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©R.M. Akhmadullin1*, D.R. Gatiyatullin1, A.G.Akhmadullina1, L.V.Verizhnikov1, T.F. Nigmatullin2+,N.A. Mukmeneva2*, I.A. Karimov3
1 RDC AhmadullinS. Sibirsky Tract 34, b. 10, Kazan, 420029, Republic of Tatarstan. Russian Federation. Phone: 89872734141. E-mail: firstname.lastname@example.org
2Technology of Synthetic Rubber Department, Kazan National Research Technological University, Karl Marx 68, Kazan, 420015, Republic of Tatarstan, Russian Federation. Phone: 89375228344.
3Technology of Engineering Materials Department, Kazan National Research Technological University, Karl Marx 68, Kazan, 420015, Republic of Tatarstan, Russian Federation. Phone:89510666700. E-mail: email@example.com
Keywords: 2,6-di-tert-butylphenol, liquid-phase oxidation, sterically hindered diphenoquinone, sulfuric oxygen-containing organic compounds.
The oxidation of 2,6-di-tert-butylphenol to 3,3′,5,5′-tetra-tert-butyl-diphenoquinone in alkaline medium with sulfuric oxygen-containing organic compounds (dimethylsulfoxide, dimethyl sulfone) and aqueous solution of potassium hydroxide has been studied. An effective alkaline catalyst for 2,6-di-tert-butylphenol oxidation is considered. The alkaline catalyst is based on products of mercaptides oxidation, obtained in process of caustic regeneration of liquefied petroleum gases sweetening from mercaptanes. Elementary and fractional analyses of catalyst has been defined. A comparative analysis of the kinetics of oxidation of 2,6-di-tert-butyl phenol with model reactions have been investigated.
Nowadays there is a following paradoxical situation in Russia: with large volumes of polymers realization as well as a huge planning to expand their production in the next years there is no any strategy for creating and increasing of amount of domestic stabilizers. This time there are only morally outdated stabilizers, which are produced in small values.
According to the information above the problem of creating highly effective domestic stabilizers for polymers which are able to compete with world production of such type is a topical problem.
One of the perspective phenolic antioxidant for industrial application is 4,4′-bis (2,6-di-tert-butylphenol) (BP). It has all positive properties, which are necessary for its widely usage and it is profitably different with its property of different ways of using BP for stabilization of cautchouc, plastics and rubber, as well as fuels and oils [1-5]. According to the Standard 12.1.007-76 the stabilizer 4,4′-bis (2,6-di-tert-butylphenol) is dated back to harmless chemicals and permitted for using in polymers, which are in contact with food products, as well as in polymers of medical supplies.
There are a lot of researches in the special literature, which are dedicated to the ways of preparation of 4,4′-bis (2,6-di-tert-butylphenol) by the oxidation of 2,6-di-tert-butylphenol (MP) to 3,3′,5,5′-tetra-tert-butyl-4,4′-diphenoquinone (DPQ), which is then turned to the desired product BP (scheme 1).
Figure 1.A two-step process of the BP synthesis.
The main condition in the most part of the works on methods of synthesis of DPQ by the oxidation of MP (Step 1, scheme 1) is the presence of a catalyst of alkaline nature. However, the oxidation rate in the alkaline condition of MP remains rather low and the process needs intensification.
The continuation of studies of the development of efficient and low-waste technology of BP’s synthesis remains popular considering the current problems and prospects of using BP.
A bubble type cylindrical reactor is loaded with 50.0 ml toluene, and then added 0.022 mol of MP and 0.0012 mol of DPQ. By the time we rich predetermined temperature (85°C) we add the catalyst and oxygen at a rate of 500 hr-1. The speed of magnetic stirrer is 1400 rpm.
Carrying of analyses. Constructing of kinetic cumulating curve of DPQ performed according to the light absorption of the reaction solution of DPQ in samples with photocolorimetric method on the spectrophotometer Ekros PE5300V at a wavelength λ = 540 nm.
The analysis of component system of reaction feed was held on the Gas Chromatograph – Crystal 5000. The chromatography-mass spectrometry analysis was held to determine the composition of the test POC catalyst (phenols oxidation catalyst). This analysis was held on the instrument GCMS 2010 Plus Shimadzu (Japan). The collection of mass spectra NIST-11 was used to identify the components.
Table. 1. The speciation of the POC catalyst Table. 2. Elemental POC catalyst composition
Table. 3. The contents of the initial components and the final products in the oxidation reaction of MP with oxygen in the presence of catalysts – [16 mol / l] aqueous KOH and POC. The concentration of the catalyst in the reaction mixture is 3.0 wt%.
The element analysis of mixture was held in workstation Auriga Cross Beam (Carl Zeiss). The microscope is equipped with an energy dispersive spectrometer Inca X-MAX (Oxford Instruments) with a resolution of 127 eV.
Results and discussion
The task to increase basement during the reactions of oxidation of MP can be solved by using super base systems, which include sulfoxides and hydroxides of alkaline metals. This was clearly shown in the works of Vitkovskaya N. M., Mc. Gregor, Stuart, O’Donnel and others [9-12]. Stuart and O’Donnel showed  that the hydroxide-ion activity in the water solutions of dimethylsulfoxide increased with the increase of its concentration. Increased reactivity allowed leading base-catalyzed reactions at room temperature or at much lower temperatures. For example, Kram  and others learned that the leading of Volf-Kishner reduction reactions and Coupe elimination can take place at room temperature.
