NOVEL CRYSTALLINE COMPOSITES COMPRISING PHYTOSTEROLS AND PHYTOSTANOLS OR DERIVATIVES THEREOF

Abstract: A novel composite crystalline structure comprising a phytosterol and a phytostanol, or a derivative of either for use in treating or preventing cardiovascular disease and it underlying conditions such as atherosclerosis and hypercholesterolemia.

Description: FIELD OF THE INVENTION This present invention relates to the field of phytosterols and phytostanols and their use in treating and preventing cardiovascular disease, its underlying conditions such as atherosclerosis, hypercholesterolemia, and hyperlipidemia and other disorders. BACKGROUND OF THE INVENTION While recent advances in science and technology are helping to improve quality and add years to human life, the prevention of atherosclerosis, the underlying cause of cardiovascular disease ("CVD") has not been sufficiently addressed. Atherosclerosis is a degenerative process resulting from an interplay of inherited (genetic) factors and environmental factors such as diet and lifestyle. Research to date suggest that cholesterol may play a role in atherosclerosis by forming atherosclerotic plaques in blood vessels, ultimately cutting off blood supply to the heart muscle or alternatively to the brain or limbs, depending on the location of the plaque in the arterial tree (1 ,2). Overviews have indicated that a 1% reduction in a person's total serum cholesterol yields a 2% reduction in risk of a coronary artery event (3). Statistically, a 10% decrease in average serum cholesterol (e.g. from 6.0 mmol/L to 5.3 mmol/L) may result in the prevention of 100,000 deaths in the United States annually (4). Sterols are naturally occurring compounds that perform many critical cellular functions. Phytosterols such as campesterol, stigmasterol and beta-sitosterol in plants, ergosterol in fungi and cholesterol in animals are each primary components of cellular and sub-cellular membranes in their respective cell types. The dietary source of phytosterols in humans comes from plant materials i.e. vegetables and plant oils. The estimated daily phytosterol content in the conventional western-type diet is approximately 60-80 milligrams in contrast to a vegetarian diet which would provide about 500 milligrams per day. Phytosterols have received a great deal of attention due to their ability to decrease serum cholesterol levels when fed to a number of mammalian species, including humans. While the precise mechanism of action remains largely unknown, the relationship between cholesterol and phytosterols is apparently due in part to the similarities between the respective chemical structures (the differences occurring in the side chains of the molecules). It is assumed that phytosterols displace cholesterol from the micellar phase and thereby reduce its absorption or possibly compete with receptor and/or carrier sites in the cholesterol absorption process. Over forty years ago, Eli Lilly marketed a sterol preparation from tall oil and later from soybean oil called Cytellin™ which was found to lower serum cholesterol by about 9% according to one report (5). Various subsequent researchers have explored the effects of sitosterol preparations on plasma lipid and lipoprotein concentrations (6) and the effects of sitosterol and campesterol from soybean and tall oil sources on serum cholesterols (7). A composition of phytosterols which has been found to be highly effective in lowering serum cholesterol is disclosed in US Patent Serial No. 5,770,749 to Kutney et al. and comprises no more than 70% by weight beta-sitosterol, at least 10% by weight campesterol and stigmastanol (beta-sitostanol). It is noted in this patent that there is some form of synergy between the constituent phytosterols, affording even better cholesterol-lowering results than had been previously achieved. Despite the obvious and now well recorded advantages of phytosterols, not only in the treatment of CVD and its underlying conditions such as hypercholesterolemia, hyperlipidemia, atherosclerosis, hypertension, thrombosis but in the treatment of other diseases such as Type II diabetes, dementia cancer and aging, the administration of phytosterols and the incorporation thereof into foods, pharmaceuticals and other delivery vehicles has been complicated by the fact that they are highly hydrophobic (i.e.they have poor water solubility) and they are generally also poorly soluble in oils. The provision of a water and oil-soluble phytosterol derivative which could be administered orally and which could be incorporated without further modification into delivery vehicles would be highly desirable. It is an object of the present invention to obviate or mitigate the above disadvantages. SUMMARY OF THE INVENTION The present invention provides a composite crystalline structure comprising a phytosterol and a phytostanol, or a derivative of either. The present invention further comprises a composition for treating or preventing CVD and its underlying conditions including atherosclerosis, hypercholesterolemia, hyperlipidemia, hypertension, thrombosis, and related diseases such as Type II diabetes, as well as other diseases that include oxidative damage as part of the underlying disease process such as dementia, aging, and cancer which comprises one or more composite crystalline structures comprising phytosterols or phytostanols, or derivatives thereof and a pharmaceutically acceptable or food quality carrier or adjuvant therefor. The present invention further provides foods, beverages and nutraceuticals supplemented with one or more of the composite crystalline structures described herein. The present invention further provides a method for treating or preventing CVD and its underlying conditions including atherosclerosis, hypercholesterolemia, hyperlipidemia, hypertension, thrombosis, and related diseases such as Type II diabetes, as well as other diseases that include oxidative damage as part of the underlying disease process such as dementia, ageing, and cancer by administering to an animal one or more of the composite crystalline structures as described herein. The present invention further provides a process of preparing a composite crystalline structure comprising a phytosterol and a phytostanol, or a derivative of either, which comprises: a) dissolving the phytosterol and the phytostanol in a solvent at an ambient temperature or temperature above ambient but lower than the boiling point of the solvent; b) cooling the solvent to allow crystal formation; and c) filtering and washing the crystals so formed. What is achieved within the scope of the present invention is the creation of a composite crystalline structure wherein a phytosterol and a phytostanol, under appropriate conditions, are recrystallized together forming a unitary structure which is a single composite endotherm as evidenced using differential scanning calorimetry ("DSC"). In addition, these new crystalline structures have their own x-ray powder diffraction ("XRD") profiles, their own chemical characteristics and their own particular melting points as compared to each of the individual phytosterols or phytostanol alone or together in a composition. In other words, what is created is a structure chemically and physically unlike either of the phytosterol or phytostanol starting materials alone, or mixed in composition. These crystalline composites have numerous advantages over individual phytosterols or phytostanols or mixtures thereof previously known and described in the art. In particular, it has been found that solubility in oils, oil-based media and fats is improved by a method which is simple, economical and which does not require extensive prior modifications to the sterols or