CS196648B1 - Method of preparing hydroperoxides - Google Patents
Method of preparing hydroperoxides Download PDFInfo
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- CS196648B1 CS196648B1 CS747476A CS747476A CS196648B1 CS 196648 B1 CS196648 B1 CS 196648B1 CS 747476 A CS747476 A CS 747476A CS 747476 A CS747476 A CS 747476A CS 196648 B1 CS196648 B1 CS 196648B1
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- CS
- Czechoslovakia
- Prior art keywords
- oxidation
- hydroperoxides
- reaction
- weight
- hydrocarbons
- Prior art date
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- 150000002432 hydroperoxides Chemical class 0.000 title claims description 11
- 238000000034 method Methods 0.000 title claims description 9
- 238000007254 oxidation reaction Methods 0.000 claims description 20
- 230000008569 process Effects 0.000 claims description 7
- 150000002978 peroxides Chemical class 0.000 claims description 6
- 238000002360 preparation method Methods 0.000 claims description 5
- 125000000751 azo group Chemical group [*]N=N[*] 0.000 claims description 3
- 239000000969 carrier Substances 0.000 claims description 2
- 150000001875 compounds Chemical class 0.000 claims description 2
- 230000003647 oxidation Effects 0.000 description 19
- 150000002430 hydrocarbons Chemical class 0.000 description 15
- 229930195733 hydrocarbon Natural products 0.000 description 14
- 238000006243 chemical reaction Methods 0.000 description 12
- 239000003054 catalyst Substances 0.000 description 10
- 239000000203 mixture Substances 0.000 description 6
- FRIBMENBGGCKPD-UHFFFAOYSA-N 3-(2,3-dimethoxyphenyl)prop-2-enal Chemical compound COC1=CC=CC(C=CC=O)=C1OC FRIBMENBGGCKPD-UHFFFAOYSA-N 0.000 description 5
- 239000007791 liquid phase Substances 0.000 description 5
- KWOLFJPFCHCOCG-UHFFFAOYSA-N Acetophenone Chemical compound CC(=O)C1=CC=CC=C1 KWOLFJPFCHCOCG-UHFFFAOYSA-N 0.000 description 4
- 239000004215 Carbon black (E152) Substances 0.000 description 4
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 229910001882 dioxygen Inorganic materials 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 229910052723 transition metal Inorganic materials 0.000 description 4
- 150000003624 transition metals Chemical class 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- OIGWAXDAPKFNCQ-UHFFFAOYSA-N 4-isopropylbenzyl alcohol Chemical compound CC(C)C1=CC=C(CO)C=C1 OIGWAXDAPKFNCQ-UHFFFAOYSA-N 0.000 description 2
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- RWGFKTVRMDUZSP-UHFFFAOYSA-N cumene Chemical compound CC(C)C1=CC=CC=C1 RWGFKTVRMDUZSP-UHFFFAOYSA-N 0.000 description 2
- OECMNLAWCROQEE-UHFFFAOYSA-N cyclohexylbenzene;hydrogen peroxide Chemical compound OO.C1CCCCC1C1=CC=CC=C1 OECMNLAWCROQEE-UHFFFAOYSA-N 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 239000003999 initiator Substances 0.000 description 2
- 229910052747 lanthanoid Inorganic materials 0.000 description 2
- 150000002602 lanthanoids Chemical class 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- BDCFWIDZNLCTMF-UHFFFAOYSA-N 2-phenylpropan-2-ol Chemical compound CC(C)(O)C1=CC=CC=C1 BDCFWIDZNLCTMF-UHFFFAOYSA-N 0.000 description 1
- JLBJTVDPSNHSKJ-UHFFFAOYSA-N 4-Methylstyrene Chemical compound CC1=CC=C(C=C)C=C1 JLBJTVDPSNHSKJ-UHFFFAOYSA-N 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 229910052787 antimony Inorganic materials 0.000 description 1
- WATWJIUSRGPENY-UHFFFAOYSA-N antimony atom Chemical compound [Sb] WATWJIUSRGPENY-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- MHAJPDPJQMAIIY-UHFFFAOYSA-M hydroperoxide group Chemical group [O-]O MHAJPDPJQMAIIY-UHFFFAOYSA-M 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 238000007348 radical reaction Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
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- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
Vynález sa týká spósobu přípravy hydroperoxidov katalyzovanou oxidáciou alkylaromatických, resp. cykloalkylaromatických uhlovodíkov s molekulovým kyslíkom v kvapalnej fáze.The present invention relates to a process for the preparation of hydroperoxides by catalyzing the oxidation of alkylaromatic and / or alkylaromatic compounds. cycloalkylaromatic hydrocarbons with molecular oxygen in the liquid phase.
