the present invention provides a novel solvent extraction means for production of fragrance components . unlike currently used solvent extraction methods , the present invention utilizes as its solvent an organic ester , particularly a volatile organic ester . by volatile in the present context is meant an ester having a boiling point no higher than about 130 ° c . useful esters for the present purpose are represented by the formula ch 3 coor , where r ═ ch 3 , c 2 h 5 , c 3 h 7 , c 4 h 9 or c 5 h 11 . a particularly preferred ester for this purpose is ethyl acetate , because of its greater volatility ( a boiling point of about 77 ° c ., similar to the more traditional solvent used in this process ). however , other esters of the noted formula , for example isobutyl acetate , which may have higher boiling points , can also provide the same result , but with somewhat greater effort required to remove the solvent , with the risk of loss of some top notes in the process . although ethyl acetate is of course a well known solvent which is frequently used in preparing extracts of plants for the isolation of biologically active materials , such as proteins , polysaccharides and the like , it has not , to the inventors &# 39 ; knowledge , previously been used in the isolation of fragrance components . indeed , given the generally oily or non - polar characteristics of the bulk of fragrance components , it is somewhat counterintuitive to use a polar solvent such as ethyl acetate to extract these materials from plants . it does , however , not only effectively yield the same typical fractions of aroma materials as the non - polar solvent extraction , but it unexpectedly gives a substantially higher yield , up to two to three times that achieved with a traditional hexane extraction . more importantly , the resultant fractions obtained are also of a very different character than those obtained with a hexane , toluene or benzene extraction , having different physical characteristics , being overall more aromatic , and having a different odor profile than the same fractions obtained with petrochemical solvent extraction . of particular advantage is the fact that extracts made by this method can certified organic . ethyl acetate is an organic ester obtainable by the reaction of two natural substances , ethyl alcohol and vinegar . thus , aroma components isolated in this manner do not contain undesirable petrochemical residues that make other commercially available concretes , waxes or absolutes undesirable to a certain segment of the fragrance industry , and make them further unable to be certified as organic . the method of extraction of the plant material is relatively straightforward . plant material known to contain the aroma components of interest are gathered . these can be any portion of the plant , e . g ., flowers , stems , leaves , or roots . porous plant material , such as leaves and flowers , can be used whole or ground , while non - porous materials , such as nuts or seeds , must be ground before extraction . the plant material is then immersed in the ester solvent and allowed to reside together for a short period of time , as short as 15 seconds , but typically no more than five to ten minutes . longer residence times of 30 - 60 minutes , which are more typical of a hexane - based process , result in the extraction of materials that may be incompatible with other aroma ingredients , such as certain essential oils . in this wash , the ratio of the solvent to plant material is not critical , and may be just enough to cover the plant material . as one example , however , if a relatively light material , such as flowers are being used , about 3 kilograms of solvent to every kilogram of plant material provides good results . the ratio can be altered depending on the density of the source material , so that with very dense materials , less solvent can be used , and with lighter material , more solvent may be used . generally speaking , the use of more solvent results in the extraction of more material faster . however , there is no criticality in these amounts , as the only limitation is the ability to remove the solvent at the end of the process . after immersion , the solvent fraction and the plant fraction of the mixture are then separated . surprisingly , and unlike a hexane extraction , a large quantity of aromatic material can be extracted in the very short , single exposure as described above , and no further washes are necessary to obtain an acceptable yield . however , it is possible , if desired , to expose the plant fraction to a second solvent wash , again for no more than 5 minutes , this time with about a 2 : 1 ratio of solvent : plant , and the two fractions separated . optionally , a third washing of the plant material is conducted , for a slightly longer period , e . g ., at least about 10 minutes , with a solvent : plant ratio of about 1 : 1 . if multiple washings are performed , these will be combined for the following steps . it should be noted , however , that there will not ordinarily be a very significant increase in yield with multiple washings , as the first washing extracts so much of the aromatic material . after washing ( s ), the plant material is discarded , and then the solvent evaporated from the washing ( s ), leaving a concrete . the concrete is a mixture of waxes and aromatic materials , which can be used as - is ( as can any waxes further purified from the concrete or the remaining extract ) in cosmetic products , such as lipsticks or lotions , in the same manner as other waxes are used , to modify physical properties , such as viscosity or structure , but with the added advantage of providing aroma at the same time . in an alternate embodiment , all or a portion of the concrete obtained can also be further treated to isolate the absolute and