During the searching of common mechanism of nucleophile reactions’ catalyze in the presence of dimethylsulfoxide Kingsburry  showed that increasing of speed takes place even at low concentrations of dimethylsulfoxide and it is caused by changes in enthalpy. The effect here does not depend on the charge of reactants.
The new catalyst system (POC) for oxidation of MP is offered in this work from the position of basicity increase. The POC (table 1) represents water solutions KOH with alkaline concentration of 30% resulting at installation of heterogeneous-catalytic mercaptan removal from butane fraction of the “LUKOIL-Nizhegorodnefteorgsintes” LCC , which contains products of deep oxidation of sulfur compounds.
The method of gas chromatography-mass spectroscopy revealed that POC contains an oxygen organosulfur compounds, such as dimethylsulfoxide, dimethylsulfone, methylmethanethiosulfonate, etc.
The quantity of the sulfur content in the POC catalyst is determined on the base of elemental analysis (Table. 2).
We can compare catalytic activity of POC with aqueous solutions of KOH model (Fig. 1), because POC catalytic system is aqueous alkaline solution based on potassium hydroxide. Experiments show that the guide-potassium hydroxide is the most active in comparison with sodium hydroxide, what, apparently, can be explained by bigger radius of the outer electron shell of KOH.
We can see from pic. 1 that the yield of DPQ depends on catalyst and after 150 min. was: 1 – 9%; 2 – 40%; 3 – 91%.
The high speed oxidation of MP and absence of induction period are mentioned in the presence of a POC catalyst.
Fig. 1. The kinetic curves of DPQ accumulation Fig. 2. Kinetic curves of DPQ accumulation
during MP oxidation reaction in toluene in the during MP oxidation reaction in toluene
dependence on the type of catalyst: dependent on concentration of POC catalyst:
1 – [KOH] = 6.8 mol / l; 2 – [KOH] = 1 – [POC] = 3.0 wt%, 2 – [POC] = 4.4 wt%, 3 –
16 mol / l; 3 – POC ([KOH] = 6.8 mol / l) [POC] = 7.1% mass, 4 -. [POC] = 13.3% wt.
Chromatographic analysis of the reaction mass (Table 3) before and after oxidation of MP in the presence of catalysts – [16 mol/l] aqueous solution of potassium hydroxide and POC showed the following results: conversion of MP in the presence of POC was 99.9%, selectivity according to DPQ – 91% and according to BP – 9%.
It is important to mention here that maximum conversion of MP in the presence of POC catalyst is achieved two times faster in comparison with an aqueous KOH solution under the same conditions.
The investigation of the influence of POC catalyst concentration on the process of MP oxidation showed absence of the induction period and increasing of the initial reaction speed with increasing catalyst concentration (Fig. 2).
To identify the cause of the accelerating action of POC catalyst on the oxidation of MP we studied the influence of dimethylsulfoxide (DMSO) and dimethylsulfone (DMSO2) (Fig. 3a, b), which were identified as part of the POC by the method of gas chromatography-mass spectrometry (Table. 2)
Fig. 3. Kinetic curves of accumulation in DPQ during the MP oxidation reaction in toluene according to the composition of the catalyst system. The catalyst concentration of [16 mol / l] in a KOH solution in the reaction mixture – 3.0% by weight.: a: 1 – without DMSO, 2 – [DMSO] = 0.5% by weight, 3 – [DMSO] = 1.0% by weight. b: 1 – without DMSO2, 2 – [DMSO2] = 1.0 wt%, 3 – [DMSO2] = 2.0 wt.%.
Fig. 4.Kinetic curves of DPQ accumulation during the oxidation reaction of MP in toluene according to the composition of the catalyst system. The catalyst concentration of [16 mol/l] aqueous KOH solution in the reaction mixture – 3.0% wt .: 1 – idle; 2 – [DMSO] = 1.0% wt .; 3 – [DMSO2] = 2.0% wt .; 4 – [DMSO] = 1.0% by weight. + [DMSO2] = 2.0 wt%.
Thus, the meaning of incepted speed of reactions in the model systems in presence of oxygen shows that individual components accelerates the oxidation of MP being the part of the catalyst – aqueous solution of potassium hydroxide (Fig. 3). While concentration of dimethylsulfoxide and dimethylsulfone increases and reaction of catalyst concentration (aqueous solution of potassium hydroxide) remains unchangeable the speed of reaction increases.
In addition, the reaction of oxidation of MP in presence of both components (dimethylsulfoxide or dimethylsulfone) was carried out. In this reaction, the composition of the model alkaline solution to the composition of POC catalyst was approached.
As one can see from the Fig. 4, the co-presence of dimethylsulfoxide or dimethylsulfone in the reaction composition leads to significant acceleration of the MP oxidation and to the absence of induction period. This is typical for the reaction of MP oxidation in the presence of POC catalyst (Fig. 1, 2).
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