Organické hydroperoxidy sa pripravujú prevažne priamymi oxidáciami uhlovodíkov s kyslíkom alebo vzduchom. Reakcia sa uskutečňuje v kvapalnej fáze a prebieha radikálovým mechanizmom. Aby sa zvýšili rýchlosti oxidácie, pridávajú sa k východiskovým uhlovodíkom látky, ktoré iniciujú radikálovu reakciu. Najčastejšie sú to termicky nestabilně organické zlúčeniny, áko azozlúčeniny, peroxidy, hydroperoxidy. Ich počiaťočné koncentrácie bývajú do 5 %. Vyššie koncéhtrácie iniciátora sa nepoužívajú, pretože rýchlosti už bývajú dost vysoké a tiež sa znižuje selektivita reakcie. Konverzita uhlovodíků sa obmedzuje, pričom oxidácia sa přerušuje, keď dbsah hydroperoxidu v zmesi dosiáhne 20 až 35 %. Pri vyšších koncentráciach peroxidu dochádza pri reakčných podmienkach k indukovanému radikálovému rozpadu hydraoperoxidu, ktorý například v případe kuménhydropéroxidu vedie k metanolu, acetofenónu, dimetylfenylkarbinolu a metylstyrénu. Narastanie koncentrácie bočných produktóv spósobuje znižovanie selektivity reakcie. Pri výrobě sa dbá, aby sa nikde nepřehnal hydroperoxid, čo by málo za následok explóziu. Preto sa oxiduje v protiprúdnom etážoyom vertikáln-om alebo horizontálnom reaktore vo vnútri dokonale chladenom.Organic hydroperoxides are prepared predominantly by direct oxidation of hydrocarbons with oxygen or air. The reaction takes place in the liquid phase and proceeds through a free-radical mechanism. In order to increase the oxidation rates, substances which initiate a radical reaction are added to the starting hydrocarbons. Most often, they are thermally unstable organic compounds such as azo compounds, peroxides, hydroperoxides. Their initial concentrations are up to 5%. Higher initiator concentrations are not used because the velocities are already high enough and the selectivity of the reaction is also reduced. The hydrocarbon conversion is limited, and the oxidation is interrupted when the hydroperoxide content in the mixture reaches 20 to 35%. At higher peroxide concentrations, induced radical decomposition of the hydroperoxide under the reaction conditions leads to methanol, acetophenone, dimethylphenylcarbinol and methylstyrene, for example in the case of cumene hydroperoxide. Increasing the concentration of side products causes a reduction in the selectivity of the reaction. During production, care is taken that the hydroperoxide is not exaggerated anywhere, which would result in little explosion. Therefore, it is oxidized in a counter-current vertical or horizontal reactor inside a perfectly cooled reactor.
. Tieto nedostatky v podstatnej miere odstraňuje spósob přípravy hydropéroxidov oxidáciou alkylaromatických alebo cykloalkylaromatických uhlovodíkov s molekulovým kyslíkom v kvapalnej fáze, ktorého podstata spočívá v tom, že ako katalyzátory sa používajú nepřechodné alebo přechodné kovy připadne lantanidy vo formě polynukleárnych komplexov, fyzikálně alebo chemicky viazané na organické alebo anorganické nosiče.. These drawbacks are substantially eliminated by the process for the preparation of hydroproxides by oxidation of alkylaromatic or cycloalkylaromatic hydrocarbons with molecular oxygen in the liquid phase, which consists in the use of transition metals or transition metals or lanthanides in the form of polynuclear complexes, physically or chemically bound to the catalysts. inorganic carriers.
