METHOD OF VITAMIN PRODUCTION

Abstract: The invention provides a method of producing alpha -tocopherol and alpha -tocopheryl esters. The method comprises using a biological system to produce farnesol or geranylgeraniol. Then, the farnesol or geranylgeraniol is chemically converted into alpha -tocopherol or an alpha -tocopheryl ester.

Description: " METHOD OF VITAMIN PRODUCTION " REFERENCE TO RELATED APPLICATION This application claims priority from U.S. Provisional Application Serial No. 60/091,868, filed July 6, 1998, entitled "Method of Vitamin Production." FIELD OF THE INVENTION The present invention relates to methods of producing vitamins, particularly vitamin E and related compounds. BACKGROUND OF THE INVENTION Vitamin E (d-alpΛa-tocopherol, 1) is an important nutritional supplement in humans and animals. Compound 1 is obtained commercially by isolation from a variety of plant oils, or semisynthetically by ring methylation of the related naturally occurring d-gamma-tocopherol 2. A more important source of vitamin E is total synthesis, which provides d, 1-alp. a-tocopherol 3. Although a mixture of isomers, 3 provides much of the biological activity of 1 and is widely used due to its lower cost and greater availability. For a general discussion of vitamin E, see L. Machlin, ed., "Vitamin E: A Comprehensive Treatise", Marcel Dekker, NY, 1980. d, 1-alpha-Tocopherol 3 is obtained by reacting trimethylhydroquinone 4 with either phytol 5 or isophytol 6 in the presence of an acid catalyst, often a Lewis acid such as zinc chloride. This technology was reviewed by S. Kasparek in L. Machlin, ed., Vitamin E: A Comprehensive Treatise, chapter 2, pp. 8-65, Marcel Dekker, NY, 1965. References 140 - 166 of this chapter provide the primary references to detailed methods of preparing compound 3. The isophytol 6 or phytol 5 required for the preparation of 3 are obtained through multistep synthesis. Starting materials typically include acetone (see Kasparek, in Machlin, Vitamin E: A Comprehensive Treatise, pp. 44-45, Dekker, NY 1980, and references cited therein) and cyclic isoprene tri er (Pond et al., US 3,917,710 and 3,862,988 (1975) . In addition, gamma-tocopherol was first made by total synthesis by Jacob, Steiger, Todd and Wilcox (J. Chem. Soc. 1939, 542) . These workers produced the vitamin by reacting the monobenzoate ester of 2, 3-dimethylhydroquinone with phytyl bromide in the presence of zinc chloride, followed by removal of the benzoate to give a low yield (22%) of gamma-tocopherol. Published syntheses of the tocopherols and tocotrienols were reviewed by S. Kasparek in L. Machlin, "Vitamin E - A Comprehensive Treatise", Dekker, NY, 1980; however, no further methods of preparing gamma-tocopherol have been recorded. Despite the various known methods for preparing or isolating members of the vitamin E family of compounds, there remains a need for improved and more efficient methods of production. BRIEF DESCRIPTION OF THE DRAWINGS Fig. IA illustrates a diagramatic representation of the mevalonate-dependent isoprenoid biosynthetic pathway. Fig. IB illustrates a diagramatic representation of the mevalonate-independent isoprenoid biosynthetic pathway. Fig. 2 illustrates an embodiment of a route for chemical synthesis of vitamin E from geranylgeraniol. Fig. 3 illustrates an embodiment of a route for chemical synthesis of vitamin E from farnesol. Fig. 4 illustrates the growth and farnesol production of strains derived from strain MBNA1-13. Fig. 5 illustrates the growth of wild-type, erg9 and repaired ERG9 strains. Fig. 6 illustrates the production of farnesol in microorganisms with amplified production of HMG CoA reductase . Fig. 7 illustrates the production of farnesol and GG in strains overexpressing GGPP synthases. Fig. 8 illustrates the effect of amplified production of FPP synthase on farnesol and GG production. Fig. 9 illustrates the pathway for metabolic conversion of isoprenol and prenol to farnesol. Fig. 10 illustrates an embodiment of a route of chemical synthesis of gamma-tocopherol. DETAILED DESCRIPTION OF THE INVENTION 1.0 Introduction The present invention provides a method for producing α-tocopherol and α-tocopheryl esters in which a biological system is used to produce farnesol or geranylgeraniol (GG) . Farnesol can be used as a starting material to chemically synthesize the final product, α-tocopheryl esters. Alternatively, the farnesol can be converted chemically to GG. GG, produced biologically or by synthesis from farnesol, can then be used as a starting material to make α-tocopheryl and α-tocopheryl esters. The present invention also includes various aspects of biological materials and intermediates useful in the production of farnesol or GG by biological production. The present invention also includes methods of producing α-tocopherol and α-tocopheryl esters using farnesol and/or GG produced by any means as the starting material. 2.0 Biological Production of Farnesol and GG Isoprenoids are the largest family of natural products, with about 22,000 different structures known. All isoprenoids are derived from the C 5 compound isopentylpyrophosphate (IPP) . Thus, the carbon skeletons of all isoprenoid compounds are created by sequential additions of the C 5 units to the growing polyprenoid chain. While the biosynthetic steps leading from IPP to isoprenoids are universal, two different pathways leading to IPP exist. Fungi (such as yeast) and animals possess the well known mevalonate-dependent pathway (depicted in Fig. IA) which uses acetyl CoA as the initial precursor. Bacteria and higher plants, on the other hand, possess a newly discovered mevalonate independent pathway, also referred to herein as the non-mevalonate pathway, (depicted in Fig. IB) leading from pyruvate and glyceraldehyde 3- phosphate [Lois et al., Proc . Natl . Acad. Sci . USA, 95, 2105-2110 (1998); Rohmer et al . , J. Am. Chem. Soc . 118, 2564-2566 (1996); Arigoni, et al . , Proc . Natl . Acad. Sci . USA, 94, 10600-10605 (1997); Lange et al . , Proc . Na tl . Acad. Sci . USA, 95, 2100-2104 (1998)]. In plants, there is evidence that both the mevalonate-dependent and independent pathways exist, the former being cytosolic and the latter being plastidial [Arigoni, et al . , Proc . Natl . Acad. Sci . USA, 94, 10600-10605 (1997); Lange et al . , Proc . Natl . Acad. Sci . USA, 95, 2100-2104 (1998)]. Several steps of the mevalonate-independent pathway have been established. The first step, catalyzed by D-1-deoxyxylulose 5-phosphate synthase, forms D-1-deoxyxylulose 5-phosphate from pyruvate and glyceraldehyde 3-phosphate. The second and third steps, catalyzed by D-1-deoxyxylulose 5-phosphate reductoisomerase, catalyze the conversion of D-l- deoxyxylulose 5-phosphate to 2-C-methyl D erythritol-4-P (MEP) . Several further reactions are required to convert MEP to IPP, and these enzymes are unknown at this time [Lois et al., Proc . Na tl . Acad. Sci . USA, 95, 2105-2110 (1998); Takahashi et al . , Proc . Natl . Acad. Sci . USA, 95, 2100-2104 (1998); Duvold et al . Tetrahedron Letters, 38, 4769-4772 (1997)]. Farnesol and GG are prenyl alcohols produced by dephosphorylation of farnesylpryrophosphate (FPP) and geranylgeranylpyrophosphate (GGPP) , respectively. FPP and GGPP are intermediates in the biosynthesis of isoprenoid compounds, including sterols, ubiquinones, heme, dolichols, and carotenoids, and are used in the post-translational prenylation of proteins. Both FPP and GGPP are derived from IPP. Embodiments of the present invention include the biological production of farnesol or GG in prokaryotic or eukaryotic cell cultures and cell-free systems, irrespective of whether the organism utilizes the mevalonate-dependent or -independent pathway for the biosynthesis of the precursor of all isoprenoids, IPP. Reference herein to farnesyl phosphate or geranylgeranyl phosphate refers to the respective mono-, di- and tri- phosphate compounds, unless one specific form is specifically designated. 2.1 Modified Microorganism Suitable biological systems for producing farnesol and GG include prokaryotic and eukaryotic cell cultures and cell-free systems. Preferred biological systems include fungal, bacterial and microalgal systems. More preferred biological systems are fungal cell cultures, more preferably a yeast cell culture, and most preferably a Saccharomyces cerevisiae cell culture. Fungi are preferred since they have a long history of use in industrial processes and can be manipulated by both classical microbiological and genetic engineering techniques. Yeast, in particular, are well-characterized genetically. Indeed, the entire genome of S. cerevisiae has been sequenced, and the genes coding for enzymes in the isoprenoid pathway have already been cloned. Also, S . cerevisiae grows to high cell densities, and amounts of squalene and ergosterol (see Fig. 1) up to 16% of cell dry weight have been reported in genetically-engineered strains. For a recent review of the isoprenoid pathway in yeast, see Parks and Casey, Annu . Rev. Microbiol . 