stanols, such as by esterification. Naturally occurring and isolated phytosterols and stanols are in coarse, powder, crystalline form which is not amenable to the formation of a homogeneous mixture in water, oils or fats, without some type of modification. Although esterification of phytosterols and stanols does make them considerably more soluble in fats and oils and is a widely used technique for practical reasons, these esterified derivatives do not inhibit the absorption of cholesterol as effectively as free sterols (8). In a number of prior patents, stanols, in particular, are esterified in order to enhance their poor solubility (see US Patent Serial No. 5,502,045 to Raision Tehtaat Oy AB). The disadvantages of phytosterol/stanol fatty acid esters include the following: decreased absorption of lipophilic micronutrients (like beta- carotene) (9) and increased processing time and costs to prepare. Heating beta- sitosterol in oil is described in PCT/FI99/00121 ; however, the resultant product is one in which the sterols are only partially dissolved. Within the scope of the present invention, naturally occurring phytosterols and phytostanols in crystalline form, are re-crystallized together to form unitary composite crystalline structures which not only exhibit enhanced solubility in oils and fats as compared to individual phytosterols or phytostanols or mixtures thereof previously known and described in the art, but also show greater efficacy in lowering serum cholesterol. Accordingly, oil and fat-based compositions comprising the crystalline structures of the present invention can be prepared and used as such or they can be easily incorporated into foods, beverages, dietary supplements, pharmaceuticals and nutraceuticals. This enhanced solubility generally translates into lower concentrations of phytosterols and/or phytostanols that need be provided in the oil or fat in order to achieve the desired therapeutic or dietary effect. These and other advantages of the present invention are outlined in more detail hereinbelow. BRIEF DESCRIPTION OF THE DRAWINGS The present invention is illustrated by the following non-limiting drawings in which: Figure 1 is a microscopic photograph of the crystalline material from FCP-3P1 ; Figure 2 is another microscopic photograph of the crystalline material from FCP-3P1 ; Figure 3 is a microscopic photograph of the crystalline structure from FCP-3P2; Figure 4 is another microscopic photograph of the crystalline structure from FCP-3P2; ._, Figure 5 is a microscopic photograph of an equal mixture of FCP-3P1 and FCP-3P2 recrystallized from ethyl acetate; Figure 6 is another microscopic photograph of an equal mixture of FCP-3P1 and FCP- 3P2 recrystallized from ethyl acetate; Figure 7 is another microscopic photograph of an equal mixture of FCP-3P1 and FCP- 3P2 recrystallized from ethyl acetate; 3^ * ' ' Figure 8 is another microscopic photograph of an equal mixture of FCP-3P1 and FOPS' 3P2 recrystallized from ethyl acetate; Figures 9 is the DSC indium calibration data; Figure 10 is the DSC data overlay for FCP-3P1 , FCP-3P2, the equal mixture of FCP-3P1 and FCP-3P2 in composition and the recrystallized material (FM-PH-38); Figure 11 is the DSC data for FCP-3P2; Figure 12 is the DSC data for FCP-3P1 ; Figure 13 is the DSC data for an equal mixture of FCP-3P1 and FCP-3P2 in composition; Figure 14 is DSC data for the equal mixture of FCP-3P1 and FCP-3P2 recrystallized from ethyl aectate; Figure 15 is the X-ray diffraction data for FCP-3P2; Figure 16 is the X-ray diffraction data for FCP-3P1 ; and Figure 17 is the X-ray diffraction data for the equal mixture of FCP-3P1 and FCP-3P2 recrystallized from ethyl acetate. PREFERRED EMBODIMENTS OF THE INVENTION According to one embodiment the present invention, there is provided a composite crystalline structure comprising a phytosterol and a phytostanol, or a derivative of either suitable for use per se in treating or preventing CVD and its underlying conditions, such as atherosclerosis, hypercholesterolemia, hyperlipidemia, hypertension, thrombosis, and related diseases such as Type II diabetes, as well as in treating and preventing other diseases that include oxidative damage as part of the underlying disease process such as dementia, aging, and cancer. At the outset, it is to be understood that throughout this specification, the terms "composite crystalline structure", "crystalline composite structure", "new crystalline structures", "composite crystals", "novel structures", "composite" and "crystal structures" are used interchangeably and are intended, unless otherwise clearly stated, to possess the same meaning. Phytosterols/Phytostanols The term "phytosterol", within the scope of the present invention, includes all phytosterols without limitation, for example: sitosterol, campesterol, stigmasterol, brassicasterol, desmosterol, chalinosterol, poriferasterol, clionasterol and all natural or synthesized forms and derivatives thereof, including isomers. The term "phytostanol" includes all saturated or hydrogenated phytosterols and all natural or synthesized forms and derivatives thereof, including isomers. It is to be understood that modifications to the phytosterols and phytostanols i.e. to include modified side chains also falls within the purview of this invention. It is also to be understood that, when in doubt throughout the specification, the term "phytosterol" encompasses both phytosterol and phytostanol i.e. the terms may be used interchangeably unless otherwise specified. The phytosterols and phytostanols for use in forming the crystalline composite structures in accordance with this invention may be procured from a variety of natural sources. For example, they may be obtained from the processing of plant oils (including aquatic plants) such as corn oil and other vegetable oils, wheat germ oil, soy extract, rice extract, rice bran, rapeseed oil, sesame oil and fish oils. Without limiting the generality of the foregoing, it is to be understood that there are other sources of phytosterols and phytostanols such as marine animals from which the composition of the present invention may be prepared. US Patent Serial No. 4,420,427 teaches the preparation of sterols from vegetable oil sludge using solvents such as methanol. Alternatively, phytosterols and phytostanols may be obtained from tall oil pitch or soap, by-products of forestry practises as described in US Patent Serial No.5, 770, 749, incorporated herein by reference. Phytosterols and phytostanols are widely available through commercial supply companies. Without limiting the generality of the foregoing, it is to be understood that there are numerous known methods of extracting and purifying phytosterols and phytostanols from the "source" of choice and the present invention is not limited to any one method of attaining these purified phytosterols and phytostanols. Generally, however, the phytosterols and phytostanols, purified from the source, are in a crystalline form, with each sterol and stanol represented by an individual crystal structure, and having its own DSC endotherm and XRD profile. In a most preferred form, the crystalline composite structure of the present invention is formed with naturally-derived or synthesized beta-sitosterol or campesterol and either sitostanol or campestanol, or mixtures thereof. Recrystallization Process In a preferred form, the recrystallization process is as follows: a) one or more phytosterols and phytostanols are selected for combination into the unique crystalline structure; b) these phytosterols and phytostanols are dissolved in a solvent at an ambient temperature or temperature above ambient but lower than the boiling point of the solvent; c) the solvent is cooled to allow