Účinok katalyzátorov možno zvýšiť prítomnosťou malých koncentrácii termicky málo stálých látok, ako sú azozlúčeniny, peroxidy, hydroperoxidy vo východiskovom uhlovodíku. Neznižuje sa tým celková selektivita procesu, ale oxidačně rýchlosti podstatné narastajú. Oxidácia uhlovodíkov sa uskutočňuje v dobře chladených reaktoroch s intenzívnym stykom oxidačného plynu a kvapaliny. Teploty oxidácie sú závislé od oxidujúceho sa uhlovodíka. Ako oxidačně činidlo je možno použit kyslík alebo vzduch. Na neutralizáciu kyslých vedlajších produktov, ktoré katalýzu jú heterolyticky rozpad peroxidov na fenol je možné použit zásadi196648 tých látok, ktoré ich neutralizujú. Výběr alkylaromatických alebo cykloalkylaromatlckých uhiovodíkov prakticky nie je obmedzený, Podstatou je, aby alkylaromatický uhlovodík obsahoval na jadre aspoň jeden uhlovodíkový reťazec v ktorom je vodíkový atóm viazaný na terciárny uhlíkatý atóm. V případe cykloalkylaromatických uhlovodíkov, kde dochádza k oxidácii cyklanlckého kruhu, je táto podmienka spravidla splněná, Přiklad 1 'The effect of the catalysts can be increased by the presence of small concentrations of thermally low stable substances such as azo compounds, peroxides, hydroperoxides in the starting hydrocarbon. This does not reduce the overall process selectivity, but the oxidation rates increase substantially. The oxidation of the hydrocarbons takes place in well-cooled reactors with intense contact of the oxidizing gas and the liquid. The oxidation temperatures are dependent on the oxidizing hydrocarbon. Oxygen or air may be used as the oxidizing agent. To neutralize the acidic by-products which catalyses the heterolytic decomposition of peroxides to phenol, bases may be used to neutralize them. The choice of alkylaromatic or cycloalkylaromatic hydrocarbons is practically not limited. It is essential that the alkylaromatic hydrocarbon contain at least one hydrocarbon chain at the core in which the hydrogen atom is bonded to the tertiary carbon atom. In the case of cycloalkylaromatic hydrocarbons where the cyclanyl ring is oxidized, this condition is generally met, Example 1 '
Skleněný reaktor objemu 150 ml s intenzívnym premiešavaním kvapaliny sa naplní kuménom, ktorý obsahuje 0,1 °/o hm. kuménhydroperoxidu ako iniciátora. .Zmes sa oxiduje -pri teplote 110 °C s kyslíkom. Po 475-tich minútach sa reakcia preruší a oxidačná zmes sa analyzuje. Analýzou sa zistilo, že obsahuje 27,1 % hmotnostných kuménhydroperoxidu, 2,25 % hmotnostných kumylalkoholu a stopy acetofenónu. Selektivita reakcie bola 92,4 °/o.A 150 ml glass reactor with vigorous liquid stirring is filled with cumene containing 0.1% w / w. cumene hydroperoxide as initiator. The mixture is oxidized at 110 ° C with oxygen. After 475 minutes, the reaction was stopped and the oxidation mixture was analyzed. Analysis revealed that it contained 27.1% by weight of cumene hydroperoxide, 2.25% by weight of cumyl alcohol and traces of acetophenone. The selectivity of the reaction was 92.4%.
Příklad 2Example 2
Postup rovnaký ako v příklade 1, ale oxidačná zmes obsahovala komplexný katalyzátor Obsahujúci 0,95 % železa a 0,15 °/o médi, a to v koncentrácii 0,23 % hmotnostných. Po 400 minútach oxidácie vznikloThe procedure was the same as in Example 1, but the oxidation mixture contained a complex catalyst containing 0.95% iron and 0.15% media at a concentration of 0.23% by weight. After 400 minutes oxidation was formed
29.3 °/o hmotnostných kuménhydroperoxidu a 1,67 % hmotnostných kumylalkoholu. Selektivita reakcie bola 94,6 %.29.3% by weight of cumene hydroperoxide and 1.67% by weight of cumyl alcohol. The selectivity of the reaction was 94.6%.
Příklad 3Example 3
Podmienky ako vxpríklade 2, ale ako katalyzátor sa použil komplex olova v koncentrácii 0,27 % hmotnostných. Selektivita reakcie bola 92,3 %.Conditions as in Example 2, x, but the catalyst used is a complex of lead at a concentration of 0.27% by weight. The selectivity of the reaction was 92.3%.