wax fractions , by washing at least once with alcohol , followed by chilling and filtration . a single wash will result in extraction of a significant portion of the aromatic material , but multiple washings , preferably at least two , will ordinarily increase the efficiency of the separation . ethanol is the preferred alcohol for this stage , but the alcohol may be any monohydric or polyhydric alcohol , for example , isopropanol or propylene glycol , that is consistent with a cosmetic and / or fragrance end use of the final product . it is preferred that the alcohol used be relatively volatile ; however , if the evaporation of the solvent is not essential for the intended end use , then a non - volatile solvent , such as glycerine , could also be used , on the understanding that the non - volatile material will significantly dilute the final absolute . a chilling step after the wash results in a separation out of a wax fraction , which can then be separated from the alcohol wash , for example by filtration . the resulting alcohol fraction is then evaporated off to produce the absolute , which may be optionally filtered to remove any remaining small solids . an exemplary procedure for this washing process is as follows : 10 parts of 200 proof alcohol is added for every part of concrete . the mixture is mixed with a propeller mixture at room temperature for about an hour , then chilled with slow mixing to − 30 ° c . the mixture is filtered to clarity . the solid extract is then added back to the mixing vessel , and additional alcohol is added , typically about 8 parts alcohol to one part of solid extract . the mixing , chilling and filtering steps are repeated , then a third washing , with about 6 parts alcohol to one part solid extract , is performed . those skilled in the art will readily recognize that the conditions of foregoing procedures are not necessarily critical , and can be modified , for example , as to residence time in solvent , ratio of solvent to material , number of washes , and the like ; modifications may result in a difference in ultimate yield but will nonetheless result in qualitatively similar products at the end of the procedure . the resulting fractions , i . e ., concretes , waxes and absolutes are , as noted above , unexpectedly chemically distinct from a corresponding petrochemical solvent extract of the same material . initial observations on the fragrance qualities of the absolutes by an expert perfumer showed a very distinct difference qualitatively between hexane derived extracts and ethyl acetate derived extracts . this suggested that perhaps there may be a chemical difference in the composition of the extracts as well . in order to confirm this hypothesis , the two types of extracts were subjected to a gc / ms analysis . the results , repeated with several different types of floral extracts , do in fact show that the chemical components of hexane extracts differ significantly from the ethyl acetate extracts . these differences are found both in proportions of components common in both , as well as the overall identity of the components in each . for example , with jasmine extracts , a total of 60 components are found between the two abstracts , with only seven being found in both extracts , and even in the case of commonly found components , these are found , in some cases , in vastly different amounts . a more detailed analysis of these experiments is provided in example 3 below . another observation is that absolutes prepared in the manner of the present invention will typically show a lower indole content than the corresponding petrochemically isolated absolute . this can be quite important because the indole portion of a fragrance is also referred to the “ animalic content ”, conveying a character to a fragrance that is specifically not desired in a high quality floral . in addition , similar tests show a higher benzyl acetate content in the hexane extraction . another distinction is the concentration of waxes obtained in this extraction procedure is significantly higher than that observed with the hexane extract . because the waxes themselves have a cosmetic utility separate from that of the absolutes ( i . e ., any cosmetic or pharmaceutical use that waxes are normally put to ), this provides an added efficiency to the process . in addition , the character of the waxes obtained is distinct : the waxes produced by the ethyl acetate process are generally darker and more aromatic than the typical hexane process waxes . thus , the results observed confirm that each of the fractions obtained from the process is a unique product , chemically distinct from comparable fractions obtained by more traditional petrochemical - based extraction procedures . the plant source for extraction can be any type of plant which is useful as a source of aroma components . these include , for example , fruits ( strawberry , apple , melon , lemon , lime , orange , and grapefruit ), herbs or leaves ( e . g ., tomato , basil , patchouli , citrus , sage , violet , rosemary or hay ), seeds ( e . g ., coriander , caraway , cocoa , tonka , nutmeg , mace cardamom , and anise ), spices ( star anise , pepper , allspice ), woods ( e . g ., birch , cedar , sandalwood , juniper , larch and pine ), barks ( e . g ., cinnamon ), roots ( e . g ., ginger , vetiver or iris ) and flowers . it is particularly advantageous , however , when applied to flowers , because of the typical difficulty in obtaining good quality essential oils from flowers , combined with the great demand for floral components and the great expense associated with them . an essential oil is ordinarily defined as the oil obtained by steam distillation of a plant material . peppermint , sandalwood , basil , and rose oils are all essential oils , obtained by steam distillation ; in some cases , although