Patent Description:
In addition to being an essential raw material in the production of pulp and paper, eucalyptus biomass is also a relevant source of value-added compounds.

Among these value-added compounds there are phenolic compounds, which include flavonoids, phenolic acids, aldehydes, cinnamic acids, coumarins and chromones, benzophenones, xanthones and tannins (<NPL>; <NPL>). Phenolic compounds owe their added value to their antimicrobial and antitumor activities, as well as their antioxidant activity. Additionally, its anti-inflammatory, anti-allergic and anti-hemorrhagic effects are reported (<NPL>; <NPL>; <NPL>).

Because of these properties, phenolic compounds are included in herbal medicines and dietary supplements (<NPL>;<NPL>).

Another type of value-added compounds present in eucalyptus biomass are triterpene compounds, such as betulinic acid, betulinic acid, <NUM>-acetylbetulinic acid, <NUM>-acetylbetulinic acid, ursolic acid, <NUM>-acetylurosolic acid, oleanolic acid, <NUM>-acetyloleanolic acid, β-amyrin, α-amyrin, β-sitosterol, α-amyrenone, lupeol (<NPL>; <NPL>. ), which, in turn, have antioxidant, anti-microbial, anti-viral, anti-allergic, anti-pruritic and anti-angiogenic properties (<NPL>).

Another product from eucalyptus biomass is its essential oil, with a typical composition that includes monoterpenes such as <NUM>,<NUM>-cineole (eucalyptol), α-Pinene, β-Pinene, limonene, camphene, p-cymene, and sequiterpenes. such as aromadendrene or globulol (<NPL>), with biological activities proven, for example, anti-microbial, anti-viral, fungicidal, insecticidal, anti-inflammatory, anti-nociceptive, antioxidant and phytotoxic (<NPL>)).

The beneficial characteristics of these families of compounds have led to the development of methods that allow their extraction, either from eucalyptus biomass or from other raw materials of plant origin.

One of the most used methods for phenolic and triterpene compounds is solid-liquid extraction, which consists of bringing the biomass into contact with a solvent such as, for example, water or polar and non-polar solvents or different mixtures thereof. The extraction process can take place at different temperatures, solid/liquid ratios and at different extraction times (<NPL>).

Another common extraction process is the Soxhlet extraction, in which a solvent, or mixtures thereof, is continuously recycled and brought into contact with the biomass, through consecutive cycles of boiling and condensation (<NPL>).

These two extraction techniques are characterized by requiring a high consumption of solvents or their mixtures, and by long extraction times (<NPL>).

There is also the possibility of extraction using supercritical fluids. This technique is faster, more selective for less polar (or non-polar) compounds and, additionally, with a lower environmental impact (<NPL>). However, in general, supercritical extraction requires the use of expensive equipment and its configurations and operations are considered complex (<NPL>).

In turn, hydrodistillation is used for the extraction of essential oils, consisting of the immersion of the raw material in water and exposure to heat up to the boiling point of the mixture, causing the release of the essential oil from the raw material. The compounds are then separated by density difference after condensation of the mixture (<NPL>).

A brief search makes it possible to find different works that describe obtaining extracts rich in value-added compounds from plant biomass, using the aforementioned extraction techniques and solvents.

Patent application<CIT> describes a method for obtaining triterpenoids, such as lupeol and betulinic acid, from plant biomass such as birch bark, which involves the use of at least two organic solvents in extraction processes. Solvents considered in the invention described in this patent application include aromatic hydrocarbons such as xylene, o-xylene, m-xylene, p-xylene, toluene, benzene and combinations thereof, chlorinated solvents such as chloroform and dichloromethane, as well as other organic solvents compounds such as ethyl t-butyl ether and ethyl acetate.

Patent <CIT> describes a method of obtaining a eucalyptus extract, more particularly a fraction rich in mono and sesquiterpene compounds abundant in the essential oil, through several extraction steps involving organic solvents chosen from n-hexane, toluene, dichloroethane, chloroform, ethyl acetate, acetone, methanol, ethanol, propanol, butanol, ethylene glycol, propylene, glycol, butylene glycol and the like.