49:95-116 (1995). The preferred prokaryote is E. coli . E. coli is well established as an industrial microorganism used in the production of metabolites (amino acids, vitamins) and several recombinant proteins. The entire E. coli genome has also been sequenced, and the genetic systems are highly developed. As mentioned above, E. coli uses the mevalonate-independent pathway for synthesis of IPP. The E. coli dxs, dxr, idi , and ispA genes, encoding D-l- deoxyxylulose 5-phosphate synthase, D-1-deoxyxylulose 5- phosphate reductoisomerase, IPP isomerase, and FPP synthase, respectively, have been cloned and sequenced [Fujisaki, et. al, J. Biochem . 108, 995-1000 (1990); Lois et al., Proc . Natl . Acad. Sci . USA, 95, 2105-2110 (1998); Hemmi et al. , J. Bi ochem. , 123, 1088-1096 (1998)]. Preferred microalga for use in the present invention include Chlorella and Prototheca . Suitable organisms useful in producing farnesol and GG are available from numerous sources, such as the American Type Culture Collection (ATCC) , Rockville, MD, Culture Collection of Algae (UTEX) , Austin, TX, the Northern Regional Research Laboratory (NRRL) , Peoria, IL and the E. coli Genetic Stock Center (CGSC) , New Haven, CT. In particular, there are culture collections of S. cerevisiae that have been used to study the isoprenoid pathway which are available from, e.g., Jasper Rine at the University of California, Berkeley, CA and from Leo Parks at North Carolina State University, Raleigh, NC. Preferably the cells used in the cell culture are genetically modified to increase the yield of farnesol or GG. Cells may be genetically modified by genetic engineering techniques (i.e., recombinant technology), classical microbiological techniques, or a combination of such techniques and can also include naturally occurring genetic variants. Some of such techniques are generally disclosed, for example, in Sambrook et al., 1989, Molecular Cloning: A Laboratory Manual , Cold Spring Harbor Labs Press. The reference Sambrook et al . , ibid. , is incorporated by reference herein in its entirety. A genetically modified microorganism can include a microorganism in which nucleic acid molecules have been inserted, deleted or modified (i.e., mutated; e.g., by insertion, deletion, substitution, and/or inversion of nucleotides) , in such a manner that such modifications provide the desired effect of increased yields of farnesol or GG within the microorganism or in the culture supernatant. As used herein, genetic modifications which result in a decrease in gene expression, in the function of the gene, or in the function of the gene product (i.e., the protein encoded by the gene) can be referred to as inactivation (complete or partial) , deletion, interruption, blockage or down-regulation of a gene. For example, a genetic modification in a gene which results in a decrease in the function of the protein encoded by such gene, can be the result of a complete deletion of the gene (i.e., the gene does not exist, and therefore the protein does not exist) , a mutation in the gene which results in incomplete or no translation of the protein (e.g., the protein is not expressed) , or a mutation in the gene which decreases or abolishes the natural function of the protein (e.g., a protein is expressed which has decreased or no enzymatic activity) . Genetic modifications which result in an increase in gene expression or function can be referred to as amplification, overproduction, overexpression, activation, enhancement, addition, or up-regulation of a gene. Addition of cloned genes to increase gene expression can include maintaining the cloned gene(s) on replicating plasmids or integrating the cloned gene(s) into the genome of the production organism. Furthermore, increasing the expression of desired cloned genes can include operatively linking the cloned gene(s) to native or heterologous transcriptional control elements. 2.1.1 Sgualene Svnthase Modifications Embodiments of the present invention include biological production of farnesol or GG by culturing a microorganism, preferably yeast, which has been genetically modified to modulate the activity of one or more of the enzymes in its isoprenoid biosynthetic pathway. In one embodiment, a microorganism has been genetically modified by decreasing (including eliminating) the action of squalene synthase activity (see Fig. 1) . For instance, yeast erg9 mutants that are unable to convert mevalonate into squalene, and which accumulate farnesol, have been produced. Karst and Lacroute, Molec . Gen . Genet . , 154, 269-277 (1977); U.S. Patent No . 5,589,372. As used herein, reference to erg9 mutant or mutation generally refers to a genetic modification that decreases the action of squalene synthase, such as by blocking or reducing the production of squalene synthase, reducing squalene synthase activity, or inhibiting the activity of squalene synthase, which results in the accumulation of farnesyl diphosphate (FPP) unless the FPP is otherwise converted to another compound, such as farnesol by phosphatase activity. Blocking or reducing the production of squalene synthase can include placing the ERG9 gene under the control of a promoter that requires the presence of an inducing compound in the growth medium. By establishing conditions such that the inducer becomes depleted from the medium, the expression of ERG9 (and therefore, squalene synthase synthesis) could be turned off. Also, some promoters are turned off by the presence of a repressing compound. For example, the promoters from the yeast CTR3 or CTR1 genes can be repressed by addition of copper. Blocking or reducing the activity of squalene synthase could also include using an excision technology approach similar to that described in U.S. Patent No. 4,743,546, incorporated herein by reference. In this approach, the ERG9 gene is cloned between specific genetic sequences that allow specific, controlled excision of the ERG9 gene from the genome. Excision could be prompted by, for example, a shift in the cultivation temperature of the culture, as in U.S. Patent No. 4,743,546, or by some other physical or nutritional signal. Such a genetic modification includes any type of modification and specifically includes modifications made by recombinant technology and by classical mutagenesis. Inhibitors of squalene synthase are known (see U.S. Patent No. 4,871,721 and the references cited in U.S. Patent No. 5,475,029) and can be added to cell cultures. In another embodiment, an organism having the mevalonate-independent pathway of isoprenoid biosynthesis (such as E. coli ) is genetically modified so that it accumulates FPP and/or farnesol. For example, decreasing the activity of octaprenyl pyrophosphate synthase (the product of the ispB gene) would be expected to result in FPP accumulation in E. coli . (Asai, et al., Biochem. Biophys. Res. Comm. 202, 340-345 (1994)). The action of a phosphatase could further result in farnesol accumulation in E. coli . Yeast strains need ergosterol for cell membrane fluidity, so mutants blocked in the ergosterol pathway, such as erg9 mutants, need extraneous ergosterol or other sterols added to the medium for the cells to remain viable. The cells normally cannot utilize this additional sterol unless grown under anaerobic conditions. Therefore, a further embodiment of the present invention is the use of a yeast in which the action of squalene synthase is reduced, such as an erg9 mutant, and which takes up exogenously supplied sterols under aerobic conditions. Genetic modifications which allow yeast to utilize sterols under aerobic conditions are demonstrated below in the Examples section (see Example 1) and are also known in the art. For example, such genetic modifications include upc (uptake control mutation which allows cells to take up sterols under aerobic conditions) and heml (the HEM1 gene encodes aminolevulinic acid synthase which is the first committed step to the heme biosynthetic pathway from FPP, and heml mutants are capable of taking up ergosterol under aerobic conditions following a disruption in the ergosterol biosynthetic pathway, provided the cultures are supplemented with unsaturated fatty acids) . Yeast strains having these mutations can be produced using known techniques and also are available from, e.g., Dr. Leo Parks, North Carolina State University, Raleigh, NC. Haploid cells containing these mutations can be used to generate other mutants by genetic crosses with other haploid cells. Also, overexpression of the SUT1 (sterol uptake) gene can be used to allow for uptake of sterols under aerobic conditions. The SUT1 gene has been cloned and sequenced. Bourot and Karst, Gene, 165: 97-102 (1995) . In a further embodiment, microorganisms of the present invention can be used to produce farnesol and/or GG by culturing microorganisms in the presence of a squalene synthase inhibitor. In this manner, the action of squalene synthase is reduced. Squalene synthase inhibitors are known to those skilled in the art. (See, for example, U.S. Patent No. 5,556, 990. 