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      Selective phenol methylation to 2,6-dimethylphenol in a fluidized bed of iron-chromium mixed oxide catalyst with o–cresol circulation

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          Abstract

          Background

          2,6-dimethylphenol (2,6-DMP) is a product of phenol methylation, especially important for the plastics industry. The process of phenol methylation in the gas phase is strongly exothermic. In order to ensure good temperature equalization in the catalyst bed, the process was carried out using a catalyst in the form of a fluidized bed - in particular, the commercial iron-chromium catalyst TZC-3/1.

          Results

          Synthesis of 2,6-dimethylphenol from phenol and methanol in fluidized bed of iron-chromium catalyst was carried out and the fluidization of the catalyst was examined. Stable state of fluidized bed of iron-chromium catalyst was achieved. The measured velocities allowed to determine the minimum flow of reactants, ensuring introduction of the catalyst bed in the reactor into the state of fluidization. Due to a high content of o-cresol in products of 2,6-dimethylphenol synthesis, circulation in the technological node was proposed. A series of syntheses with variable amount of o-cresol in the feedstock allowed to determine the parameters of stationary states.

          Conclusion

          A stable work of technological node with o-cresol circulation is possible in the temperature range of350-380°C, and o-cresol in/phenol in molar ratio of more than 0.48. Synthesis of 2,6-DMP over the iron-chromium catalyst is characterized by more than 90% degree of phenol conversion. Moreover, the O-alkylation did not occur (which was confirmed by GC-MS analysis). By applying o-cresol circulation in the 2,6-DMP process, selectivity of more than 85% degree of 2,6-DMP was achieved. The participation levels of by-products: 2,4-DMP and 2,4,6-TMP were low. In the optimal conditions based on the highest yield of 2,6-DMP achieved in the technological node applying o-cresol circulation, there are 2% mol. of 2,4-DMP and 6% mol. of 2,4,6-TMP in the final mixture, whereas 2,4,6-TMP can be useful as a chain stopper and polymer’s molar mass regulator during the polymerization of 2,6-DMP.

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          Most cited references33

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          Types of gas fluidization

          D. Geldart (1973)
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            Cu–Co Synergism in Cu1−xCoxFe2O4—Catalysis and XPS Aspects

            T. Mathew (2002)
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              • Record: found
              • Abstract: not found
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              Phenol methylation over nanoparticulate CoFe2O4 inverse spinel catalysts: The effect of morphology on catalytic performance

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                Author and article information

                Contributors
                pczukows@pk.edu.pl
                gberkowicz@chemia.pk.edu.pl
                baron@pk.edu.pl
                kandefer@pk.edu.pl
                dariusz.jamanek@ichp.pl
                stefan.szarlik@ichp.pl
                zbigniew.wielgosz@ichp.pl
                maria.zielecka@ichp.pl
                Journal
                Chem Cent J
                Chem Cent J
                Chemistry Central Journal
                Springer International Publishing (Cham )
                1752-153X
                16 September 2014
                16 September 2014
                2014
                : 8
                : 1
                : 51
                Affiliations
                [ ]Cracow University of Technology, Faculty of Chemical Engineering and Technology, ul. Warszawska 24, 31-155 Cracow, Poland
                [ ]Industrial Chemistry Research Institute, ul. Rydygiera 8, 01-793 Warsaw, Poland
                Article
                51
                10.1186/s13065-014-0051-6
                4172955
                fa2549e7-c6b4-4677-be7c-3b65a891e250
                © Żukowski et al.; licensee Chemistry Central Ltd. 2014

                This is an Open Access article distributed under the terms of the Creative Commons Attribution License ( http://creativecommons.org/licenses/by/4.0), which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly credited. The Creative Commons Public Domain Dedication waiver ( http://creativecommons.org/publicdomain/zero/1.0/) applies to the data made available in this article, unless otherwise stated.

                History
                : 25 April 2014
                : 4 August 2014
                Categories
                Research Article
                Custom metadata
                © The Author(s) 2014

                Chemistry
                2,6-dimethylphenol,fluidized bed,iron-chromium catalyst
                Chemistry
                2,6-dimethylphenol, fluidized bed, iron-chromium catalyst

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