RU1805127C - Method of phenol synthesis - Google Patents

Method of phenol synthesis

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Publication number
RU1805127C
RU1805127C SU884445646A SU4445646A RU1805127C RU 1805127 C RU1805127 C RU 1805127C SU 884445646 A SU884445646 A SU 884445646A SU 4445646 A SU4445646 A SU 4445646A RU 1805127 C RU1805127 C RU 1805127C
Authority
RU
Russia
Prior art keywords
nitric oxide
catalyst
yield
benzene
target product
Prior art date
Application number
SU884445646A
Other languages
Russian (ru)
Inventor
Александр Сергеевич Харитонов
Татьяна Николаевна Александрова
Лидия Алексеевна Вострикова
Казимира Гавриловна Ионе
Геннадий Иванович Панов
Original Assignee
Институт катализа СО АН СССР
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 Институт катализа СО АН СССР filed Critical Институт катализа СО АН СССР
Priority to SU884445646A priority Critical patent/RU1805127C/en
Application granted granted Critical
Publication of RU1805127C publication Critical patent/RU1805127C/en

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Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

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

Abstract

Изобретение относитс  к органическому синтезу, в частности, к получению фенола . Цель - увеличение выхода целевого продукта . Получение ведут окислением бензола оксидом азота при 350 - 400°С в присутствии катализатора. В качестве последнего используют цеолит типа пентасил с мольным отношением 5Ю2/А 20з в интервале 40 - 100. Способ позвол ет повысить выход целевого продукта на 1,3 - 3,3% и упростить технологию за счет снижени  температуры процесса на 100%. 2 табл.The invention relates to organic synthesis, in particular to the production of phenol. The goal is to increase the yield of the target product. The preparation is carried out by oxidation of benzene with nitric oxide at 350-400 ° C in the presence of a catalyst. As the latter, a pentasil-type zeolite with a molar ratio of 5X2 / A 20g in the range of 40-100 is used. The method allows to increase the yield of the target product by 1.3-3.3% and to simplify the technology by reducing the process temperature by 100%. 2 tab.

Description

Изобретение относитс  к способу получени  фенола который  вл етс  ценным многотоннажным продуктом, дл  производ ства фенольных смол, синтеза капролакта- мэ, синтеза адипиновой кислоты.The invention relates to a method for producing phenol, which is a valuable multi-ton product, for the production of phenolic resins, the synthesis of caprolactame, and the synthesis of adipic acid.

Цель изобретени  - увеличение выхода целевого продукта. The purpose of the invention is to increase the yield of the target product.

Пример 1. Пентасил с отношением. 5Ю2/А120з.- 100, загружают в кварцевый реактор с внутренним диаметром 7 мм, Объем катализатора 2 см3, катализатор беретс  в виде фракции 0,5 - 1 мм. На катализатор, нагретый до заданной температуры, подают со скоростью 60 см /мин реакционную смесь следующего состава (моль. %): бензол - 4,8, оксид азота (1) - 19,5, остальное гелий или иной инертный газ, например, азот. С помощью газового хроматографического анализа определ етс  состав реакционной смеси до и после реактора, на основании чего рассчитываетс  степень превращени  бензола, селективность по фенолу и выход фенола. Помимо CeHsOH и С02, других угле- водородсодержащих соединений, а в том числе малеионового ангидрида и СО, средиExample 1. Pentasil with attitude. 5U2 / A120z.- 100, loaded into a quartz reactor with an inner diameter of 7 mm, the volume of the catalyst is 2 cm3, the catalyst is taken in the form of a fraction of 0.5-1 mm. A reaction mixture of the following composition (mol.%) Is supplied to a catalyst heated to a predetermined temperature at a speed of 60 cm / min: benzene - 4.8, nitric oxide (1) - 19.5, the rest is helium or another inert gas, for example, nitrogen. Using gas chromatographic analysis, the composition of the reaction mixture before and after the reactor is determined, based on which the degree of benzene conversion, phenol selectivity and phenol yield are calculated. In addition to CeHsOH and CO2, other hydrocarbon-containing compounds, including maleic anhydride and CO, among

продуктов реакции не обнаружено. Результаты представлены в табл. 1.no reaction products were found. The results are presented in table. 1.

При м е р ы 2 - 14. Реакцию ведут, аналогично примеру 1. Примен емый катализатор , температура реакции и полученные результаты представлены в табл. 1 и 2. Табл. 2 показывает неэффективность использовани  цеолитов других типов, кроме предложенного, в данном способе.Examples 2 to 14. The reaction is carried out, analogously to example 1. The catalyst used, the reaction temperature and the results obtained are presented in table. 1 and 2. Tab. 2 shows the inefficiency of using zeolites of other types than those proposed in this method.

Данный способ позвол ет повысить выход целевого продукта на 1,3 - 3,3%, в сравнении с прототипом и упростить технологию за счет снижени  температуры процесса на 100% (в сравнении с прототипом ). Изменение мольного соотношени  бензол: оксид азота в интервале 1 : 1,7 - 5,6 не вли ет на достижение поставленной цели.This method allows to increase the yield of the target product by 1.3 - 3.3%, in comparison with the prototype and to simplify the technology by reducing the process temperature by 100% (in comparison with the prototype). A change in the molar ratio of benzene: nitric oxide in the range of 1: 1.7-5.6 does not affect the achievement of the goal.

Claims (1)

Формула изобретени The claims Способ получени  фенола окислением бензола оксидом азота при повышенной температуре в присутствии катализатора, отличающийс  тем, что, с целью увеличени  выхода целевого продукта, в ка00A method for producing phenol by oxidizing benzene with nitric oxide at an elevated temperature in the presence of a catalyst, characterized in that, in order to increase the yield of the target product, by ka00 СWITH соwith о елabout eating ND VJNd vj 31805127 431805127 4 местве катализатора используют цеолитти- 1°° па пентасил с мол рным соотношением провод т при 350 4UU иThe catalyst is used with a zeolite-1 °° pentasil with a molar ratio carried out at 350 4UU and Каталитические свойства пентасилов (Н-форма) в реакции окислени  бензола оксидом азота (1)Catalytic properties of pentasils (H-form) in the reaction of benzene oxidation with nitric oxide (1) Запредельные примеры. Outrageous examples. Таблица 1Table 1 Тао лица2Tao Faces2 Каталитические свойства цеолитов различного типа в реакции окислени  бензола оксидом азота (1) при 500 СCatalytic properties of zeolites of various types in the reaction of benzene oxidation with nitric oxide (1) at 500 C
SU884445646A 1988-06-22 1988-06-22 Method of phenol synthesis RU1805127C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SU884445646A RU1805127C (en) 1988-06-22 1988-06-22 Method of phenol synthesis

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SU884445646A RU1805127C (en) 1988-06-22 1988-06-22 Method of phenol synthesis

Publications (1)

Publication Number Publication Date
RU1805127C true RU1805127C (en) 1993-03-30

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
SU884445646A RU1805127C (en) 1988-06-22 1988-06-22 Method of phenol synthesis

Country Status (1)

Country Link
RU (1) RU1805127C (en)

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
Iwanto М. NirataY.-i. Phys. Chem; 1983, 87, № 6, p. 903-905. *

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