2.1.2 HMG-CoA Reductase Modifications A further embodiment of the present invention is the use of a microorganism which has been genetically modified to increase the action of HMG-CoA reductase. It should be noted that reference to increasing the action of HMG-CoA reductase and other enzymes discussed herein refers to any genetic modification in the microorganism in question which results in increased functionality of the enzymes and includes higher activity of the enzymes, reduced inhibition or degradation of the enzymes and overexpression of the enzymes. For example, gene copy number can be increased, expression levels can be increased by use of a promoter that gives higher levels of expression than that of the native promoter, or a gene can be altered by genetic engineering or classical mutagenesis to increase the activity of an enzyme. One of the key enzymes in the mevalonate-dependent isoprenoid biosynthetic pathway is HMG-CoA reductase which catalyzes the reduction of 3- hydroxy-3-methylglutaryl-coenzyme A (HMG-CoA) . This is the primary rate-limiting and first irreversible step in the pathway, and increasing HMG-CoA reductase activity leads to higher yields of squalene and ergosterol in a wild-type strain of S . cerevisiae, and farnesol in an erg9 strain. One mechanism by which the action of HMG-CoA reductase can be increased is by reducing inhibition of the enzyme, by either genetically modifying the enzyme or by modifying the system to remove the inhibitor. For instance, both sterol and non-sterol products of the isoprenoid pathway feedback inhibit this enzyme (see, e.g., Parks and Casey, Annu . Rev. Microbiol . 49:95-116 (1995) . Alternatively or in addition, the gene(s) coding for HMG-CoA reductase can be altered by genetic engineering or classical mutagenesis techniques to decrease or prevent inhibition. Also, the action of HMG- CoA reductase can be increased by increasing the gene copy number, by increasing the level of expression of the HMG- CoA reductase gene(s), or by altering the HMG-CoA reductase gene(s) by genetic engineering or classical mutagenesis to increase the activity of the enzyme. See U.S. Patent No. 5,460,949, the entire contents of which are incorporated herein by reference. For example, truncated HMG-CoA reductases have been produced in which the regulatory domain has been removed and the use of gene copy numbers up to about six also gives increased activity. Id. See also, Downing et al., Bi ochem . Bi ophys . Res . Commun . , 94, 974-79 (1980) describing two yeast mutants having increased levels of HMG-CoA reductase. Two isozymes of HMGCoA reductase, encoded by the HMG1 and HMG2 genes, exist in S. cerevisiae . The activity of these two isozymes is regulated by several mechanisms including regulation of transcription, regulation of translation, and for Hmg2p, degradation of the enzyme in the endoplasmic reticulum (Hampton and Rine, 1994; Donald, et. al . 1997) . In both Hmglp and Hmg2p, the catalytic domain resides in the " COOH terminal portion of the enzyme, while the regulatory domain resides in the membrane spanning NH 2 -terminal region. It has been shown that overexpression of just the catalytic domain of Hmglp in 5. cerevi si ae increases carbon flow through the isoprenoid pathway, resulting in overproduction of squalene (Saunders, et. al . 1995; Donald, et . al . , 1997) . The present inventors have expressed the catalytic domain of the S. cerevisiae Hmg2p in strains having a normal (i.e., unblocked) isoprenoid pathway and observed a significant increase in the production of squalene. Furthermore, overexpression of the catalytic domain of Hmg2p resulted in increased farnesol production in an erg9 mutant, and increased farnesol and GG production in an erg9 mutant overexpressing GGPP synthase, grown in fermentors. 2.1.3 GGPP Synthase Modifications A further embodiment of the present invention is the use of a microorganism which has been genetically modified to increase the action of GGPP synthase. Genes coding for this enzyme from a variety of sources, including bacteria, fungi, plants, mammals, and archaebacteria, have been identified. See, Brinkhaus et al . , Arch. Biochem. Biophys., 266, 607-612 (1988); Carattoli et al . , J. Biol. Chem., 266, 5854-59 (1991); Chen et al . , J. Biol. Chem., 268, 11002-11007 (1993); Dogbo et al . , Biochim. Biophys. Acta, 920, 140-148 (1987); Jiang et al . , J. Biol. Chem., 270, 21793-99 (1995); Kuntz al . , Plant J. , 2, 25-34 (1992); Laferriere, et al., Biochim. Biophys. Acta, 1077, 167-72 (1991); Math et al . , Proc. Natl. Acad. Sci. USA, 89, 6761- 64 (1992); Ohnuma et al . , J. Biol. Chem., 269, 14792-97 (1994); Sagami et al., Arch. Biochem. Biophys., 297, 314-20 (1992); Sagami et al., J. Biol. Chem., 269, 20561-66 (1994); Sandmann et al., J. Photochem. Photobiol. B: Biol., 18, 245-51 (1993); Scolnik et al . , Plant Physiol., 104, 1469-70 (1994); Tachibana et al., Biosci. Biotech. Biochem., 1, 1129-33 (1993); Tachibana et al . , J. Biochem. , 114, 389-92 (1993); Wiede ann et al . , Arch. Biochem. Biophys., 306, 152-57 (1993). Some organisms have a bifunctional enzyme which also serves as an FPP synthase, so it is involved in the overall conversion of IPP and DMAPP to FPP to GGPP (see Fig. 1) . Some enzymes, such as those found in plants, have relaxed specificity, converting IPP and DMAPP to GGPP (see Fig. 1) . Genetic modifications of GGPP synthase, as used herein, encompass engineering a monofunctional GGPP synthase or a bifunctional FPP/GGPP synthase to enhance the GGPP synthase activity component of the enzyme. A preferred GGPP synthase gene is the BTS1 gene from S. cervisiae . The BTS1 gene and its isolation are described in Jiang et al . , J. Biol . Chem. , 270, 21793- 99 (1995) and copending application Serial No. 08/761,344, filed on December 6, 1996, the complete disclosure of which incorporated herein by reference. However, GGPP synthases of other hosts can be used, and the use of the bifunctional GGPP synthases may be particularly advantageous in terms of channeling carbon flow through FPP to GGPP, thereby avoiding loss of FPP to competing reactions in the cell. In further embodiments of the invention, in addition to the modifications of GGPP synthase described above, the wild type GGPP synthase is eliminated from the production organism. This would serve, for example, to eliminate competition between the modified GGPP synthase and the wild type enzyme for the substrates, FPP and IPP. Deletion of the wild-type gene encoding GGPP synthase could also improve the stability of the cloned GGPP synthase gene by removing regions of high genetic sequence homology, thereby avoiding potentially detrimental genetic recombination. 2.1.4 FPP Synthase Modifications A further embodiment of the present invention is the use of a microorganism which has been genetically modified to increase the action of FPP synthase . Genes coding for this enzyme from a variety of sources have been identified. See, Anderson et al., J. Biol . Chem. , 264, 19176-19184 (1989); Attucci, et al . , Arch . Biochem . Biophys . , 321, 493-500 (1995); Cane et al., J. Am. Chem . Soc , 105, 122-124 (1983); Chambon et al . , Current Genetics, 18, 41-46 (1990);, Chambon et al . , Lipids, 26, 633-36 (1991); Chen al., Protein Science, 3, 600-607 (1994); Davisson, et al., J. Am. Chem. Soc , 115, 1235-45 (1993); Ding et al . , Biochem. J. , 275, 61-65 (1991); Hugueney et al., FEBS Letters, 273, 235-38 (1990); Joly et al., J. Biol . Chem. , 268, 26983-89 (1993); Koyama al . , J. Bi ochem. , 113, 355-63 (1993); Sheares, et al . , Bi ochem . , 28, 8129-35 (1989); Song et al . , Proc Natl . Acad. Sci . USA, 91, 3044-48 (1994); Spear et al . , J. Biol . Chem. , 267, 14662-69 (1992); Spear et al., J. Biol . Chem. , 269, 25212- 18 (1994). Anderson et al . , J. Biol . Chem. , 264, 19176- 19184 (1989) reported a 2-3 fold overexpression of FPP synthase with the S. cerevisiae gene in a yeast shuttle vector. As described in the Examples section, it has been surprisingly found that overexpression of FPP synthase did not lead to an increase in farnesol production, but unexpectedly lead to an increase in the production of GG in the absence of any overexpression of GGPP synthase. In further embodiments of the invention, in addition to the modifications of FPP synthase described above, the wild type FPP synthase is eliminated from the production organism. This would serve, for example, to eliminate competition between the modified FPP synthase and the wild type enzyme for the substrates, IPP, DMAPP and GPP. Deletion of the wild-type gene encoding FPP synthase could also improve the stability of the cloned FPP synthase gene by removing regions of high genetic sequence homology, thereby avoiding potentially detrimental genetic recombination. 