New proposal for extracting rosemary compounds: Process intensification and economic evaluation.

This paper brings forward techno-economic results of a study developed with rosemary. Process intensification was applied for obtaining two fractions of bioactive compounds: one fraction rich in volatile oil and other fraction rich in non-volatile extract. Terpenoids as 1,8-cineole and camphor were obtained by supercritical CO 2 extraction (SFE-CO 2 ). Afterwards, phenolic compounds as rosmarinic acid and carnosic acid were obtained by pressurized water extraction (PWE). We performed SFE-CO 2 and PWE in the same multipurpose equipment without unloading the bed. Extraction yields and composition of each extract fraction were evaluated. We obtained approximately 2.5 wt.% of a fraction rich in volatile oil at 40 °C, 30 MPa and solvent mass to feed mass (S/F) ratio of 2.5 g CO 2 /g rosemary. Likewise, we obtained approximately 18.6 wt.% of a fraction rich in non-volatile extract at continuous temperature increase of 1.1 °C/min (from 40 °C to 172 °C), 10 MPa and S/F ratio of 9.5 g water/g rosemary. We simulated costs of manufacturing of extracts obtained by SFE-CO 2 in three productive plants containing 2 vessels of 10 L, 50 L and 100 L. The influence of bed geometry was considered into the simulation model, whereas the bed height (H B ) to bed diameter (D B ) ratios were: H B1 /D B1 = 7.1 and H B2 /D B2 = 2.7. We simulated the productivity of extracts and operating costs for an industrial plant containing 2 vessels of 100 L using the process intensification performed in this paper (SFE-CO 2 + PWE). The proposal is promising and can encourage industrial application, because the higher use of the vegetal matrix for obtaining diversified bioactive compounds can reduce 28% of the annual production costs of SFE-CO 2 + PWE processes whether comparing with SFE-CO 2 process alone. [ABSTRACT FROM AUTHOR]