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Hitoshi Kosuge

Researcher at Tokyo Institute of Technology

Publications -  40
Citations -  438

Hitoshi Kosuge is an academic researcher from Tokyo Institute of Technology. The author has contributed to research in topics: Distillation & Mass transfer. The author has an hindex of 11, co-authored 40 publications receiving 407 citations.

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Study on removal of cadmium from wastewater by emulsion liquid membrane.

TL;DR: To determine the optimum operation conditions, the effect of several parameters such as surfactant concentration, carrier concentration, pH of external and internal phases, oil to internal phase volume ratio, emulsion to external phaseVolume ratio, solvent type, solute concentration, presence of iodide and chloride in external phase, and mixing conditions have been investigated.
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Isobaric vapor-liquid-liquid equilibria with a newly developed still

TL;DR: In this article, a new and simple apparatus for the measurement of isobaric vapor-liquid-liquid equilibrium (VLLE) is developed by modifying the still proposed by van Zandijcke et al.
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A correlation method for isobaric vapor–liquid and vapor–liquid–liquid equilibria data of binary systems

TL;DR: In this article, a correlation method for isobaric VLE and VLLE of binary systems was proposed, taking the coordination number in UNIQUAC model as a fitting parameter and employing an objective function of relative difference between the experimental and the predicted temperatures of VLE data.
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Simulation and optimization of heterogeneous azeotropic distillation process with a rate-based model

TL;DR: In this article, a rate-based simulation method for sieve tray columns is developed with the correlations of clear liquid height and mass transfer rate that were obtained in previous experiments of the homogeneous and heterogeneous ternary distillation with a Sieve tray column.
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Vacuum fermentation integrated with separation process for ethanol production

TL;DR: In this paper, continuous fermentation integrated with separation process at atmospheric and vacuum pressures is investigated, where an initial glucose concentration of 200gL¹ was used to produce yeast cells under batch operating mode.