2.1.5 Phosphatase Modifications A further embodiment of the present invention is the use of a microorganism which has been genetically modified to increase phosphatase action to increase conversion of FPP to farnesol or GGPP to GG. For example, both S. cerevisiae and E. coli contain numerous phosphatase activities. By testing several phosphatases for efficient dephosphorylation of FPP or GGPP, one could select an appropriate phosphatase and express the gene encoding this enzyme in a production organism to enhance farnesol or GG production. In addition to (or instead of) increasing the action of a desired phosphatase to enhance farnesol or GG production, one could eliminate, through genetic means, undesirable phosphatase activities. For example, one could eliminate through mutation the activity of a phosphatase that specifically acts on FPP, so that the FPP that was spared would be available for conversion to GGPP and subsequently GG. 2.1.6 Additional Genetic Modifications. Modifications of Other Isoprenoid Pathway Enzymes. Modifications that can be made to increase the action of HMGCoA reductase, GGPP synthase and phosphatases are described above. Modification of the action of isoprenoid pathway enzymes is not limited to those specific examples, and similar strategies can be applied to modify the action of other isoprenoid pathway enzymes such as acetoacetyl Co- A thiolase, HMG-CoA synthase, mevalonate kinase, phosphomevalonate kinase, phosphomevalonate decarboxylase, IPP isomerase, farnesyl pyrophosphate synthase or D-l- deoxyxylulose 5-phosphate synthase D-1-deoxyxylulose 5- phosphate reductoisomerase . Engineering of Central Metabolism to Increase Precursor Supply to the Isoprenoid Pathway. In organisms having the mevalonate-dependent isoprenoid pathway, the biosynthesis of farnesol or GG begins with acetyl CoA (refer to Figure 1) . One embodiment of the present invention is genetic modification of the production organism such that the intracellular level of acetyl CoA is increased, thereby making more acetyl CoA available for direction to the isoprenoid pathway (and hence to farnesol and/or GG) . For example, the supply to acetyl CoA can be increased by increasing the action of the pyruvate dehydrogenase complex. The supply of acetyl CoA can be further increased by increasing the level of pyruvate in the cell by increasing the action of pyruvate kinase. In organisms having the mevalonate-independent isoprenoid pathway, the biosynthesis of isoprenoids begins with pyruvate and glyceraldehyde 3-phosphate. The supply of pyruvate and glyceraldehyde 3-phosphate available for isoprenoid biosynthesis can be increased by increasing the action of pyruvate kinase and triophosphate isomerase, respectively. The examples above are provided only to illustrate the concept of engineering central metabolism for the purpose of increasing production of isoprenoid compounds, and are not an exhaustive list of approaches that can be taken. Numerous other strategies could be successfully applied to achieve this goal. Blocking Pathways that Compete for FPP or GGPP. In yeast, FPP is a branch point intermediate leading to the biosynthesis of sterols, heme, dolichol, ubiquinone, GGPP and farnesylated proteins. In E. coli , FPP serves as the substrate for octaprenyl pyrophosphate synthase in the pathway leading to ubiquinone. In bacteria that synthesize carotenoids, such as Erwina uredovora, FPP is converted to GGPP by GGPP synthase in the first step leading to the carotenoids. To increase the production of farnesol or GG, it is desirable to inactivate genes encoding enzymes that use FPP or GGPP as substrate, or to reduce the activity of the enzymes themselves, either through mutation or the use of specific enzyme inhibitors (as was discussed above for squalene synthase) . In S . cerevisiae, for example, it may be advantageous to inactivate the first step in the pathway from FPP to heme, in addition to inactivating ERG9. As discussed earlier, in E. coli , partial or complete inactivation of the octaprenyl pyrophosphate synthase could increase the availability of FPP for conversion of farnesol. Finally, in bacteria that produce carotenoids, such as Erwina uredovora, elimination of GGPP synthase can increase the level of FPP for conversion of farnesol, while inactivating or reducing the activity of phytoene synthase (the crtB gene product) can increase the level of GGPP available for conversion to GG. It is possible that blocking pathways leading away from FPP or GGPP could have negative effects on the growth and physiology of the production organism. It is further contemplated that additional genetic modifications required to offset these complications can be made. The isolation of mutants of S. cerevisiae that are blocked in the isoprenoid pathway and take up sterols under aerobic conditions, as described above, illustrates that compensating mutations can be obtained that overcome the effects of the primary genetic modifications. Isolation of Production Strains that are Resistant to Farnesol or GG. In the Examples section, production of high levels of farnesol and GG by genetically modified strains of S. cerevisiae is described. It is recognized that as further increases in farnesol or GG production are made, these compounds may reach levels that are toxic to the production organism. Indeed, product toxicity is a common problem encountered in biological production processes. However, just as common are the genetic modifications made by classical methods or recombinant technology that overcome product toxicity. The present invention anticipates encountering product toxicity. Thus a further embodiment of this invention is the isolation of mutants with increased resistance to farnesol and/or GG. Isolation of Production Organisms with Improved Growth Properties . One effect of blocking the isoprenoid pathway in S . cerevisiae is that the mutant organisms (in the present invention, erg9 mutants) grow more slowly than their parent (unblocked) strains, despite the addition of ergosterol to the culture medium. That the slower growth of the erg9 mutants is due to the block at erg9 is illustrated in Example l.G, which shows that repairing the erg9 mutation restores the growth rate of the strain to about that of the wild-type parent. The slower growth of the erg9 mutants could be due to differences related to growing on exogenously supplied ergosterol vs. ergosterol synthesized in the cell, or could be due to other physiological factors. One embodiment of the present invention is to isolate variants of the farnesol or GG producing strains with improved growth properties. This could be achieved, for example by continuous culture, selecting for faster growing variants. Such variants could occur spontaneously or could be obtained by classical mutagenesis or molecular genetic approaches. 2.2 Incorporation of Prenol and Isoprenol In a further embodiment of the present invention, farnesol or GG is produced by the introduction of isoprenol and/or prenol into a fermentation medium. With reference to Fig. 9, each of these compounds, when taken up by an organism is phosphorylated with a pyrophosphate group to form, respectively, 3-isopentenyl pyrophosphate and 3,3-dimethylallyl pyrophosphate. These two compounds interconvert by the action of isopentenyl pyrophosphate isomerase. These compounds are then converted to farnesyl pyrophosphate by the action of FPP synthase. Farnesol is formed by dephosphorylation of farnesyl pyrophosphate. Farnesyl pyrophosphate can be further converted to geranylgeranyl pyrophosphate. Geranylgeraniol is formed be dephosyphorylation of geranylgeranyl pyrophosphate. GG would be formed from FPP by the combined action of GGPP synthase and a phosphatase. Isoprenol and prenol are commercially available compounds and can be produced by methods known in the art In this embodiment, the microorganism used in the fermentation can be any microorganism as described elsewhere herein. In addition, the microorganism can be genetically modified to increase the action of dimethylallyl transferase to promote the production of geranyl pyrophosphate and farnesol pyrophosphate. Genes coding for this enzyme from a variety of sources have been identified [Chen et al., Protein Sci . , 3, 600-607 (1994)]. In addition a microorganism can be genetically modified to increase the action of isoprenol kinase or prenol kinase. Although these enzymes have not been discovered, similar enzymes that phosphorylate farnesol and geranylgeraniol have been described [Bentinger et al., Arch . Biochem . Biophys . , 353, 191-198 (1998); Ohnuma et al., J . Biochem . , 119, 541-547 (1996)]. 