Patent application <CIT> describes a process for obtaining different compounds from vegetable matter, such as essential oil, phenolic compounds, sugar derivatives, triterpenes compounds and organic acids. The described process involves the application of different extraction steps (two, three or more) with the same type of solvent, or with different choices or mixtures thereof. It is cited, for example, the use of ethyl acetate, sodium hydroxide and hexane solutions.

Patent application <CIT> describes a method for obtaining an extract rich in triterpenic acids from eucalyptus barks, involving the solid-liquid extraction of the bark with hexane and the fractionation of the crude extract by means of an alkaline solution, followed by separation of the aqueous phase, its filtration, acidification and finally isolation of the enriched triterpenic acids.

Patent application <CIT> discloses a method for extracting eucalyptus oil which involves drying the eucalyptus leaves in the shade, treating them with cellulase, and then distilling and extracting the oil.

<CIT> depicts an air freshener composition that uses a combination of specific plant extracts to effectively clean and freshen the air, where the extract is produced by crushing leaves and, adding ethanol and then extracting the resultant mixture using microwave heating and filtering and concentrating the resultant filtrate under reduced pressure.

Academic works report the use of carbon dioxide extractions under supercritical conditions, as is the case of the study by <NPL>) or de Santos et al. (<NPL>) for the extraction of, respectively, triterpene compounds and phenolic compounds from E. globulus bark. In turn, Ferreira and co-authors (<NPL>), describe the extraction of E. globulus leaves with chosen solvents such as chloroform, ethanol and methanol.

Thus, there is a predominance of extraction processes for value-added compounds that use organic solvents and often their mixtures, in several extraction steps. As is well known, organic solvents are toxic to humans, animals and the environment, and there is a growing demand for less adverse alternatives. The existing extraction processes limit the type of extract obtained, and the processes developed are mostly focused on the production of extracts enriched in a certain type of compounds.

It is therefore extremely important to develop an extraction method that allows obtaining different extracts, enriched in certain families of value-added bioactive compounds, with different polarities and different bioactive properties, from the same biomass, maximizing the generation of added value, and which allows for a reduction in the use of organic solvents, both in quantity and in their number and, consequently, also leading to a decrease in the costs involved in the process, with regard to the recovery of organic solvents and reduction of environmental impacts. Moderate temperature and pressure conditions are also desirable. These requirements are satisfied by the process described in this patent application.

The present invention is directed to an integrated process for extracting bioactive compounds from eucalyptus biomass, comprising the following steps:.

Diagram of the integrated process for simultaneous production of value-added bioactive compounds from eucalyptus biomass as described in this invention. HRW - extract with phenolic compounds obtained from residual water from hydrodistillation; EB - eucalyptus biomass; EEO - eucalyptus essential oil; TT - extract of triterpene compounds.

The invention described in this document concerns an integrated process for the simultaneous production of value-added bioactive compounds from the same eucalyptus biomass, as described in this patent application and claim <NUM>, which allows obtaining a variety of extracts, enriched in specific families of compounds and with different degrees of polarity, using a smaller number and respective amount of organic solvents. The problems of solvent recovery and of possible toxicity and/or environmental contamination are thus minimized. It also allows a reduction in the costs associated with the production of extracts rich in value-added bioactive compounds. The process described in this document involves an integrated process that includes extraction stages, which enhance the production of different extracts, enriched in different families of value-added compounds from the same biomass, and the recirculation of one of the products of this extraction process, reducing the problems associated with the recovery of organic solvents and the associated costs.

In fact, and as detailed below, in the process described here, the base biomass, for example eucalyptus leaves or bark, generates itself the solvent that will then allow the extraction of the triterpene compounds, that is, the essential oil, obtained by hydrodistillation of the original biomass and its subsequent use as a solvent in the sequential extraction of triterpene compounds.

In a preferred embodiment of the invention, the process further comprises a step of drying the hydrodistilled biomass resulting from step c).

In a preferred embodiment of the invention, the extraction of step f) is carried out in a medium acidified by an organic acid.

