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Equipment for intensification of the process of oxyethylation of nonionogenic surface-active compounds

  • New Machinery and Equipment
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Chemical and Petroleum Engineering Aims and scope

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Literature cited

  1. N. N. Lebedev, V. P. Savel'yanov, and Yu. I. Baranov, “Pattern of distribution of ethylene oxide during reaction with alcohols and water and estimation of the composition of the end products,” Zh. Prikl. Khim.,42, 1815 (1969).

    Google Scholar 

  2. B. E. Nedbailyuk, S. V. Romanchuk, V. I. Gusev, et al., “Tubular reactor for oxyethylation of higher fatty alcohols with distributed feeding of ethylene oxide,” Khim. Promst., No. 6, 371 (1985).

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  3. I. G. Reznikov, A. V. Kulikova, and A. I. Grebennikova, “Controlled change in the molecular composition of oxyethylated alcohols,” Khim. Promst., No. 1, 15 (1985).

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  4. USA Patent No. 2,988,572.

  5. FRG Patent No. 2,358,874.

  6. Yu. D. Panaev, Yu. N. Kolesnik, and V. G. Pravdin, “Mathematical modelling of the process of oxyethylation of higher fatty alcohols in continuous-process reactors,” in: Sixth All-Union Conference on Modelling of Chemical and Petrochemical Processes and Reactors [in Russian], Dzerzhinsk (1977), pp. 405–414.

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Translated from Khimicheskoe i Neftyanoe Mashinostroenie, No. 6, pp. 9–11, June, 1992.

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Gaivanskii, E.A. Equipment for intensification of the process of oxyethylation of nonionogenic surface-active compounds. Chem Petrol Eng 28, 360–362 (1992). https://doi.org/10.1007/BF01148979

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  • DOI: https://doi.org/10.1007/BF01148979

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