2.3 Fermentation Media and Conditions In the method for production of farnesol or GG, a microorganism having a genetically modification, as discussed above is cultured in a fermentation medium for production of farnesol or GG. An appropriate, or effective, fermentation medium refers to any medium in which a genetically modified microorganism of the present invention, when cultured, is capable of producing farnesol or GG. Such a medium is typically an aqueous medium comprising assimilable carbon, nitrogen and phosphate sources. Such a medium can also include appropriate salts, minerals, metals and other nutrients. In addition, when an organism which is blocked in the ergosterol pathway and requires exogenous sterols, the fermentation medium must contain such exogenous sterols. Appropriate exemplary media are shown in the discussion below and in the Examples section. It should be recognized, however, that a variety of fermentation conditions are suitable and can be selected by those skilled in the art. Sources of assimilable carbon which can be used in a suitable fermentation medium include, but are not limited to, sugars and their polymers, including, dextrin, sucrose, maltose, lactose, glucose, fructose, mannose, sorbose, arabinose and xylose; fatty acids; organic acids such as acetate; primary alcohols such as ethanol and n-propanol; and polyalcohols such as glycerine. Preferred carbon sources in the present invention include monosaccharides, disaccharides, and trisaccharides. The most preferred carbon source is glucose. The concentration of a carbon source, such as glucose, in the fermentation medium should promote cell growth, but not be so high as to repress growth of the microorganism used. Typically, fermentations are run with a carbon source, such as glucose, being added at levels to achieve the desired level of growth and biomass, but at undetectable levels (with detection limits being about <0.1g/l). In other embodiments, the concentration of a carbon source, such as glucose, in the fermentation medium is greater than about 1 g/L, preferably greater than about 2 g/L, and more preferably greater than about 5 g/L. In addition, the concentration of a carbon source, such as glucose, in the fermentation medium is typically less than about 100 g/L, preferably less than about 50 g/L, and more preferably less than about 20 g/L. It should be noted that references to fermentation component concentrations can refer to both initial and/or ongoing component concentrations. In some cases, it may be desirable to allow the fermentation medium to become depleted of a carbon source during fermentation. Sources of assimilable nitrogen which can be used in a suitable fermentation medium include, but are not limited to, simple nitrogen sources, organic nitrogen sources and complex nitrogen sources. Such nitrogen sources include anhydrous ammonia, ammonium salts and substances of animal, vegetable and/or microbial origin. Suitable nitrogen sources include, but are not limited to, protein hydrolysates, microbial biomass hydrolysates, peptone, yeast extract, ammonium sulfate, urea, and amino acids. Typically, the concentration of the nitrogen sources, in the fermentation medium is greater than about 0.1 g/L, preferably greater than about 0.25 g/L, and more preferably greater than about 1.0 g/L. Beyond certain concentrations, however, the addition of a nitrogen source to the fermentation medium is not advantageous for the growth of the microorganisms. As a result, the concentration of the nitrogen sources, in the fermentation medium is less than about 20 g/L, preferably less than about 10 g/L and more preferably less than about 5 g/L. Further, in some instances it may be desirable to allow the fermentation medium to become depleted of the nitrogen sources during fermentation. The effective fermentation medium can contain other compounds such as inorganic salts, vitamins, trace metals or growth promoters. Such other compounds can also be present in carbon, nitrogen or mineral sources in the effective medium or can be added specifically to the medium. The fermentation medium can also contain a suitable phosphate source. Such phosphate sources include both inorganic and organic phosphate sources. Preferred phosphate sources include, but are not limited to, phosphate salts such as mono or dibasic sodium and potassium phosphates, ammonium phosphate and mixtures thereof. Typically, the concentration of phosphate in the fermentation medium is greater than about 1.0 g/L, preferably greater than about 2.0 g/L and more preferably greater than about 5.0 g/L. Beyond certain concentrations, however, the addition of phosphate to the fermentation medium is not advantageous for the growth of the microorganisms. Accordingly, the concentration of phosphate in the fermentation medium is typically less than about 20 g/L, preferably less than about 15 g/L and more preferably less than about 10 g/L. A suitable fermentation medium can also include a source of magnesium, preferably in the form of a physiologically acceptable salt, such as magnesium sulfate heptahydrate, although other magnesium sources in concentrations which contribute similar amounts of magnesium can be used. Typically, the concentration of magnesium in the fermentation medium is greater than about 0.5 g/L, preferably greater than about 1.0 g/L, and more preferably greater than about 2.0 g/L. Beyond certain concentrations, however, the addition of magnesium to the fermentation medium is not advantageous for the growth of the microorganisms. Accordingly, the concentration of magnesium in the fermentation medium is typically less than about 10 g/L, preferably less than about 5 g/L, and more preferably less than about 3 g/L. Further, in some instances it may be desirable to allow the fermentation medium to become depleted of a magnesium source during fermentation. The fermentation medium can also include a biologically acceptable chelating agent, such as the dihydrate of trisodium citrate. In such instance, the concentration of a chelating agent in the fermentation medium is greater than about 0.2 g/L, preferably greater than about 0.5 g/L, and more preferably greater than about 1 g/L. Beyond certain concentrations, however, the addition of a chelating agent to the fermentation medium is not advantageous for the growth of the microorganisms. Accordingly, the concentration of a chelating agent in the fermentation medium is typically less than about 10 g/L, preferably less than about 5 g/L, and more preferably less than about 2 g/L. The fermentation medium can also initially include a biologically acceptable acid or base to maintain the desired pH of the fermentation medium. Biologically acceptable acids include, but are not limited to, hydrochloric acid, sulfuric acid, nitric acid, phosphoric acid and mixtures thereof. Biologically acceptable bases include, but are not limited to, ammonium hydroxide, sodium hydroxide, potassium hydroxide and mixtures thereof. In a preferred embodiment of the present invention, the base used is ammonium hydroxide . The fermentation medium can also include a biologically acceptable calcium source, including, but not limited to, calcium chloride. Typically, the concentration of the calcium source, such as calcium chloride, dihydrate, in the fermentation medium is within the range of from about 5 mg/L to about 2000 mg/L, preferably within the range of from about 20 mg/L to about 1000 mg/L, and more preferably in the range of from about 50 mg/L to about 500 mg/L. The fermentation medium can also include sodium chloride. Typically, the concentration of sodium chloride in the fermentation medium is within the range of from about 0.1 g/L to about 5 g/L, preferably within the range of from about 1 g/L to about 4 g/L, and more preferably in the range of from about 2 g/L to about 4 g/L. As previously discussed, the fermentation medium can also include trace metals. Such trace metals can be added to the fermentation medium as a stock solution that, for convenience, can be prepared separately from the rest of the fermentation medium. A suitable trace metals stock solution for use in the fermentation medium is shown below in Table 1. Typically, the amount of such a trace metals solution added to the fermentation medium is greater than about 1 ml/L, preferably greater than about 5 mL/L, and more preferably greater than about 10 mL/L. Beyond