Abstract: A process for hydrating a yeast in dehydrated form including the following steps preparing a hydration medium having yeast extract in aqueous solution, at a concentration between 1 g/L and 50 g/L; adding a yeast in dehydrated form to the hydration medium at a concentration between 10 g/L and 200 g/L; the process being carried out at a temperature between 25° C. and 40° C., for a time between 30 minutes and 8 hours. The rehydrated yeast thus obtained may be advantageously used in fermentation processes that allow the production of biofuels usable in diesel or aviation engines such as, ethanol, linear or branched alcohols with different molecular weight, or biochemicals such as, for example, ethanol, glycerol, acetic acid esters (for example, ethyl acetate), arabinitol, lactic acid, succinic acid, microbial oils (bio-oils), or propagated yeast, in particular in fermentation processes carried out in the presence of hydrolyzates deriving from lignocellulosic biomass.

Abstract: An integrated process for producing polyhydroxyalkanoates and bioethanol including: (a) feeding a part of the lignocellulosic hydrolyzate to a first fermentation device in the presence of one microorganism capable of using sugars with six carbon atoms and organic acids, obtaining a first fermentation broth; (b) subjecting the first broth to separation obtaining an aqueous suspension of cellular biomass having one polyhydroxyalkanoate and an aqueous phase having sugars with five carbon atoms in a quantity greater than or equal to 10 g/L; (c) optionally, feeding a part of the aqueous phase from step (b), to a second fermentation device, obtaining a second fermentation broth (inoculum); (d) feeding at least a part of the aqueous phase from step (b) and, optionally, the second broth and/or at least a part of lignocellulosic hydrolyzate, to a third fermentation device, obtaining a third fermentation broth; and (e) subjecting the third broth to separation obtaining bioethanol.

Abstract: The present invention relates to a process for separating natural rubber deriving from non-Hevea type plants, in the form of solid crumbs, from solutions in an organic solvent system including it, where said organic solvent system may comprise at least one nonpolar organic solvent, or a mixture of at least one nonpolar organic solvent and at least one polar organic solvent, and the concomitant removal of said organic solvent system from said rubber, where the aforementioned process comprises subjecting said solution to a stripping stage by means of water vapor, in presence of a dispersing system, separating the aforementioned crumbs of natural rubber from the liquid phase, obtained through the stripping stage, and subjecting said crumbs to drying.

Abstract: The present invention relates to the industrial sector of extracting and processing natural rubber, and other components, from plant material. In particular, the invention relates to a process for extracting latex, resin and rubber from guayule and/or guayule-type plants, which comprises harvest, preservation, mechanical and chemical treatment of the plant parts, which is applicable both in the laboratory and on an industrial scale and is characterised by significantly high yields and high quality of the extracted products.

Abstract: The present invention relates to the industrial sector of extracting and processing natural rubber, and other components, from plant material. In particular, the invention relates to a process for extracting latex, resin and rubber from guayule and/or guayule-type plants, which comprises harvest, preservation, mechanical and chemical treatment of the plant parts, which is applicable both in the laboratory and on an industrial scale and is characterised by significantly high yields and high quality of the extracted products.

Abstract: The present invention relates to a process for separating natural rubber deriving from non-Hevea type plants, in the form of solid crumbs, from solutions in an organic solvent system including it, where said organic solvent system may comprise at least one nonpolar organic solvent, or a mixture of at least one non-polar organic solvent and at least one polar organic solvent, and the concomitant removal of said organic solvent system from said rubber, where the aforementioned process comprises subjecting said solution to a stripping stage by means of water vapor, in presence of a dispersing system, separating the aforementioned crumbs of natural rubber from the liquid phase, obtained through the stripping stage, and subjecting said crumbs to drying.