion of acids to ketones reaches 99.6%.

Выход жирных кетонов высок и составл ет 74-75%. Теоретический выход кетонов 75,4%.The yield of fatty ketones is high and ranges from 74-75%. The theoretical yield of ketones is 75.4%.

Пример 1. Кетоны получают пропусканием паров синтетических жирных кислотExample 1. Ketones are obtained by passing vapors of synthetic fatty acids.

фракции СБ-Се (кислотное число 446 мг кон/г) в проточной системе через реактор, заполненный кусковым катализатором, содержашим МпОг: К2Мп04: 7 А12Оз в соотношеНИИ 1,0:2,26:7,6 в токе углекислого газа при избыточном давлении 20-40 мм рт. ст.SB-Ce fractions (acid number 446 mg con / g) in a flow system through a reactor filled with a lump catalyst containing MpOg: K2Mn04: 7 A12Oz in a ratio of 1.0: 2.26: 7.6 in a stream of carbon dioxide at an overpressure 20-40 mm Hg. Art.

Результаты кетонизации СЖК СБ-Се приведены в таблице 1.The results of the ketonization of FLC SB-Ce are given in table 1.

Хроматографический состав кетонов, полученных кетонизацией синтетических жирныхChromatographic composition of ketones obtained by the ketonization of synthetic fatty

кислот Cs-Сб, следующий:acids Cs-Sat, the following:

Исходные кислот, %Source acids,%

Кетоны, %Ketones,%

Сз -1,0Sz -1,0

С5--0,4 C5--0,4

Сц-8 ,6Sc-8, 6

C - 6,C - 6,

GIJQ-1 ,2 GIJQ-1, 2

5,05.0

С5-15,7C5-15,7

-3,0 С- -2,0 -3.0 C- -2.0

§;: Се--3,8 § ;: Се - 3.8

Со-24,3Co-24.3

1,71.7

С,-25,2 Со-9,3 C, -25.2 Co-9.3

CisCis

-0,8-0,8

Cg -18,0Cg -18.0

с„Сю -15,9 with „Xu -15.9

0,40.4

С,-5,0 Си-17,1 C, -5.0 C-17.1

С-ао S-ao

0,16 С,о-4,2 С,г -17,0 Cai-0 ,04 Си-0,5 С,з-13,60.16 C, o-4.2 C, g -17.0 Cai-0, 04 Cu-0.5 C, g-13.6

25 Дл  сравнени  привод тс  результаты декарбоксилировани  синтетических жирных кислот Сз-Сб (кислотное число 446 мг КОН/г) на катализаторе МпО.25 For comparison, the results of decarboxylation of C3-Sb synthetic fatty acids (acid number 446 mg KOH / g) on an MpO catalyst are given.

Предмет изобретени Subject invention

Катализатор дл  декарбоксилировани  жирных кислот на основе окиси марганца, отличающийс  тем, что, с целью новышени A catalyst for the decarboxylation of fatty acids based on manganese oxide, characterized in that, in order to

Таблица 1Table 1

Таблица 2table 2

активности и селективности катализатора, он содержит (вес.%) окиси марганца - от 1,0 до 10,0, манганата кали  - от 2,0 до 20,0 и активной окиси алюмини  - от 71,0 до 97,0.activity and selectivity of the catalyst, it contains (wt.%) manganese oxide - from 1.0 to 10.0, potassium manganate - from 2.0 to 20.0 and active alumina - from 71.0 to 97.0.

SU1823250A 1972-08-28 1972-08-28 SU427728A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SU1823250A SU427728A1 (en) 1972-08-28 1972-08-28

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SU1823250A SU427728A1 (en) 1972-08-28 1972-08-28

Publications (1)

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SU427728A1 true SU427728A1 (en) 1974-05-15

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SU1823250A SU427728A1 (en) 1972-08-28 1972-08-28

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SU (1) SU427728A1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007107337A1 (en) * 2006-03-20 2007-09-27 Albemarle Netherlands Bv A process for the decarboxylation of fatty acids
WO2007136873A2 (en) * 2006-05-19 2007-11-29 The Procter & Gamble Company Process for decarboxylation of fatty acids and oils to produce paraffins or olefins

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007107337A1 (en) * 2006-03-20 2007-09-27 Albemarle Netherlands Bv A process for the decarboxylation of fatty acids
US7781619B2 (en) 2006-03-20 2010-08-24 Albemarle Netherlands B.V. Process for the decarboxylation of fatty acids
CN101421215B (en) * 2006-03-20 2013-04-03 雅宝荷兰有限责任公司 A process for the decarboxylation of fatty acids
WO2007136873A2 (en) * 2006-05-19 2007-11-29 The Procter & Gamble Company Process for decarboxylation of fatty acids and oils to produce paraffins or olefins
WO2007136873A3 (en) * 2006-05-19 2008-04-10 Procter & Gamble Process for decarboxylation of fatty acids and oils to produce paraffins or olefins

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