crystal formation; and d) the crystals so formed are filtered and dried. Many solvents are suitable for use within the method of the present invention. Most preferably, the solvent is selected from any one of the following, alone or in combination: 1) any hydrocarbon solvent such as pentane, hexane and higher family members from C7 to C10 inclusive, or derivatives thereof; 2) any alcohol of the family C1 to C10 inclusive, including without limitation, ethanol, isopropyl alcohol and methanol, or derivatives thereof; 3) aromatic solvents such as toluene and xylene and derivatives thereof; 4) ketones having from 1 to 10 carbon atoms, including, without limitation, acetone, propanone, methylisobutyl ketone and butanone, or derivatives thereof; and 5) esters such as ethyl acetate and those derived from carboxylic acids of the family C2 to C10 inclusive. In one preferred form, the phytosterols and phytostanols are dissolved in the solvent at ambient room temperature from 18 to 30 ° C, although it is not intended that the process be limited to any particular temperature. For example, when isopropyl alcohol is used as the recrystallization solvent, the temperature for dissolution of the phytosterols and phytostanols is most preferably in the range of 50-80° C. What is critical is that substantially all of the phytosterols and phytostanols are dissolved in the chosen solvent (the solvent is "saturated") and that the temperature chosen is lower than the boiling point of the selected solvent. This dissolution may take anywhere from 30 minutes to 6 hours depending on the solvent used and the constituent phytosterols/stanols. Likewise, the cooling temperature of step b), to promote formation of the crystals may vary considerably but it is generally from 1 to 20° C. Preferably, the cooling occurs rapidly in less than one hour and most preferably in about 30 minutes to a temperature at which crystal formation begins. The resulting slurry is best stirred slowly during this process. After the sterols/stanols have precipitated from the solution, the crystals so formed are filtered and repeatedly washed (for example with deionized water), and then lightly compressed and suctioned free of liquid. Once recrystallization is complete, to confirm the formation of new crystalline structures, endotherm analysis using DSC technology and XRD profiles or other techniques in which the molecular structure or crystalline matrix can be checked. What has been found is that the new crystal structures so formed have properties (exhibited as XRD and DSC data) which are unlike each of the starting materials alone (the particular phytosterols or phytostanols) or in composition and which are, in fact, intermediate between the starting materials' properties. In one embodiment, the composite crystal of the present invention may be used directly and without any further adaptations or work-ups in the therapeutic and dietary protocols outlined below. In another embodiment, the composite crystal may be formed into a solid powder through precipitation, filtration and drying, spray drying, lyophilization or by other conventional work-up techniques. This powder form may then be used in the therapeutic and dietary protocols noted below. The method of the present invention, in which phytosterols and phytostanols are recrystallized together to form new crystalline structures may be used: 1) to form new "designer" compositions of phytosterols and phytostanols having any desired concentration range of the constituents; or 2) to blend or "spike" phytosterols and phytostanols into sterol compositions extracted from natural sources in order to ensure specification uniformity between batches. "Designer" compositions can be prepared, under controlled conditions, having any concentration of phytosterols and phytostanols desired. For example, a composition having 99% by weight ("w/w") phytosterols and 1 % w/w phytostanols or anywhere in between or having 99% w/w phytostanols and 1 % w/w phytosterols or anywhere in between can be prepared using the recystallization protocol. Accordingly, there is afforded a great deal of processing flexibility as the relative amounts of each sterol and stanol in the final composition can be adjusted by successive recrystallizations. For example, if a higher relative concentration of sitostanol is desired in a given composition, sitostanol may be recrystallized with the sterol/stanols already in the composition yielding one or more new composite crystal structures within that composition. Preferably, the designer composition of the present invention, prepared by recrystallization comprises 20 to 80% w/w phytosterols and from 80 to 20% w/w phytostanols, more preferably from 30 to 70% w/w phytosterols and from 70 to 30 w/w phytostanols, more preferably from 40 to 60% w/w phytosterols and from 60 to 40% w/w phytostanols and most preferably 50% w/w phytosterols and phytostanols. Blending or spiking phytosterols and phytostanols into compositions extracted from natural sources also has a number of critical commercial applications. Regardless of the natural source from which the phytosterols and phytostanols are extracted and purified, there will always be some variation, batch to batch, in the relative amounts of each phytosterol and phytostanol. This can be a production problem when it is necessary consistently to produce a composition having a particular set of specifications. The recrystallization method of the present invention addresses and solves this problem. For example, if one extracted and purified batch does not comply with the necessary specification in that the concentration of sitostanol is too low, this can readily be adjusted by recrystallizing into the composition a set amount of sitostanol to "spike" up the level. Both the formation of designer compositions and the spiking of existing natural compositions can be achieved with phytosterols and phytostanols originally derived from any source (without limitation, tall oil soap, tall oil pitch, vegetable distillate, soybean extract and the like). In addition, it is fully contemplated that phytosterol and phytostanol sources can be "mixed". In other words, a composition naturally derived from tall oil soap may be "spiked" and recrystallized with a sterol or stanol derived from soybean extract. The "spiking" of compositions is described in more detail in the Examples. Advantages of Novel Crystal Composite Structures The novel structures of the present invention afford many dietary and therapeutic advantages when compared to the use of phytosterols/phytostanols alone or together in composition. What is primarily achieved by the formation of the composite crystals is enhanced solubility of the phytosterol/stanol constituents in oils and fats, without the need for chemical or other structural modifications to the sterols and stanols. Not only does this facilitate the incorporation of sterols and stanols into "delivery" vehicles (with the attendant cost and time savings) but this new unitary structure is more readily absorbed in bile acid micelli, thereby efficiently displacing cholesterol and blocking its absorption. Both phytosterols and phytostanols must first be dissolved in oil micelles in the intestine before interaction with cholesterol can occur. For reasons that are as yet unclear, the crystal structures of the present invention, in which phytosterols and phytostanols are formed into unitary structures, maximize many of the individual advantages of phytosterols and phytostanols, while minimizing the respective disadvantages. For example, many studies suggest that stanols in general, and sitostanol in particular, are the most effective inhibitors of cholesterol absorption, however, they have poor