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Pavlov O.S.,Science and Technology Center for Chemical Engineering | Kulov N.N.,RAS Kurnakov Institute of General and Inorganic Chemistry | Pavlov D.S.,Science and Technology Center for Chemical Engineering | Pavlov S.Yu.,Science and Technology Center for Chemical Engineering
Theoretical Foundations of Chemical Engineering | Year: 2012

To produce alkyl(C1-C2)-tert-alkyl(C4-C7) ethers, different process designs are necessary depending on the raw materials and production rate. New production processes using catalytic distillation and cocurrent reactors are described and compared with conventional processes. The justification of the choice of efficient flow diagrams, reactors, and new methods for recovering C1-C2 alcohols from hydrocar- bon product streams is given. © Pleiades Publishing, Ltd., 2012. Source


Pavlov O.S.,Science and Technology Center for Chemical Engineering | Pavlov D.S.,Science and Technology Center for Chemical Engineering | Pavlov S.Yu.,Science and Technology Center for Chemical Engineering
Theoretical Foundations of Chemical Engineering | Year: 2011

Equations are proposed for the kinetics of heterogeneous catalytic liquid-phase reactions that allow for the Langmuir-Hinshelwood sorption concept and the concept of local concentrations and equations for activity coefficients in homogeneous and separating systems based on the combination of the Wilson and Margules concepts. © 2011 Pleiades Publishing, Ltd. Source

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