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Miloš Bogataj

Researcher at University of Maribor

Publications -  26
Citations -  361

Miloš Bogataj is an academic researcher from University of Maribor. The author has contributed to research in topics: Process integration & Circular economy. The author has an hindex of 8, co-authored 24 publications receiving 317 citations.

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Synthesis of non-isothermal heat integrated water networks in chemical processes

TL;DR: A new superstructure for heat exchanger network (HEN) synthesis is proposed based on mixed integer non-linear mathematical programming (MINLP) and four relevant examples are presented to illustrate various aspects of the proposed approach.
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Optimal synthesis of heat exchanger networks for multi-period operations involving single and multiple utilities

TL;DR: In this article, a modified version of the stage-wise superstructure of Yee and Grossman (1990) is adapted to the synthesis of heat exchanger networks having multiple periods of operations.
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An alternative strategy for global optimization of heat exchanger networks

TL;DR: A new strategy for global optimization of heat exchanger networks (HENs) is presented, and a concept of stage-wise superstructure augmented by an aggregated substructure is introduced, showing that currently small HEN synthesis problems to global optimality with reasonable computational effort, while good locally optimal solutions can be identified for larger problems.
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Industrial process water treatment and reuse: A framework for synthesis and design

TL;DR: A computer-aided framework for the design of water treatment and reuse networks is proposed, in which optimization methods, problem analysis tools and wastewater engineering knowledge are integrated in a computer- aided environment to facilitate the formulation and solution of the design problems with fair complexity representative of industrial applications.
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Design of the optimal total site heat recovery system using SSSP approach

TL;DR: In this paper, the possibilities of rational energy consumption and energy integration in an existing site for production of specialty chemicals were studied on the basis of real process parameters and computer simulation results.