Abstract: The present invention is a aroma recovery equipment from gases exhausted of fermentation vats comprising a first recovery group (100) comprising a first condenser (110) operating at a first temperature of recovered aromas; one second recovery group (200) comprising a second condenser (210) operating at a second temperature of recovered aromas; a cooling group (300) to provide cold by a cooling fluid (301) to said first recovery group (100) via a first fluid connection (302) and to said second recovery group (200) via a second fluid connection (303); control means (400) configured to coordinately control the temperature of said first recovery group (100) and the temperature of said second recovery group (200); and a mobile housing (500) containing said first recovery group (100), said second recovery group (200), said cooling group (300) and said control means (400).

Abstract: A computational method of modeling a bioreactor combines mechanistic models of kinetics of metabolic fluxes and flux balance analysis to predict cell culture performance. The mechanistic models include effects of process variables descriptive of extracellular environment, e.g., temperature, acidity, osmolarity, and/or metabolite concentrations. The method constrains flux rates based on the mechanistic models and computes the flux rates in view of suitable metabolic objectives. The method simulates time evolution of process variables of the bioreactor based on user input and computes performance metrics to display to the user, to control a bioreactor, and/or to train an artificial intelligence model of a bioreactor.

Abstract: The present invention is a aroma recovery equipment from gases exhausted of fermentation vats comprising a first recovery group (100) comprising a first condenser (110) operating at a first temperature of recovered aromas; one second recovery group (200) comprising a second condenser (210) operating at a second temperature of recovered aromas; a cooling group (300) to provide cold by a cooling fluid (301) to said first recovery group (100) via a first fluid connection (302) and to said second recovery group (200) via a second fluid connection (303); control means (400) configured to coordinately control the temperature of said first recovery group (100) and the temperature of said second recovery group (200); and a mobile housing (500) containing said first recovery group (100), said second recovery group (200), said cooling group (300) and said control means (400).