lipid solubility (10). Phytosterols are generally more soluble but are less effective at cholesterol lowering (11 , 12 and 13). The crystal structures of the present invention are more soluble in oils and fats than phytosterols i.e. they exhibit an oil solubility in between that of phytosterols and phytostanols and surprisingly, they exhibit cholesterol lowering efficacy more comparable to stanols than sterols. This combination allows a more effective action in lowering cholesterol than either phytosterols or phytostanol alone or in composition together. Methods of Use The structures of the present invention may be used directly and without further modification in cooking, baking and the like as agents to lower serum cholesterol in animals, particularly humans. They may be added to any edible oil and used for cooking, baking, and general use. Alternatively, the structures may be treated to enhance delivery into various other delivery media. For example, the crystal structures may be physically modified as described in International Application No. PCT/CA99/00402, specifically pages 11-23, (published on November 25, 1999 and incorporated herein by reference) to enhance even further the solubility and dispersability of the phytosterol and/or phytostanol in the chosen delivery medium. In addition, the present invention fully contemplates the formation of oleaginous gel foodstuffs such as peanut butter, mayonnaise, ice cream and margarine spreads incorporating such structures. Further, the composite crystals can readily be included in a variety of low fat foods such as yoghurts in which the fine crystals disperse evenly in the product. There are numerous modes or "vehicles" of delivery of this composition, accordingly, this invention is not intended to be limited to the following delivery examples. 1) Pharmaceutical Dosage Forms: It is contemplated within the scope of the present invention that the structures of the present invention may be incorporated into various conventional pharmaceutical preparations and dosage forms such as tablets (plain and coated) for use orally, bucally or lingually, capsules (hard and soft, gelatin, with or without additional coatings) powders, granules (including effervescent granules), pellets, microparticulates, solutions (such as micellar, syrups, elixirs and drops), lozenges, pastilles, ampuls, emulsions, microemulsions, ointments, creams, suppositories, gels, and transdermal patches, modified release dosage forms together with customary excipients and/or diluents and stabilizers. The structures of the present invention, adapted into the appropriate dosage form as described above may be administered to animals, including humans, orally, by injection (intra-venously, subcutaneously, intra-peritoneally, intra-dermally or intra-muscularly), topically or in other ways. Although the precise mechanism of action is unclear, the structures of the present invention, administered intra-venously, lower serum cholesterol. It is believed that some blends of phytosterols, in concert, may have, in addition to the role as an inhibitor of cholesterol absorption in the intestine, a systemic effect on cholesterol homeostasis through bile acid synthesis, enterocycte and biliary cholesterol excretion, bile acid excretion and changes in enzyme kinetics and cholesterol transport between various compartments within the body (PCT/CA97/00474 which was published on January 15, 1998). The structures as described herein may be used in both dietary and therapeutic capacities in order to treat and/or prevent CVD, its underlying conditions such as hypercholesterolemia, hyperlipidemia, arteriosclerosis, hypertension, thrombosis, related diseases such as Type II diabetes, as well as other diseases that include oxidative damage as part of the underlying disease process such as dementia, aging, and cancer. In populations, which are considered "high-risk" for CVD or any of the oxidation related disorders, it is contemplated that the compositions and foodstuffs in which they are contained be used in primary, secondary and tertiary treatment programs. In order to appreciate the various possible vehicles of the delivery of the compositions, the list below is provided. The doses of the derivatives will vary depending upon, among other factors, the mode of delivery (i.e. how and into which food or beverage or pharmaceutical the derivatives are ultimately incorporated), the patient size and condition, the result to be achieved, as well as other factors known to those skilled in the art of food additives and medicinal agents. Generally, however, it is preferred that the derivatives of the present invention be administered to humans in a form comprising up to 6 grams (based on a 70kg person) of phytosterols and/or phytostanols per day, more preferably from 1-5 grams per day and most preferably 1.5 grams per day. It will also be recognized that the provision of much larger daily doses of the derivatives are not harmful to the animal host, as excess will simply pass through normal excretory channels. 2) Foods/Beverages/Nutraceuticals: In another form of the present invention, the structures of the present invention may be incorporated into foods, beverages and nutraceuticals, including, without limitation, the following: 1) Dairy Products -such as cheeses, butter, milk and other dairy beverages, spreads and dairy mixes, ice cream and yoghurt; 2) Fat-Based Products-such as margarines, spreads, mayonnaise, shortenings, cooking and frying oils and dressings; 3) Cereal-Based Products-comprising grains (for example, bread and pastas) whether these goods are cooked, baked or otherwise processed; 4) Confectioneries-such as chocolate, candies, chewing gum, desserts, non-dairy toppings (for example Cool Whip™), sorbets, icings and other fillings; 5) Beverages- whether alcoholic or non-alcoholic and including colas and other soft drinks, juice drinks, dietary supplement and meal replacement drinks such as those sold under the trade-marks Boost™ and Ensure™; and 6) Miscellaneous Products-including eggs and egg products, processed foods such as soups, pre-prepared pastas The optimal ratio of phytosterols to phytostanol in the composite depends, to some extent, on the matrix in which the composite is to be suspended or incorporated. Generally, foods with a high fat content will accommodate a higher proportion of phytostanols than lower fat foods. This can be determined empirically with each type of food/beverage in which it is desired to add the composite. The structures of the present invention may be incorporated directly and without further modification into the food, nutraceutical or beverage by techniques such as mixing, infusion, injection, blending, dispersing, emulsifying, immersion, spraying and kneading. Alternatively, these structures may be applied directly onto a food or into a beverage by the consumer prior to ingestion. These are simple and economical modes of delivery. While the following examples are intended to illustrate various aspects of the present invention and to assist in the preparation of the structures, they are not intended to limit the scope of invention as claimed herein. EXAMPLE 1 Recrystallization from Ethyl Actetate An equal mixture (1:1 by weight) of a non-hydrogenated tall oil derived composition comprising primarily campesterol and beta-sitosterol (hereinafter called FCP-3P1) and a hydrogenated tall oil derived phytosterol composition comprising primarily sitostanol and campestanol (hereinafter called FCP-3P2) was dissolved in ethyl acetate at ambient room temperaure (21° C) to achieve saturation solution. Phytosterol was recrystallized from the saturated ethyl acetate solution at approximately 6° C overnight before being filtered