certain concentrations, however, the addition of a trace metals to the fermentation medium is not advantageous for the growth of the microorganisms. Accordingly, the amount of such a trace metals solution added to the fermentation medium is typically less than about 100 mL/L, preferably less than about 50 mL/L, and more preferably less than about 30 mL/L. It should be noted that, in addition to adding trace metals in a stock solution, the individual components can be added separately, each within ranges corresponding independently to the amounts of the components dictated by the above ranges of the trace metals solution. As shown below in Table 1, a suitable trace metals solution for use in the present invention can include, but is not limited to ferrous sulfate, heptahydrate; cupric sulfate, pentahydrate; zinc sulfate, heptahydrate; sodium molybdate, dihydrate; cobaltous chloride, hexahydrate; and manganous sulfate, monohydrate. Hydrochloric acid is added to the stock solution to keep the trace metal salts in solution. TABLE 1 TRACE METALS STOCK SOLUTION The fermentation medium can also include vitamins. Such vitamins can be added to the fermentation medium as a stock solution that, for convenience, can be prepared separately from the rest of the fermentation medium. A suitable vitamin stock solution for use in the fermentation medium is shown below in Table 2. Typically, the amount of such vitamin solution added to the fermentation medium is greater than 1 ml/L, preferably greater than 5 ml/L and more preferably greater than 10 ml/L. Beyond certain concentrations, however, the addition of vitamins to the fermentation medium is not advantageous for the growth of the microorganisms. Accordingly, the amount of such a vitamin solution added to the fermentation medium is typically less than about 50 ml/L, preferably less than 30 ml/L and more preferably less than 20 ml/L. It should be noted that, in addition to adding vitamins in a stock solution, the individual components can be added separately each within the ranges corresponding independently to the amounts of the components dictated by the above ranges of the vitamin stock solution. As shown in Table 2, a suitable vitamin solution for use in the present invention can include, but is not limited to, biotin, calcium pantothenate, inositol, pyridoxine-HCl and thiamine-HCl . Table 2 As stated above, when an organism is blocked in the sterol pathway, an exogenous sterol must be added to the fermentation medium. Such sterols include, but are not limited to, ergosterol and cholesterol. Such sterols can be added to the fermentation medium as a stock solution that is prepared separately from the rest of the fermentation medium. Sterol stock solutions can be prepared using a detergent to aid in solubilization of the sterol. A typical ergosterol stock solution is described in Example l.D. Typically, an amount of sterol stock solution is added to the fermentation medium such that the final concentration of the sterol in the fermentation medium is within the range of from about 1 mg/L to 3000 mg/L, preferably within the range from about 2 mg/L to 2000 mg/L, and more preferably within the range from about 5 mg/L to 2000 mg/L. Microorganisms of the present invention can be cultured in conventional fermentation modes, which include, but are not limited to, batch, fed-batch, cell recycle, and continuous. It is preferred, however, that the fermentation be carried out in fed-batch mode. In such a case, during fermentation some of the components of the medium are depleted. It is possible to initiate the fermentation with relatively high concentrations of such components so that growth is supported for a period of time before additions are reguired. The preferred ranges of these components are maintained throughout the fermentation by making additions as levels are depleted by fermentation. Levels of components in the fermentation medium can be monitored by, for example, sampling the fermentation medium periodically and assaying for concentrations. Alternatively, once a standard fermentation procedure is developed, additions can be made at timed intervals corresponding to known levels at particular times throughout the fermentation. As will be recognized by those in the art, the rate of consumption of nutrient increases during fermentation as the cell density of the medium increases. Moreover, to avoid introduction of foreign microorganisms into the fermentation medium, addition is performed using aseptic addition methods, as are known in the art. In addition, a small amount of anti- foaming agent may be added during the fermentation. The temperature of the fermentation medium can be any temperature suitable for growth and production of farnesol or GG. For example, prior to inoculation of the fermentation medium with an inoculum, the fermentation medium can be brought to and maintained at a temperature in the range of from about 20°C to about 45°C, preferably to a temperature in the range of from about 25°C to about 40°C, and more preferably in the range of from about 28°C to about 32°C. The pH of the fermentation medium can be controlled by the addition of acid or base to the fermentation medium. In such cases when ammonia is used to control pH, it also conveniently serves as a nitrogen source in the fermentation medium. Preferably, the pH is maintained from about 3.0 to about 8.0, more preferably from about 3.5 to about 7.0, and most preferably from about 4.0 to about 6.5. The fermentation medium can also be maintained to have a dissolved oxygen content during the course of fermentation to maintain cell growth and to maintain cell metabolism for production of farnesol or GG. The oxygen concentration of the fermentation medium can be monitored using known methods, such as through the use of an oxygen electrode. Oxygen can be added to the fermentation medium using methods known in the art, for , through agitation and aeration of the medium by stirring, shaking or sparging. Preferably, the oxygen concentration in the fermentation medium is in the range of from about 20% to about 100% of the saturation value of oxygen in the medium based upon the solubility of oxygen in the fermentation medium at atmospheric pressure and at a temperature in the range of from about 20°C to about 40°C. Periodic drops in the oxygen concentration below this range may occur during fermentation, however, without adversely affecting the fermentation. Although aeration of the medium has been described herein in relation to the use of air, other sources of oxygen can be used. Particularly useful is the use of an aerating gas which contains a volume fraction of oxygen greater than the volume fraction of oxygen in ambient air. In addition, such aerating gases can include other gases which do not negatively affect the fermentation. In an embodiment of the fermentation process of the present invention, a fermentation medium is prepared as described above and in Example l.H. This fermentation medium is inoculated with an actively growing culture of microorganisms of the present invention in an amount sufficient to produce, after a reasonable growth period, a high cell density. Typical inoculation cell densities are within the range of from about 0.01 g/L to about 10 g/L, preferably from about 0.2 g/L to about 5 g/L and more preferably from about 0.05 g/L to about 1.0 g/L, based on the dry weight of the cells. In production scale fermentors, however, greater inoculum cell densities are preferred. The cells are then grown to a cell density in the range of from about 10 g/L to about 100 g/L preferably from about 20 g/L to about 80 g/L, and more preferably from about 50 g/L to about 70 g/L. The residence times for the microorganisms to reach the desired cell densities during fermentation are typically less than about 200 hours, preferably less than about 120 hours, and more preferably less than about 96 hours. In one mode of operation of the present invention, the carbon source concentration, such as the glucose concentration, of the fermentation medium is monitored during fermentation. Glucose concentration of the fermentation medium can be monitored using known techniques, such as, for example, use of the glucose oxidase enzyme test or high pressure liquid chromatography, which can be used to monitor glucose concentration in the supernatant, e.g., a cell-free component of the fermentation medium. As stated previously, the carbon source concentration should be kept below the level at which cell growth inhibition occurs. Although such concentration may vary from organism to organism, for glucose as a carbon source, cell growth inhibition occurs at glucose concentrations greater than at about 60 g/L, and can be determined readily by trial. Accordingly, when glucose is used as a carbon source the glucose is preferably fed to the fermentor and maintained below detection limits. Alternatively, the glucose concentration in the fermentation medium is maintained in the range of from about 1 g/L to about 100 g/L, more preferably in the range of from about 2 g/L to about 50 g/L, and yet more preferably in the range of from about 5 g/L to about 20 g/L. Although the carbon source concentration can be maintained within desired levels by addition of, for example, a substantially pure glucose solution, it is acceptable, and may be preferred, to maintain the carbon source concentration of the fermentation medium by addition of aliquots of the original fermentation medium. The use of aliquots of the original fermentation medium may be desirable because the concentrations of other nutrients in the medium (e.g. the nitrogen and phosphate sources) can be maintained simultaneously. Likewise, the trace metals concentrations can be maintained in the fermentation medium by addition of aliquots of the trace metals solution. 