In a preferred embodiment of the invention, the extraction of step f) is carried out with aliphatic alcohols selected from the group consisting of methanol, ethanol and propanol.

In a preferred embodiment of the invention, the process further comprises a step of purifying the extract of triterpene compounds dissolved in eucalyptus essential oil resulting from step d) until obtaining eucalyptus essential oil and an extract of triterpene compounds.

In a preferred embodiment of the invention, the step of purifying the extract of triterpene compounds dissolved in eucalyptus essential oil is carried out through purification methods, individually or sequentially, selected from the group consisting of filtration, alkaline extraction, acidification and precipitation.

In a preferred embodiment of the invention, the process further comprises a step of purifying the extract of phenolic compounds obtained in step f).

In a preferred embodiment of the invention, the step of purifying the extract of phenolic compounds is carried out through purification methods, individually or sequentially, selected from the group consisting of filtration, evaporation and lyophilization.

In a preferred embodiment of the invention, the process further comprises collecting the eucalyptus essential oil obtained in steps c) and e) for subsequent rectification and/or concentration and/or purification.

In a preferred embodiment of the invention, the process further comprises collecting the extracts with phenolic compounds obtained from the residual water of the hydrodistillation obtained in steps c) and e) for subsequent rectification and/or concentration and/or purification.

Within the scope of the present invention, a bioactive compound refers to compounds present in plant materials with beneficial effects on human health, such as antioxidant, antimicrobial, anti-tumor, anti-inflammatory and anti-allergic effects, among other beneficial effects.

Within the scope of the present invention, extract with phenolic compounds obtained from the residual water of hydrodistillation refers to a non-volatile extract obtained from the residual water resulting from the hydrodistillation process of leaves to collect the essential oil, which has phenolic compounds in its constitution, such as, for example and not limited to flavonoids, phenolic acids, aldehydes, cinnamic acids, coumarins and chromones, benzophenones, xanthones and tannins.

Within the scope of the present invention, essential oil refers to the product obtained after subjecting plant biomass to the hydrodistillation process, where water is evaporated simultaneously with the essential oil and after condensation they are separated into two phases, one of which is the essential oil. This consists of a complex mixture of biologically active compounds.

Selected eucalyptus biomass, leaves, is subjected to hydrodistillation until the production of an extract with phenolic compounds obtained from the residual water of hydrodistillation and an essential eucalyptus oil. The hydro-distilled biomass, that is, after the hydrodistillation process, is dried before its subsequent extraction. Eucalyptus essential oil obtained in the first hydrodistillation is used to extract the leaves resulting from the drying step and/or bark. This extraction results in an extract of triterpene compounds dissolved in eucalyptus essential oil and extracted biomass. This biomass, be it leaves and/or bark, is again hydrodistilled to recover the essential oil that was retained in the biomass of the previous step, obtaining hydrodistilled biomass, eucalyptus essential oil and an extract with phenolic compounds obtained from the residual water of the hydrodistillation.

The resulting biomass is sent to another extraction with water and/or with aliphatic alcohols and/or with mixtures of water and aliphatic alcohols. This last extraction, in addition to the extract rich in triterpene compounds and the constituents of eucalyptus essential oil obtained during the process steps described above, allows for an extract of phenolic compounds to be obtained.

The extract of triterpene compounds dissolved in eucalyptus essential oil and resulting from extraction with the essential oil is subjected to one or more purification processes. The extract of phenolic compounds obtained in the final step is subjected to one or more purification processes.

The different streams of the product ranges obtained in this integrated process, whether from eucalyptus essential oil or from extract with phenolic compounds obtained from the residual water of hydrodistillation, are collected individually and subjected, according to their constitution, to rectification, concentration and/or purification processes.

Different purification processes can be selected, individually or sequentially, among, for example, but not limited to, filtration, alkaline extraction, acidification and precipitation.

The process described in this patent application thus allows the production of a variety of value-added compounds from the same biomass, enabling the recirculation of different by-products and solvents, thus minimizing production costs and subsequent environmental impacts. In fact, one of the products obtained, the essential oil, is used for the extraction, in this integrated process, of another family of products. Triterpene compounds, eucalyptus essential oil, extracts with phenolic compounds obtained from the residual water from hydrodistillation and phenolic compounds are obtained through the sequential and integrated steps of the process in question.