onto No.1 Whatman filter paper using a Buchner glass filter funnel with vacuum suction. The recrystallized material was dried at 35° C under open atmosphere in a hot oven for 48 hours before storage in a 50 ml polypropylene screw capped tube. This ethyl acetate recrystallized material from an equal mixture of FCP-3P1 and FCP-3P2 is referred to in some of the Figures as FM-PH-38. An analysis of this new recrystallized product was undertaken using microscopic photography, Differential Scanning Calorimetry ("DSC") and X-ray Diffraction ("XRD") and appropriate comparisons were made between the data for FM-PH-38 and: 1) each of the starting materials alone: FCP-3P1 and FCP-3P2; and 2) and equal mixture of FCP-3P1 and FCP-3P2 in composition i.e. not recrystallized together. Microscopic Photography: The solid state crystalline structures of FCP-3P1 , FCP-3P2 and FM-PH-38 were investigated using microscopic photography at 15X and 40X magnification (although only 40X magnification is shown in the Figures). The individual material was examined under a light microscope and photographic records were obtained against a dark background using black and white film. Records for FCP-3P1 are depicted in Figures 1 and 2. Records for FCP-3P2 are depicted in Figures 3 and 4. Records for recrystallized product FM-PH-38 are depicted in Figures 5 through 8 inclusive. Differential Scanning Calorimetry DSC determinations were carried out using a Dupont Model 91 OS DSC (New Castle, DL) calibrated with indium. Samples weighing between 3 to 4 mg were placed in open aluminum pans (n=3 for each of the test materials). The DSC cell was purged with nitrogen flowing at 40 ml/min. All measurements were made with a scan rate of 10° C/min. Scans were obtained by heating from ambient temperature to 350° C. DSC data for FCP-3P1 , FCP-3P2 and FM-PH-38 are presented in Figures 9 through 14. X-Ray Diffraction XRD measurements of FCP-3P1 , FCP-3P2 and FM-PH-38 were achieved using a wide angle x-ray diffractor and are presented in Figures 15 through 17. Generally, XRD is the classical method to investigate how crystals form and are assembled together. Chemical Composition The features of the chemical composition were investigated using gas chromatography/ mass spectrometry ("GC/MS"). This method involves the use of a bonded phase 5% diphenyl dimethylsiloxane fused silica capillary column for the separation of the four phytosterols. Quantitation of the four major phytosterol components is based on an internal standard ratio approach with the use of cholestane added to each sample as the internal standard. The peak area ratio of each phytosterol to cholestane was plotted against spiked calibration standard concentrations. Calibration standard curves were established from weighted (1/Y) linear regression analysis of peak area ratios against a minimum of 6 phytosterol standard concentrations over a range from 0.01 to 3.0 mg/ml. A Hewlett Packard Model 5890 series II gas chromtograph was operated with model 5971 GC/MS (MSD) and a model 3635 autosampler using the following parameters: GC column 30m x 0.25mm x 0.25 urn SAC-5 GC oven temp 270 degrees C GC column carrier gas helium GC/MSD transfer line temp 300 degrees C Injector temp 300 degrees C Injection volume 1ul Injection mode splitless (purge time 0.5 minutes) Results and Discussion: Photomicrographs: Differences in appearance of the crystal outline between FCP-3P1 , FCP-3P2 and FM-PH- 38 in Figures 1 through 8 show that these three materials are chemically unique. FM-PH- 38 crystals in Figures 5 through 8 clearly show thinner rods. Although the clarity seems to be similar to FCP-3P2, the shape is not at all similar to the block-shaped crystals shown in Figures 3 and 4. DSC: The data is presented in its entirety in Figures 9 through 13 but is summarized in Table 1: Table 1 Melting points for individual sterols and stanols, in degrees C are as follows: Beta-sitosterol 140 Sitostanol 138-139 Campesterol 157-158 Campestanol 146.5-147.8 The DSC endotherms profiled in Figures 9 through 13 indicated that the four major components interact during melting and do not directly or simply correlate with the melting points of the individual components. A physical mixture (composition) of FCP-3P1 and FCP-3P2 shows two endotherms at 118.31 °C and 138.72° C as compared to the recrystallized material (FM-PH-38) which demonstrates a single composite endotherm with peaks at 135.37° C and 139.39° C comprising three closely overlapping peaks (triplet). This clearly shows that the two starting materials have combined to produce a composite crystalline structure having its own particular melting properties in comparison with the individual starting materials alone, or in composition. XRD: Data is shown in Figures 15 through 17. Spectra for FM-PH-38 shows no well defined peaks which indicates that there is no well defined crystal order as in most crystalline structures, including FCP-3P1 and FCP-3P2. Overall, the crystal habit of FM-PH-38 is different from the other materials. Chemical Composition: The GC/MS results indicating the proportion of the four major phytosterols in the three materials are as follows: Table 2-Summary of Four Major Phytosterols Table 3- GC/MS Quantitation of Major Phytosterols in FCP-3P2 Table 4- GC/MS Quantitation of Major Phytosterols in FCP-3P1 Table 5- GC/MS Quantitation of Major Phytosterols in FM-PH-38 EXAMPLE 2 Recrystallization from Isopropyl Alcohol An equal mixture (1:1 by weight) of FCP-3P1 and FCP-3P2 was dissolved in isopropyl alcohol at 75° C to achieve saturation solution. Phytosterol was recrystallized from the saturated isopropyl alcohol solution at approximately 6° C overnight before being filtered onto No.1 Whatman filter paper using a Buchner glass filter funnel with vacuum suction. The recrystallized material was dried at 35° C under open atmosphere in a hot oven for 48 hours before storage in a 50 ml polypropylene screw capped tube. EXAMPLE 3 Recrystallization from Methylisobutyl Ketone ("MIBK") An equal mixture (1 :1 by weight) of FCP-3P1 and FCP-3P2 was dissolved in MIBK at ambient temperature to achieve saturation solution. Phytosterol was recrystallized from the saturated MIBK solution at approximately 6° C overnight before being filtered onto No.1 Whatman filter paper using a Buchner glass filter funnel with vacuum suction. The recrystallized material was dried at 35° C under open atmosphere in a hot oven for 48 hours before storage in a 50 ml polypropylene screw capped tube. EXAMPLE 4 Recrystallization from Toluene An equal mixture (1 :1 by weight) of FCP-3P1 and FCP-3P2 was dissolved in toluene at ambient temperature to achieve saturation solution. Phytosterol was recrystallized from the saturated toluene solution at approximately 6° C overnight before being filtered onto No.1 Whatman filter paper using a Buchner glass filter funnel with vacuum suction. The recrystallized material was dried at 35° C under open atmosphere in a hot oven for 48 hours before storage in a 50 ml polypropylene screw capped tube. EXAMPLE 5 Recrystallization from Hexane/Acetone An equal mixture (1 :1 by weight) of FCP-3P1 and FCP-3P2 was dissolved in a hexane/acetone blend (50% of each w/w) at ambient temperature to achieve saturation solution. Phytosterol was recrystallized from the saturated hexane/acetone solution at approximately 6° C overnight before being filtered onto No.1 Whatman filter paper using a Buchner glass filter funnel with vacuum suction. The recrystallized material was dried at 35° C under open atmosphere in a hot oven for 48 hours before storage in a 50 ml polypropylene screw capped tube. EXAMPLE 6 Purification and Hydrogenation of Crude Tall Oil Phytosterols, and Subsequent Blending or "Spiking" using