2.4 Farnesol and GG Recovery Once farnesol or GG are produced by a biological system, they are recovered or isolated for subsequent chemical conversion to to α-tocopherol or α-tocopheryl esters. The present inventors have shown that for both farnesol and GG, the product may be present in culture supernatants and/or associated with the yeast cells. With respect to the cells, the recovery of farnesol or GG includes some method of permeabilizing or lysing the cells. The farnesol or GG in the culture can be recovered using a recovery process including, but not limited to, chromatography, extraction, solvent extraction, membrane separation, electrodialysis, reverse osmosis, distillation, chemical derivatization and crystallization. When the product is in the phosphate form, i.e., farnesyl phosphate or geranylgeranyl phosphate, it only occurs inside of cells and therefore, requires some method of permeabilizing or lysing the cells. 3.0 Chemical Synthesis of GG and Farnesol 3.1 Chemical Synthesis of GG As noted above, in one embodiment of the invention, GG is produced biologically, and in alternate embodiments, GG can be produced by other methods. For example, GG can also be produced from farnesol by chemical synthesis. Many suitable methods are known in the art. In one such method, farnesol is converted to farnesyl bromide (PBr 3 in ether) and subjected to displacement with ethyl acetoacetate. The resulting crude keto ester is saponified, decarboxylated, and the resulting ketone purified by distillation. Following the procedure of Klinge and De uth ( Synlett 1993, 783), the ketone is subjected to Wittig-Horner reaction with diisopropyl ethylphosphonoacetate (NaH, glyme) to give an approximately 80/20 mixture of t,t,t- and t,t,c-ethyl geranylgeranoate. Reduction of ethyl geranylgeranoate with diisobutylaluminum hydride provides GG cleanly. The t,t,t- and t,t-c- mixture can be separated at the ester (e.g., by distillation) or alcohol (e.g., by crystallization as described in EP 711749) oxidation level. The production of farnesol as a starting material for the chemical production of GG can be accomplished by biological production, such as by use of a modified microorganism having some of the modified characteristics described above. 3.2 Chemical Synthesis of Farnesol As noted above, in one embodiment of the invention, farnesol is produced biologically, and in alternate embodiments, farnesol can be produced by other methods. For example, farnesol can also be produced by chemical synthesis. Many suitable methods are known in the art. 4.0 Production of Tocopherol from GG by Chemical Synthesis In a further embodiment of the present invention, a method for producing vitamin E from geranylgeraniol is provided. Geranylgeraniol contains four olefin moieties. As used in this invention, the olefin moieties of geranylgeraniol are consecutively numbered starting from the hydroxy terminus, i.e., the first olefin moiety refers to C 2 -C 3 double bond, the second olefin moiety refers to C 6 - C 7 double bond, the third olefin moiety refers to C 10 -C double bond and the fourth olefin moiety refers to C 14 -C 15 double bond. The method of the present invention involves reducing at least one olefin moiety of geranylgeraniol to form an allylic alcohol. Preferably the allylic alcohol is phytol and/or isophytol. The formation of the allylic alcohol can be achieved by a selective reduction of olefins which reduces at least one of the second, third or fourth olefin moieties without reducing the first olefin moiety. Preferably the reduction reduces all olefin moieties except the first olefin moiety. The reduction of an olefin moiety can be accomplished by any of the known alkene reduction conditions including diimide reduction; dissolving metal reduction; metal hydride reduction; and hydrogenation in the presence of a metal catalyst such as palladium, rhodium, nickel, platinum, ruthenium, copper, chromium or a combination thereof. Preferably, the second, third and fourth olefin moieties are reduced by hydrogenation. If an enantiomerically enriched or enantiomerically pure vitamin E synthesis is desired, one can effect the reduction of olefin moiety using an asymmetric catalyst such as those known in the art for asymmetric hydrogenation reactions . Alternatively, a racemic mixture of allylic alcohol can be produced and subjected to a chiral separation to provide a desired stereo isomer of the allylic alcohol. In one embodiment of the present invention, a protecting group is added to geranylgeraniol prior to reducing the second, third and/or fourth olefin moieties. As used in this invention, a protecting group refers to any compound which can be added to (or combined with) geranylgeraniol prior to reduction of one or more olefin moieties and removed after the reduction to provide an allylic alcohol from geranylgeraniol. Preferably, the protecting group is a hydroxy protecting group. The hydroxy protecting group is selected such that reduction of the second, third and fourth olefin moieties can be achieved selectively without reducing the first olefin moiety. A variety of hydroxy protecting groups known in the art may be employed. Examples of many of these possible groups can be found in "Protective Groups in Organic Synthesis" by T.W. Green, John Wiley and Sons, 1981, pp. 10-86, which is incorporated herein by reference in its entirety. Preferably, the hydroxy protecting group is an ester. More preferably, the ester is a sterically hindered (i.e., bulky) ester which provides a sufficient protection of C 2 -C 3 olefin moiety from being reduced under the conditions of reducing geranylgeraniol to a protected allylic alcohol. Exemplary bulky ester groups include isobutyrate and pivaloate. Vitamin E is formed from the allylic alcohol and a hydroquinone. Preferably, the hydroquinone is a trimethyl hydroquinone, more preferably, the hydroquinone is 2,3,5- trimethyl hydroquinone. It should be appreciated that a formation of compounds related to vitamin E (i.e., α- tocopherol) can be achieved using a corresponding hydroquinone for a particular tocopherol derivative. For example, β-, γ- , and δ-tocopherol can be synthesized from the allylic alcohol and 2,5-dimethyl hydroquinone, 2,3- dimethyl hydroquinone and 2-methyl hydroquinone, respectively. Without being bound by any theory, it is believed that contacting the allylic alcohol with an acid generates a carbonium ion which reacts with the hydroquinone to form vitamin E. A similar carbonium ion can be generated from a halogen derivative of phytol. For example, contacting a halogenated phytane such as bromo-, chloro- or iodophytane with a Lewis acid such as zinc halide including zinc bromide, zinc chloride and zinc iodide; aluminum halide including aluminum bromide and aluminum chloride; boron halide including boron trichloride and boron trifluoride; silver halide including silver chloride, silver bromide and silver iodide; nickel halide such as nickel chloride and nickel bromide; and other metal halide Lewis acids can generate carbonium ions which can react with a hydroquinone to form vitamin E. Fig. 2 illustrates a particularly preferred embodiment of vitamin E synthesis from geranylgeraniol. The hydroxy group of geranylgeraniol 2-1 is protected as isobutyrate ester or other bulky ester using the corresponding acid or its derivative such as anhydride or acyl chloride. Geranylgeranylisobutyrate 2-2 is then selectively hydrogenated using a metal catalyst such as palladium on carbon to produce phytylisobutyrate 2-3. Hydrogenation of geranylgeranylisobutyrate 2-2 reduces the second, third and fourth olefin moieties without affecting the first olefin moiety. It is believed that the steric bulk of isobutyrate