The biomass extracted by hydrodistillation was lyophilized, crushed, and then extracted with the oil, such as eucalyptus essential oil and/or <NUM>,<NUM>-cineole. Approximately <NUM> of eucalyptus leaves and/or bark were extracted with <NUM> of eucalyptus essential oil and/or <NUM>,<NUM>-cineole, at room temperature, protected from light and with stirring for up to <NUM> hours.

Biomass and the liquid fraction (extract enriched in triterpene compounds dissolved in essential oil) were separated by pressing separation process, obtaining an extract rich in triterpene compounds dissolved in essential oil and/or <NUM>,<NUM>-cineole. The total triterpenes content was <NUM> kg-<NUM> of dry biomass, containing <NUM> kg-<NUM> of ursolic acid dry biomass, <NUM> kg-<NUM> of oleanolic acid dry biomass, <NUM> kg-<NUM> of dry biomass of betulinic acid and <NUM>-<NUM> of betulinic acid biomass.

A volume of <NUM> of crude essential oil extract was extracted with <NUM> of <NUM> aqueous sodium hydroxide (NaOH), this L-L extraction being repeated between <NUM> and <NUM> times. The aqueous phase was separated from the organic phase (essential oil and/or cineole) by decanting. It was further centrifuged, and then vacuum filtered through a Whatman <NUM> cellulose filter (<NUM> pm), resulting in a clearer solution. Said solution was acidified to pH < <NUM> with <NUM> sulfuric acid (H<NUM>SO<NUM>), resulting in a precipitated suspension. The precipitate was vacuum filtered, washed with <NUM> of distilled water until neutral pH, and dried at <NUM> for <NUM>.

<NUM> of extract were obtained, consisting of <NUM>% ursolic acid, <NUM>% oleanolic acid, <NUM>° betulinic acid and <NUM>% betulinic acid.

The extracted biomass was sequentially subjected to extraction with water, and/or short chain aliphatic alcohols, and/or mixtures of water and aliphatic alcohols with or without acidification (e.g. with acetic acid), using solvent/biomass ratios, by mass /volume, up to <NUM>:<NUM>, with an extraction time of up to <NUM> and temperatures at least equal to room temperature and up to the boiling temperature of the solvent used.

The solid fraction and the extract rich in phenolic compounds dissolved in the used solvent were separated by filtration, alkaline extraction, acidification and precipitation, and the solid extract obtained by removing the solvent by evaporation, lyophilization and a combination of both.

Overall yields of at least <NUM> % and <NUM> % were observed for extractions with methanol:water and ethanol:water mixtures, respectively, and <NUM> % and <NUM> % for extractions with ethanol and methanol, respectively in terms of kg extract produced per kg of biomass.

Claim 1:
An integrated process for extracting bioactive compounds from eucalyptus biomass, comprising the following steps:
a) selection of leaves of eucalyptus;
b) hydrodistillation of the leaves of eucalyptus for the production of an extract with phenolic compounds obtained from the residual water of hydrodistillation, an essential oil of eucalyptus and a hydrodistilled biomass;
c) separating the extract with phenolic compounds obtained from the residual water of hydrodistillation, the essential oil of eucalyptus and the hydrodistilled biomass obtained in step b) ;
d) extracting the biomass resulting from step c) and/or eucalyptus bark with the eucalyptus essential oil resulting from step c) until obtaining an extract of triterpene compounds dissolved in eucalyptus essential oil and an extracted biomass;
e) hydrodistillation of the extracted biomass resulting from step d) until obtaining an extract with phenolic compounds obtained from the residual water of the hydrodistillation, the eucalyptus essential oil and a hydrodistilled biomass;
f) extraction of the biomass resulting from step e) with water and/or with an aliphatic alcohol and/or with mixtures of water and aliphatic alcohols until obtaining an extract of phenolic compounds and a post-extraction biomass.