not all , rose being a notable exception , the essential oils are the richest and most complex , and therefore , most important , aroma component of a particular plant . many flowers , however , will not yield an essential oil by steam distillation . jasmine is perhaps the best known of these flowers . attempts at steam distillation of jasmine flowers results in a water condensate that smells nothing like the flowers , with no essential oil . the only way to get the aroma out of jasmine flowers is by extracting it with a solvent , which heretofore has always been petrochemical , and therefore unacceptable to some consumers . advantageously , the present invention now for the first time provides the means by which an essential oil can be obtained from certain plant sources without the use of petrochemical solvents . as an added benefit , the present method provides a greater yield of certain fractions . in comparable extractions , the yield of the concrete is significantly higher for the ethyl acetate concrete compared to the hexane concrete ( see example 2 below ). the yield of aromatic absolute is about the same for the ethyl acetate process as for the hexane process , so that the increase in the amount of concrete is represented in the higher amount of waxes that are extracted by the ethyl acetate . this is particularly unexpected , since waxes are generally nonpolar , and yet the present process extracts more of them with a solvent that is more polar than the petrochemical solvents , and with a shorter solvent residence time . in addition , the processing costs for achieving this result are substantially the same as those incurred with the use of hexane , thus in effect reducing the costs of the final products . perhaps more importantly , however , the method also provides a means for getting organically certifiable floral fragrances , something that has heretofore not been achievable with more than a handful of floral sources , because of the damaging effects of steam distillation on floral oils . this more natural quality of the fragrance components can be an important feature both to perfumers as well as aromatherapists , and will also enhance the enjoyment of the fragrance by the ultimate consumer of the product . examples of flowers that are sources of popular aroma components , and which will be useful in this extraction procedure include , but are not limited to rose , jasmine , orange blossom , carnation , geranium , mimosa , tuberose , violet , lavender , lilac , honeysuckle , blue chamomile , orchids and muguet . although the present method is particularly important in isolating aroma components from flowers or floral parts , it will also be appreciated that it can be employed with any plant material containing aroma or wax components soluble in the volatile ester . examples of other useful plant sources include trees , shrubs , herbs and vegetables , and the plant parts used for extraction may be any plant part , including , but not limited to , fruits , berries , leaves , stems , twigs , bark , wood , buds , seeds , roots , and pods . examples of natural sources of fragrance components can be found , for example , in perfumery , practice and principles , calkin and jellinek ( 1994 ), or perfumery and flavoring materials , bedoukian ( 1995 ), the contents of each being incorporated herein by reference . the concretes , absolutes and waxes produced by the method can be used in a number of ways in fragranced products . each can be used atone , in combination with each other , or in combination with one or more components appropriate to their intended end use , for example , for cosmetic or pharmaceutical use , with a topically acceptable carrier . examples of products in which the components can be used are personal care products such as perfumes , colognes , fragranced body sprays and splashes ; products for application to the hair , such as shampoos , conditioners , setting gels , hair sprays and the like ; products for application to the skin , such as cosmetic creams , lotions , milks , sticks , glosses , gets and powders ; or color cosmetics , such as lipsticks , lip glosses , foundations , blushes , eyeshadows , eyeliners or mascaras ; home fragrance products , such as candles , room sprays , fragrance diffusers , wax tarts , incense , and the like ; and aromatherapy products , such as fragranced massage oils . the preparation of such products is well known in the art ; for example , formulations of cosmetic and pharmaceutical compositions are described in harry &# 39 ; s cosmeticology , eighth edition , m . reiger , ed . ( 2000 ), and remington : the science and practice of pharmacy , twentieth edition , a . gennaro , ed ., ( 2003 ) the contents of each of these being incorporated herein by reference . the components produced by the present method can be readily used in any such types of formulations in place of traditionally prepared components . the skilled artisan will readily recognize other applications of the aroma components produced by the present invention , and will further recognize that they can be used in any context in which traditional fragrance components can be used . 