Recrystallization Process Goal: The therapeutic composition to be prepared had to fall within the following predetermined specifications: Beta-sitosterol 38-60% Sitostanol 14-34% Campesterol 9-28% Campestanol 2-14% a) Purification: crude tall oil sterols (55 kg) were dispersed into 220 L of isopropyl alcohol ("IPA"). Activated carbon (5.5 kg) was added to purify the sterols. The purification was carried out by agitating the mixture for 2 hours at 65° C. The carbon was filtered out using a Mott filter, also at 65° C. b) Hydrogenation.A portion (30% w/w) of the purified phytosterol (59.41% beta-sitosterol; 4.73% sitostanol; 24.19% campesterol; and 7.39% campestanol, all % w/w) mixture was hydrogenated in IPA using palladium on alumina catalyst. The hydrogenation process was carried out at 70° C and 60psi hydrogen pressure for 3 hours. A Mott filter was used to recover the palladium catalyst after hydrogenation. c) Blending/Spiking: The hydrogenated portion (74.47% sitostanol and 20.35% campestanol) and the non-hydrogenated portion (70% w/w with specification noted above) were dissolved in IPA solution at 75° C to achieve saturation solution. The product was recrystallized from the saturated isopropyl alcohol solution at approximately 6° C overnight before being filtered onto No.1 Whatman filter paper using a Buchner glass filter funnel with vacuum suction. The recrystallized material was then dried at 35° C under open atmosphere in a hot oven for 48 hours before storage in a 50 ml polypropylene screw capped tube. The recrystallized product so formed had the following specifications (% w/w): Beta-sitosterol 41.59% Sitostanol 25.65% Campesterol 16.93% Campestanol 11.28% The sitostanol concentration is significantly higher in the recrystallized product than the originally purified material (25.65% as compared to 4.73%) which translates into a product of higher therapeutic efficacy. EXAMPLE 7 Purification and Hydrogenation of Crude Vegetable Derived Phytosterols, and Subsequent Blending or "Spiking" using Recrystallization Process Goal: The therapeutic composition to be prepared had to fall within the following predetermined specifications: Beta-sitosterol 18-60% Sitostanol 14-34% Campesterol 9-28% Campestanol 2-14% Stigmasterol n/a Brassicasterol n/a a) Purification: Soy sterols were purchased commercially from ADM. b) Hydrogenation: A portion (44% w/w) of the purified phytosterols (45.70% beta- sitosterol; 2.1% sitostanol; 27.90% campesterol; and 14.80% stigmasterol and 5.3% brassicasterol, all % w/w) mixture was hydrogenated in IPA using palladium on alumina catalyst. The hydrogenation process was carried out at 70° C and 60psi hydrogen pressure for 3 hours. A Mott filter was used to recover the palladium catalyst after hydrogenation. c) Blending/Spiking: The hydrogenated portion (with a specification of 62.60% sitostanol and 33.20% campestanol) and the non-hydrogenated portion (in an amount of 56% w/w and having the specification noted above) were dissolved in IPA solution at 75° C to achieve saturation solution. The product was recrystallized from the saturated isopropyl alcohol solution at approximately 6° C overnight before being filtered onto No.1 Whatman filter paper using a Buchner glass filter funnel with vacuum suction. The recrystallized material was then dried at 35° C under open atmosphere in a hot oven for 48 hours before storage in a 50 ml polypropylene screw capped tube. The recrystallized product so formed had the following specifications (% w/w) which fell satisfactorily within the desired ranges: Beta-sitosterol 25.60% Sitostanol 28.70% Campesterol 15.60% Campestanol 14.60% Stigmasterol 8.30% Brassicasterol 3.00% As in Example 6 above, the sitostanol concentration is significantly higher in the recrystallized product than the originally purified material (25.60% as compared to 2.10%) which translates into a product of higher therapeutic efficacy. EXAMPLE 8 Purification and Hydrogenation of Crude Vegetable Derived Phytosterols, and Subsequent Blending or "Spiking" with Tall Oil Derived Phytosterols using Recrystallization Process Goal: The therapeutic composition to be prepared had to fall within the following pre- determined specifications: Beta-sitosterol 18-60% Sitostanol 14-34% Campesterol 9-28% Campestanol 10-30% Stigmasterol n/a Brassicasterol n/a a) Purification: Vegetable sterols were purchased commercially from Henkel. b) Hydrogenation: The vegetable phytosterol mixture was hydrogenated in IPA using palladium on alumina catalyst. The hydrogenation process was carried out at 70° C and 60psi hydrogen pressure for 3 hours. A Mott filter was used to recover the palladium catalyst after hydrogenation. c) Blending/Spiking: The hydrogenated sterols (with a specification of 0% beta-sitosterol; 40% sitostanol; 0% campesterol; 40% campestanol and 0% brassicasterol, all % w/w) and the non-hydrogenated tall oil derived sterols (with a specification of 59.4% beta- sitosterol; 4.7% sitostanol; 24.2% campesterol; 7.4% campestanol and 0% brassicasterol, all % w/w) at a ratio of 55:45 % w/w were dissolved in IPA solution at 75° C to achieve saturation solution. The product was recrystallized from the saturated isopropyl alcohol solution at approximately 6° C overnight before being filtered onto No.1 Whatman filter paper using a Buchner glass filter funnel with vacuum suction. The recrystallized material was then dried at 35° C under open atmosphere in a hot oven for 48 hours before storage in a 50 ml polypropylene screw capped tube. The recrystallized product so formed had the following specifications (% w/w) which fell satisfactorily within the desired ranges: Beta-sitosterol 26.7% Sitostanol 24.1% Campesterol 10.9% Campestanol 25.3% Brassicasterol 0% EXAMPLE 9 Purification and Hydrogenation of Crude Tall Oil Derived Phytosterols, and Subsequent Blending or "Spiking" with Vegetable Derived Phytosterols using Recrystallization Process Goal: The therapeutic composition to be prepared had to fall within the following pre- determined specifications: Beta-sitosterol 18-60% Sitostanol 14-34% Campesterol 9-28% Campestanol 2-30% Stigmasterol n/a Brassicasterol n/a a) Purification: crude tall oil sterols (55 kg) were dispersed into 220 L of isopropyl alcohol ("IPA"). Activated carbon (5.5 kg) was added to purify the sterols. The purification was carried out by agitating the mixture for 2 hours at 65° C. The carbon was filtered out using a Mott filter, also at 65° C. b) Hydrogenation: The tall oil phytosterols were hydrogenated in IPA using palladium on alumina catalyst. The hydrogenation process was carried out at 70° C and 60psi hydrogen pressure for 3 hours. A Mott filter was used to recover the palladium catalyst after hydrogenation. c) Blending/Spiking: The hydrogenated sterols (with a specification of 0% beta-sitosterol; 74.5% sitostanol; 0% campesterol; 20.4% campestanol and 0% brassicasterol, all % w/w) and the non-hydrogenated vegetable derived derived sterols, purchased commercially from Henkel (with a specification of 40% beta-sitosterol; 0% sitostanol; 33% campesterol; 0% campestanol and 7% brassicasterol, all % w/w) at a ratio of 33:67 % w/w were dissolved in IPA solution at 75° C to achieve saturation solution. The product was recrystallized from the saturated isopropyl alcohol solution at approximately 6° C overnight before being filtered onto No.1 Whatman filter paper using a Buchner glass filter funnel with vacuum suction. The recrystallized material was then dried at 35° C under open atmosphere in a hot oven for 48 hours before storage in a 50 ml polypropylene screw capped tube. The recrystallized product so formed had the following specifications (% w/w) which fell satisfactorily within the desired ranges: Beta-sitosterol 