Příklad. .4Example. .4
Za intenzívneho miešania sa oxidovalIt was oxidized with vigorous stirring
PREDMETSUBJECT
1. Spůsob přípravy hydroperoxidov oxidáciou alkylaromatických alebo cykloalkylaromatických uhiovodíkov s molekulovým kyslíkom v kvapalnej fáze, vyznačujúci sa tým, že ako katalyzátory sa používajú nepřechodné alebo přechodné kovy, připadne lantanidy vo formě polynukleárnych komplexov, fyzikálně alebo cheI 4 .· cyklohexylbenzén pri teplote 115 °C kyslíkom. Na iniciáciu reakcie sa na začiatku přidal kuménhydroperoxid v množstve, aby jeho koncentrácia v zmesi bola 0,3 % hmotnostných. ' Po 370-tích minútach oxidácie vznikol cyklohexylbenzénhydroperoxid v množstve 2,8 % hmotnostných.Process for the preparation of hydroperoxides by liquid-phase oxidation of alkylaromatic or cycloalkylaromatic hydrocarbons with molecular oxygen, characterized in that the catalysts used are transition metals or transition metals or lanthanides in the form of polynuclear complexes, physically or chelated at 115 ° C. oxygen. To initiate the reaction, cumene hydroperoxide was initially added in an amount such that its concentration in the mixture was 0.3% by weight. After 370 minutes of oxidation, cyclohexylbenzene hydroperoxide was formed in an amount of 2.8% by weight.
Příklad 5Example 5
Podmienky ako v příklade 4, ale ako katalyzátor se přidal komplex antimónuv množstve 0,25 % hmotnostných. Po 560-tich minútach oxidácie vznikol cyklohexylbenzénhydroperoxid v množstve 10,1 % hmotnostných.Conditions as in Example 4, but the antimony complex was added as a catalyst in an amount of 0.25% by weight. After 560 minutes of oxidation, cyclohexylbenzene hydroperoxide was formed in an amount of 10.1% by weight.
Výhody spůsobu přípravy hydroperoxidov katalyzovianou oxidáciou alkylaromatických alebo cykloalkylaromatických uhiovodíkov s molekulovým kyslíkom v kvapalnej fáze, spočívajú okrem iného v tom, že katalyzátory, používané v spůsobe podía vynálezu, sú chemicky stabilně, lahko skladovatelné a nehořlavé látky. Roztoky peroxidov a hydroperoxidov v inertných organických rozpúšťadlách v koncentrácii do 50 % hmotnostných nerozkladajú ani pri teplotách nad 100 °C. Katalyzujú oxidáciu uhiovodíkov na zodpovedajúce hydroperoxidy, pričom zvyšujú tak reakčné rýchlosti, ako aj selektivitu reakcie. Tým, že ide o heterogénne formy katalyzátora pri ich používaní je výhoda v tom, že z vel'kej časti zotrvávajú v oxidačnom reaktore aj po vypuštění oxidačněj zmesi, čiže v jednotlivých oxidáčných cykloch sa používá len také množstvo čerstvého katalyzátora, ktorým sa doplňajú straty z predchádzajúcich cyklov.The advantages of the process for the preparation of hydroperoxides by catalytic liquid-phase oxidation of alkylaromatic or cycloalkylaromatic hydrocarbons with molecular oxygen are, inter alia, that the catalysts used in the process of the invention are chemically stable, readily storable and non-flammable substances. Solutions of peroxides and hydroperoxides in inert organic solvents at concentrations up to 50% by weight do not decompose even at temperatures above 100 ° C. They catalyze the oxidation of hydrocarbons to the corresponding hydroperoxides, increasing both reaction rates and selectivity of the reaction. Being heterogeneous forms of catalyst in their use, the advantage is that they largely remain in the oxidation reactor even after the oxidation mixture has been discharged, so that only one amount of fresh catalyst is used in the individual oxidation cycles to supplement losses from the catalyst. previous cycles.
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Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS747476A CS196648B1 (en) | 1976-11-19 | 1976-11-19 | Method of preparing hydroperoxides |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS747476A CS196648B1 (en) | 1976-11-19 | 1976-11-19 | Method of preparing hydroperoxides |
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| Publication Number | Publication Date |
|---|---|
| CS196648B1 true CS196648B1 (en) | 1980-03-31 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CS747476A CS196648B1 (en) | 1976-11-19 | 1976-11-19 | Method of preparing hydroperoxides |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2117005C1 (en) * | 1997-06-20 | 1998-08-10 | Акционерное общество "Нижнекамскнефтехим" | Method of preparing ethyl benzene hydroperoxide |
| RU2128647C1 (en) * | 1998-03-24 | 1999-04-10 | Акционерное общество "Нижнекамскнефтехим" | Ethylbenzene hydroperoxide production process |
-
1976
- 1976-11-19 CS CS747476A patent/CS196648B1/en unknown
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2117005C1 (en) * | 1997-06-20 | 1998-08-10 | Акционерное общество "Нижнекамскнефтехим" | Method of preparing ethyl benzene hydroperoxide |
| RU2128647C1 (en) * | 1998-03-24 | 1999-04-10 | Акционерное общество "Нижнекамскнефтехим" | Ethylbenzene hydroperoxide production process |
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