25 kilos of jasmine flowers are packed into a wire basket and compressed , but not so much that a solvent cannot penetrate into and flow through them . the basket is immersed into a steam jacketed stainless steel tank containing just enough room - temperature ( approximately 22 - 27 ° c .) ethyl acetate to cover the flowers completely . the combined components are not agitated after 15 seconds , the wire basket with jasmine flowers is removed from the solvent , the solvent is allowed to drain off for about one minute , and the flowers discarded . the extract solution is heated to 60 - 70 ° c . and mixed slowly until most of the ethyl acetate is removed . the evaporated ethyl acetate may be passed through a condenser and collected for re - use . when the extract is condensed to the point where it is about 50 % ethyl acetate , the extract is chilled to minus 20 ° c . and the extract is held for at least 15 minutes , which precipitates out the bulk of the waxes , leaving an extract with some additional waxes , ethyl acetate and aroma compounds . a small amount ( about 10 % of the quantity of the extract ) of 200 proof ethanol is added to the extract and mixed until uniform ( approximately 15 minutes ). the extract is added to a vacuum distillation unit and heated to 40 - 50 ° c . a moderate vacuum ( 20 - 100 mm mercury ) is applied to remove the rest of the ethyl acetate . at this stage , the extract represents a concrete , minus some of the waxes that were initially removed . the extract can then be transferred to a stainless steel jacketed tank and add 10 parts of 200 proof alcohol for every 1 part of extract , in order to separate aromatic components from waxes . the components are mixed with a propeller mixer at room temperature for 1 hour , then chilled with slow mixing to minus 30 ° c . the extract is filtered to clarity . the solid extract from the filter is added back to the tank and 8 parts of alcohol to 1 part solid extract is added . mixing , chilling and filtering is repeated . a third time repetition of the washing , with 6 parts alcohol to 1 part extract , is then performed . alcohol washings are placed in a vacuum distillation unit and warmed to 40 - 55 ° c . moderate vacuum ( 20 - 100 mm mercury ) is applied to remove alcohol . the final aromatic ethyl acetate absolute is the dark brown pasty material left after removal of the alcohol , while the remaining solid extract represents the wax fraction . one kilo of jasmine flowers is extracted by the traditional hexane process ( 3 washes at room temperature , 15 minutes soaking time each , then evaporate off the solvent ) to produce approximately 2 . 5 grams of concrete . the concrete is then extracted with ethanol , similar to the procedure described above . the yield of absolute is approximately 1 . 3 grams . one kilo of jasmine flowers is extracted with ethyl acetate by the process in example 1 to produce approximately 6 grams of concrete , the larger amount of concrete representing a higher level of waxes extracted by this process as opposed to the hexane process . the concrete is then further extracted with ethanol as per example 1 to produce approximately 1 . 2 grams of absolute , the remainder being waxes . this example illustrates the qualitative and quantitative differences between hexane - extracted and ethyl acetate - extracted absolutes hexane and ethyl acetate absolutes of different flowers are prepared substantially as disclosed above in example 2 . in a qualitative evaluation by an expert perfumer , a jasmine hexane absolute is found to have a rich , fine , sweet floral note , whereas the jasmine ethyl acetate absolute exhibits a light floral note with a less smooth sweetness . similarly , violet leaves hexane absolute possesses a very fresh , light cucumber green note , whereas a violet leaves ethyl acetate absolute has a very heavy green note , similar to that of oakmoss , with no cucumber green . these qualitative observations are followed by an evaluation of the quantitative differences between the absolutes produced by different extractions . the comparison is made by gas chromatography / mass spectrometry . the system consisted of an agilent 6890n gc with a hp1ms ( nonionic ) column made by j & amp ; w , and an agilent 5973 mass spectrometer . the runs are done with a temperature ramp of 4 ° c . per minute from 50 ° c . to 250 ° c . jasmine flowers , picked from the same fields and harvested at the same time , were extracted with hexane and ethanol or ethyl acetate and ethanol . a gc / ms analysis finds 60 compounds that can be identified and quantified . of these , only seven are found in both absolutes ; the other 54 are found in one absolute but not the other . all seven of the compounds common to both extracts ( benzyl acetate , benzyl benzoate , benzindan - 1 , 2 , 2 - trione 2 - oxime , isophytol , palmitic acid , phytol and dioctyl phthalate ) are found in significantly different concentrations in the two materials . for example , benzyl acetate is found in the hexane absolute at 16 . 99 % but in the ethyl acetate absolute at only 0 . 98 %. benzyl benzoate ( another compound common to many flower essences ) is in the hexane absolute at 12 . 6 % but in the ethyl acetate absolute at only 0 . 46 %. thirty - four compounds are found in the hexane absolute only , and 20 compounds are found in the ethyl acetate absolute only . a comparison of orange flower absolutes shows similar results . fifty - eight compounds are identified . nineteen are common to both absolutes , thirty - four are found only in the hexane absolute , and 5 are found only in the ethyl acetate absolute . violet leaves extracts show an even more dramatic difference . of the 15 compounds found in the extracts , only one , octadecadienoic acid , is common to both . eight compounds are found only in the hexane absolute , and 6 are found only in the ethyl acetate absolute . these results explain the dramatic differences observed in qualitative aroma profile , and also unequivocally show that the products of the two different extraction processes are chemically distinct entities .
the present invention relates to a method for producing petrochemical - free aroma components , which comprises extracting aroma components from plant materials with a volatile ester such as ethyl acetate . the method produces unique concrete , wax and absolute components that are useful in all types of fragranced compositions , which compositions , due to the absence of petrochemicals , can be certified as organic .