26.8% Sitostanol 24.6% Campesterol 22.1% Campestanol 6.7% Brassicasterol 4.7% EXAMPLE 10 Purification and Hydrogenation of Crude Vegetable Derived Phytosterols, and Subsequent Blending or "Spiking" with Vegetable Derived Phytosterols using Recrystallization Process Goal: The therapeutic composition to be prepared had to fall within the following pre- determined specifications: Beta-sitosterol 18-60% Sitostanol 14-34% Campesterol 9-28% Campestanol 10-30% Stigmasterol n/a Brassicasterol n/a a) Purification: Vegetable sterols were purchased commercially from Henkel and ADM. b) Hydrogenation: The vegetable phytosterol mixture from ADM was hydrogenated in IPA using palladium on alumina catalyst. The hydrogenation process was carried out at 70° C and 60psi hydrogen pressure for 3 hours. A Mott filter was used to recover the palladium catalyst after hydrogenation. c) Blending/Spiking: The hydrogenated sterols (with a specification of 0% beta-sitosterol; 55.6% sitostanol; 0% campesterol; 23.9% campestanol, 6.9% brassicastanol and 0% brassicasterol, all % w/w) and the non-hydrogenated vegetable derived sterols from Henkel (with a specification of 40% beta-sitosterol; 0% sitostanol; 33% campesterol; 0% campestanol and 7% brassicasterol, all % w/w) at a ratio of 44:56 % w/w were dissolved in IPA solution at 75° C to achieve saturation solution. The product was recrystallized from the saturated isopropyl alcohol solution at approximately 6° C overnight before being filtered onto No.1 Whatman filter paper using a Buchner glass filter funnel with vacuum suction. The recrystallized material was then dried at 35° C under open atmosphere in a hot oven for 48 hours before storage in a 50 ml polypropylene screw capped tube. The recrystallized product so formed had the following specifications (% w/w) which fell satisfactorily within the desired ranges: Beta-sitosterol 22.4% Sitostanol 24.5% Campesterol 18.5% Campestanol 10.5% Brassicasterol 3.9% Brassicastanol 3.0% EXAMPLE 11 Purification and Hydrogenation of Crude Vegetable Derived Phytosterols, and Subsequent Blending or "Spiking" with Vegetable Derived Phytosterols using Recrystallization Process Goal: The therapeutic composition to be prepared had to fall within the following pre- determined specifications: Beta-sitosterol 10-60% Sitostanol 14-34% Campesterol 5-28% Campestanol 10-30% Stigmasterol n/a Brassicasterol n/a a) Purification: Vegetable sterols were purchased commercially from Henkel. b) Hydrogenation: The vegetable phytosterol mixture was hydrogenated in IPA using palladium on alumina catalyst. The hydrogenation process was carried out at 70° C and 60psi hydrogen pressure for 3 hours. A Mott filter was used to recover the palladium catalyst after hydrogenation. c) Blending/Spiking: The hydrogenated sterols (with a specification of 0% beta-sitosterol; 40% sitostanol; 0% campesterol; 39% campestanol, and 0% brassicasterol, all % w/w) and the non-hydrogenated vegetable derived sterols (with a specification of 40% beta- sitosterol; 0% sitostanol; 33% campesterol; 0% campestanol and 6% brassicasterol, all % w/w) at a ratio of 73:27 % w/w were dissolved in IPA solution at 75° C to achieve saturation solution. The product was recrystallized from the saturated isopropyl alcohol solution at approximately 6° C overnight before being filtered onto No.1 Whatman filter paper using a Buchner glass filter funnel with vacuum suction. The recrystallized material was then dried at 35° C under open atmosphere in a hot oven for 48 hours before storage in a 50 ml polypropylene screw capped tube. The recrystallized product so formed had the following specifications (% w/w) which fell satisfactorily within the desired ranges: Beta-sitosterol 10.8% Sitostanol 29.2% Campesterol 8.9% Campestanol 28.5% Brassicasterol 1.6% EXAMPLE 12 Purification and Hydrogenation of Crude Vegetable Derived Phytosterols, and Subsequent Blending or "Spiking" with Vegetable Derived Phytosterols using Recrystallization Process Goal: The therapeutic composition to be prepared had to fall within the following predetermined specifications: Beta-sitosterol 10-60% Sitostanol 14-34% Campesterol 5-28% Campestanol 10-30% Stigmasterol n/a Brassicasterol n/a a) Purification: Vegetable sterols were purchased commercially from Cargill. b) Hydrogenation: The vegetable phytosterol mixture was hydrogenated in IPA using palladium on alumina catalyst. The hydrogenation process was carried out at 70° C and 60psi hydrogen pressure for 3 hours. A Mott filter was used to recover the palladium catalyst after hydrogenation. c) Blending/Spiking: The hydrogenated sterols (with a specification of 0% beta-sitosterol; 67% sitostanol; 0% campesterol; 25.6% campestanol, and 0% brassicasterol, all % w/w) and the non-hydrogenated vegetable derived sterols (with a specification of 43% beta- sitosterol; 1.0% sitostanol; 24% campesterol; 0.8% campestanol, 23% stigmasterol and 0.8% brassicasterol, all % w/w) at a ratio of 49:51 % w/w were dissolved in IPA solution at 75° C to achieve saturation solution. The product was recrystallized from the saturated isopropyl alcohol solution at approximately 6° C overnight before being filtered onto No.1 Whatman filter paper using a Buchner glass filter funnel with vacuum suction. The recrystallized material was then dried at 35° C under open atmosphere in a hot oven for 48 hours before storage in a 50 ml polypropylene screw capped tube. The recrystallized product so formed had the following specifications (% w/w) which fell satisfactorily within the desired ranges: Beta-sitosterol 21.9% Sitostanol 33.3% Stigmasterol 11.7% Campesterol 12.2% Campestanol 13% Brassicasterol 0.4% EXAMPLE 13 Purification and Hydrogenation of Crude Vegetable Derived Phytosterols, and Subsequent Blending or "Spiking" with Vegetable Derived Phytosterols using Recrystallization Process Goal: The therapeutic composition to be prepared had to fall within the following pre- determined specifications: Beta-sitosterol 10-60% Sitostanol 14-34% Campesterol 5-28% Campestanol 10-30% Stigmasterol n/a Brassicasterol n/a a) Purification: Vegetable sterols were purchased commercially from Cargill and Henkel. b) Hydrogenation: The vegetable phytosterol mixture from Henkel was hydrogenated in IPA using palladium on alumina catalyst. The hydrogenation process was carried out at 70° C and 60psi hydrogen pressure for 3 hours. A Mott filter was used to recover the palladium catalyst after hydrogenation. c) Blending/Spiking: The hydrogenated sterols (with a specification of 0% beta-sitosterol; 40% sitostanol; 0% campesterol; 36-44% campestanol, and 0% brassicasterol, all % w/w) and the non-hydrogenated vegetable derived sterols from Cargill (with a specification of 43% beta-sitosterol; 1.0% sitostanol; 24% campesterol; 0.8% campestanol, 23% stigmasterol and 0.8% brassicasterol, all % w/w) at a ratio of 72:28 % w/w were dissolved in IPA solution at 75° C to achieve saturation solution. The product was recrystallized from the saturated isopropyl alcohol solution at approximately 6° C overnight before being filtered onto No.1 Whatman filter paper using a Buchner glass filter funnel with vacuum suction. The recrystallized material was then dried at 35° C under open atmosphere in a hot oven for 48 hours before storage in a 50 ml polypropylene screw capped tube. The recrystallized product so formed had the following specifications (% w/w) which fell satisfactorily within the desired ranges: Beta-sitosterol 12% Sitostanol 29.1% Stigmasterol 6.4% Campesterol 6.7% Campestanol 26.1-31.9% Brassicasterol 0.2% EXAMPLE 14 Purification and Hydrogenation of Crude Vegetable Derived Phytosterols, and Subsequent Blending or "Spiking" with Vegetable Derived Phytosterols using Recrystallization Process Goal: The therapeutic composition to be prepared had to fall within the following pre- determined specifications: Beta-sitosterol 5-60% Sitostanol 14-34% Campesterol 5-28% Campestanol 10-40% Stigmasterol n/a Brassicasterol 1-5% a) Purification: Vegetable sterols were purchased commercially from Henkel. b) Hydrogenation: The vegetable phytosterol mixture was hydrogenated in IPA using palladium on alumina catalyst. The hydrogenation process was carried out at 70° C and 60psi hydrogen pressure for 3 hours. A Mott filter was used to recover the palladium catalyst after hydrogenation. c) Blending/Spiking: The hydrogenated sterols (with a specification of 0% beta-sitosterol; 40% sitostanol; 0% campesterol; 36-44% campestanol, and 0% brassicasterol, all % w/w) and the non-hydrogenated vegetable derived sterols (with a specification of 40% beta- sitosterol; 0% sitostanol; 30-36% campesterol; 0% campestanol and 6-8% brassicasterol, all % w/w) at a ratio of 83:17 % w/w were dissolved in IPA solution at 75° C to achieve saturation solution. The product was recrystallized from the saturated isopropyl alcohol solution at approximately 6° C overnight before being filtered onto No.1 Whatman filter paper using a Buchner glass filter funnel with vacuum suction. The recrystallized material was then dried at 35° C under open atmosphere in a hot oven for 48 hours before storage in a 50 ml polypropylene screw capped tube. The recrystallized product so formed had the following specifications (% w/w) which fell satisfactorily within the desired ranges: Beta-sitosterol 6.8% Sitostanol 33.2% Stigmasterol 0% Campesterol 5.1-6.1% Campestanol 29.9-36.5% Brassicasterol 1-4% REFERENCES REFERENCES 1. Law M.R., Wald N.J., Wu., Hacksaw ZA., Bailey A.; Systemic underestimation of association between serum cholesterol concentration and ischemic heart disease in observational studies: Data from BUPA Study; Br. Med. J. 1994; 308:363-366 2. Law M.R., Wald N.J., Thompson S.G.; By how much and how quickly does reduction in serum cholesterol concentration lower risk of ischemic heart disease? Br. Med. J. 1994; 308:367-373 3. La Rosa J.C., Hunninghake D.. Bush D. et al.; The cholesterol facts: A summary of the evidence relating to dietary fats, serum cholesterol and coronary heart disease:Ajoint statement by the American Heart Association and the National Heart, Lung and Blood Institute. Circulation 1990; 81:1721-1733 4. Havel R.J., Rapaport E.. Drug Therapy: Management of Primary Hyperlipidemia. New England Journal of Medicine, 1995; 332:1491-1498 5. Kuccodkar et al.; Effects of plant sterols on cholesterol metabolism. Atherosclerosis, 1976; 23:239-248 6. Lees R.S., Lees A.M. Effects of sitosterol therapy on plasma lipid and lipoprotein concentrations. In: Greten H (Ed) Lipoprotein Metabolism. Springer-Verlag, Berlin, Heidelberg, New York, 1976:119-124 7. Lees A.M., Mok H.Y.I. , Lees R.S., McCluskey M.A., Grundy S.M. Plant sterols as cholesterol-lowering agents: clinical trials in patients with hypercholesterolemia and studies of sterol balance. Atherosclerosis 1977; 28: 325-338 8. Mattson FH et al.: American Journal of Clinical Nutrition. 35(4): 697-700, 1982 9. Gyling H.K. et al. Circulation 1996; 6:1-578 10 Hassan A.S. and Rampone A.J. J. Lipid Res. 1979:20; 646-653 11. Lees R.S, Lees A.M. Effects of sitosterol therapy on plasma lipids and lipoprotein concentrations, pp 119-124 in "Lipoprotein Metabolism" Ed Greten H., Berlin, Heidelburg, NY: Springer-Verlag, 1976 12. Mattson F.H., Volpenhein R.A. and Erickson B.A. J. Nutrition 1977:107; 1109-1146 13.Heinemann et al. Agents Actions(Suppl) 1988:26; 117-122

Claims: WE CLAIM: 1. A novel composite crystalline structure comprising a phytosterol and a phytostanol, or a derivative of either. 2. The structure of claim 1 wherein the phytosterol is selected from the group consisting of sitosterol, campesterol, stigmasterol, brassicasterol, desmosterol, chalinosterol, poriferasterol, clionasterol and all natural or synthesized forms and derivatives thereof, including isomers. 3. The structure of claim 1 wherein the phytostanol is selected from the group consisting of all saturated or hydrogenated phytosterols and all natural or synthesized forms and derivatives thereof, including isomers. 4. A method of treating or preventing cardiovascular disease and its underlying conditions including athereosclerosis and hypocholeserolemia in an animal which comprises administering to the animal a composite crystalline structure comprising a phytosterol and a phytostanol, or a derivative of either. 5. The method of claim 4 wherein the phytosterol is selected from the group consisting of sitosterol, campesterol, stigmasterol, brassicasterol, desmosterol, chalinosterol, poriferasterol, clionasterol and all natural or synthesized forms and derivatives thereof, including isomers. 6. The method of claim 4 wherein the phytostanol is selected from the group consisting of all saturated or hydrogenated phytosterols and all natural or synthesized forms and derivatives thereof, including isomers. 7. The method of claim 4 wherein the animal is human. 8. A method of lowering serum cholesterol is an animal which comprises administering to the animal a composite crystalline structure comprising a phytosterol and a phytostanol, or a derivative of either. 9. A product therapeutically effective at treating and preventing cardiovascular disease and, in particular its' underlying conditions atherosclerosis and hypercholesterolemia, which comprises a composite crystalline structure comprising a phytosterol and a phytostanol, or a derivative of either and a pharmaceutically acceptable or food-grade carrier therefore. 10. A comestible or beverage comprising a composite crystalline structure of a phytosterol and a phytostanol, or a derivative of either. 11. A process of making a composite crystalline structure of a phytosterol and a phytostanol, or a derivative of either, which comprises: a) dissolving the phytosterol and the phytostanol in a solvent at an ambient temperature or temperature above ambient but lower than the boiling point of the solvent; b) cooling the solvent to allow crystal formation; and c) filtering and washing the crystals so formed. 12. The process of claim 11 wherein the solvent is any hydrocarbon having from 5 to 10 carbon atoms. 13. The process of claim 11 wherein the solvent is any alcohol having form 1 to 10 carbon atoms. 14. The process of claim 11 wherein the solvent is aromatic. 15. The process of claim 11 wherein the solvent is any ketone having form 1 to 10 carbon atoms. 16. The process of claim 11 wherein the solvent is any ester derived from carboxylic acids having from 2 to 10 carbon atoms. 17. The process of claim 15 wherein the solvent is ethyl acetate. 18. The process of claim 11 wherein the phytosterol and phytostanol are dissolved in the solvent at a temperature of between 18 and 80° C. 19. The process of claim 1 wherein the solvent is cooled, at step b) to a temperature of between 1 and 20°C. 20. The process of claim 11 wherein the phytosterol is selected from the group consisting of sitosterol, campesterol, stigmasterol, brassicasterol, desmosterol, chalinosterol, poriferasterol, clionasterol and all natural or synthesized forms and derivatives thereof, including isomers. 21. The process of claim 11 wherein the phytostanol is selected from the group consisting of all saturated or hydrogenated phytosterols and all natural or synthesized forms and derivatives thereof, including isomers.

Inventors: STEWART DAVID JOHN, STEWART, DAVID, JOHN
Applicants: FORBES MEDI TECH INC, FORBES MEDI-TECH INC.
Application year: 2001
Main classification: C07J
IPC codes: A23D7, A23D9, A23G1, A23G3, A23G4, A23G9, A23L1, A61K9, C07J9, C11B13