decreases the rate of hydrogenation of the first olefin moiety in protected geranylgeraniol, thus leading to a selective hydrogenation of olefin moieties. The hydroxy protecting group is then removed by hydrolysis under a basic condition to provide phytol 2-4. Reacting phytol 2-4 with 2, 3, 5-trimethyl hydroquinone 2-5 in the presence of an acid then results in a formation of vitamin E 2-6. Alternatively, phytylisobutyrate 2-3 can be deprotected and reacted with 2, 3, 5-trimethyl hydroquinone 2-5 in a single step by an acid catalyst to form vitamin E 2-6. Vitamin E 2-6 can further be transformed to a protected vitamin E such as vitamin E acetate 2-7 by acetylation of the free hydroxy moiety. An alternative method of chemical synthesis converting GG into α-tocopherol or α-tocopheryl esters includes the following steps: (a) selectively oxidizing the 2,3-carbon- carbon double bond in geranylgeraniol 7 to produce geranylgeraniol-2, 3-epoxide 8; (b) hydrogenating the three remaining carbon-carbon double bonds in the epoxide 8 to produce epoxyphytol 9; (c) deoxygenating the epoxyphytol 9 to produce a mixture of phytol 5 and isophytol 6 by reaction with an oxygen acceptor; and (d) reacting the phytol 5 and isophytol 6 mixture with trimethylhydroquinone 4 to produce aipha-tocopherol 3. The step of selectively oxidizing the 2, 3-carbon-carbon double bond in geranylgeraniol to produce geranylgeraniol- 2,3-epoxide is carried out with any reagent known to selectively epoxidize the olefin functionality of allylic alcohols, such as combinations of tert-butyl hydroperoxide and vanadium or molybdenum catalysts as taught by the method of Sharpless and Michaelson, J. Am. Chem. Soc. 95, 6136 (1973) . Hydrogen peroxide or other alkyl hydroperoxides could replace tert-butyl hydroperoxide, and inert solvents such as aromatic hydrocarbons, aliphatic hydrocarbons, cycloaliphatic hydrocarbons or aliphatic esters may be used. The term "aliphatic hydrocarbon" is used to include straight or branched chain alkanes having five to eight carbon atoms. Heptane is the most preferred aliphatic hydrocarbon. The term "cycloaliphatic hydrocarbon" is used to include C 5 - C 8 cycloalkanes and these substituted with one or more τ - C alkyl groups. The term "aromatic hydrocarbon" is used to include benzene and benzene substituted with one to three C τ - C 4 alkyl groups. Toluene is the most preferred aromatic hydrocarbon. The term "aliphatic esters" is used to include aliphatic esters having three to nine carbon having the formula R 1 C0 2 R 2 wherein R x and R 2 independently represent a straight or branched chain C α - C 4 alkyl group, with ethyl acetate being the preferred aliphatic ester. The step of hydrogenating the three remaining carbon- carbon double bonds in the epoxide 8 to produce epoxyphytol 9 can be done with any conventional heterogeneous or homogeneous catalyst under an atmosphere of hydrogen. Thus, supported catalysts such as palladium on carbon, platinum on carbon, platinum oxide, Raney nickel, and the like may be used at a level of about 0.001 to 0.2 parts by weight with respect to 8, with or without an inert solvent such as aliphatic esters, alkanols, aromatic hydrocarbons, aliphatic and cycloaliphatic hydrocarbons or ethers, under a pressure of from about 1 to about 200 atmospheres of hydrogen pressure at temperatures from about 0 degrees C to about 150 degrees C. The term "alkanol" is used to represent alcohols of the formulae R 3 - OH and substituted alcohols of the formula R 3 OCH 2 CH 2 OH, wherein R 3 represents a straight or branched chain C t - C 4 alkyl group. The term "ether" is used to represent ethers having the formula R α - O - R 2 , wherein R l f and R 2 are as defined above and tetrahydrofuran. The step of deoxygenating the epoxyphytol 9 to produce a mixture of phytol 5 and isophytol 6 by reaction with an oxygen acceptor can be a rhenium-catalyzed oxygen transfer reaction and can be done neat or in the presence of an inert solvent such as aromatic hydrocarbons, aliphatic hydrocarbons, cycloaliphatic hydrocarbons, aliphatic esters, alkanols, ethers or water. The reaction can also be carried out in a 2-phase water-organic solvent system with or without the addition of a phase-transfer catalyst. The catalyst can be a substituted rhenium trioxide or a polymer-supported form of such a rhenium trioxide compound. The catalyst can be used at a level of from about 0.01 - 5.0 weight percent based on 9. The oxygen acceptor must be present at a level of 1.0 - 3.0 moles per mole of 9 and may be chosen from triarylphosphines, tri-Cι-C 6 alkylphosphines, triaryl phosphites, tri-C ! -C 18 alkylphosphites, alkali metal hypophosphites or hypophosphoric acid. Other compounds capable of irreversibly accepting oxygen from 9 may be used, such as di-Ci - C 6 alkyl sulfides and certain nitrogen bases such as N - C x - C 6 alkylmorpholines . The term "aryl" is used to include phenyl and naphthyl and these substituted with one to three C α - C 6 alkyl groups. The term "aralkyl" is used to include monovalent radicals having the structure aryl(CH 2 ) n -, wherein n = 1 to 4. The term "substituted rhenium trioxide" is used to include compounds of the formula R - Re0 3 , wherein R is a hydrocarbyl group selected from the group consisting of C t - C 10 alkyl, C 6 - C 10 aryl, aralkyl, cyclopentadienyl and cyclopentadienyl substituted with one to five C τ - C 4 alkyl groups . It should be noted that the step of deoxygenating the epoxyphytol in the present invention, such as by reaction with triphenylphosphine or other suitable oxygen acceptor under catalysis by a rhenium compound such as methylrhenium trioxide, is a novel and unexpected reaction. The use of methylrhenium trioxide as a catalyst in a variety of organic reactions has been reviewed [Schmidt (J. Prakt. Chem. /Chem. -Ztg. 339, 493-496 (1997)]. Espenson and Zhu r (J. Molecular Catalysis A:Chemical 103, 87-94 (1995)] gave six examples of the use of MTO to catalyze the transfer of oxygen from epoxides to triphenylphosphine with the formation of olefins. It is to be noted that all of Espenson and Zhu's examples of olefin generation from epoxides involved simple, non-functional hydrocarbons such as cyclohexene, stilbene, cyclododecene, and so forth. These workers did not demonstrate the feasibility of carrying out such a transformation in a molecule containing additional functionality such as a primary hydroxyl group. In fact, Espenson and Zhu subsequently showed (J. Org. Chem. 61, 324-328 (1996) that MTO catalyses dehydration of primary alcohols with the formation of ethers and olefinic hydrocarbons. Therefore it is unexpected and surprising to discover that MTO/triphenylphosphine, when applied to epoxyphytol, give a good yield of allylic alcohol products such as isophytol and phytol. The step of reacting the phytol 5 and isophytol 6 mixture with trimethylhydroquinone 4 to produce alpha- tocopherol 3 is conducted in the presence of an acid catalyst, often a Lewis acid such as zinc chloride, as is conventionally done in known processes. It has been determined that a mixture of phytol 5 and isophytol 6 can be used to prepare alpha-tocopherol in the same yield as either precursor alone. Specific exemplary compounds of generic terms used herein which are suitable for use in the present invention are as follows. Typical aromatic solvents include benzene, toluene, and o, m or p-xylene or mixtures thereof. Toluene is the preferred aromatic solvent. Typical aliphatic solvents include n-pentane, n-hexane, n-heptane and n- octane and isomers thereof, n-Heptane is the preferred aliphatic hydrocarbon. Typical cycloaliphatic hydrocarbons include cyclopentane, cyclohexane, methylcyclohexane and cycloheptane. Typical aliphatic esters include methyl acetate, ethyl acetate, n-propyl acetate, n-butyl acetate, isopropyl acetate, methyl propionate, ethyl propionate, methyl butyrate and ethyl butyrate. Ethyl acetate is the preferred aliphatic ester. Typical alkanols and substituted alkanols include methanol, ethanol, n-propanol, isopropanol, n-butanol, isobutanol, 2-methoxyethanol, 2- ethoxyethanol and 2-isopropoxyethanol . Typical ethers include diethyl ether, diisopropyl ether, dibutyl ether, n- butyl methyl ether, t-butyl methyl ether and tetrahydrofuran. Typical useful Lewis acids include zinc chloride, aluminum chloride, boron trifluoride, ferric chloride and phosphoric acid. Zinc chloride is the preferred Lewis acid. 5.0 Farnesol to Vitamin E In yet another embodiment of the present invention, a method for producing vitamin E from farnesol is provided. This method generally involves converting farnesol to a first intermediate compound which comprises a sufficient number of carbon atoms to form at least a trimethyltridecyl substituent group of vitamin E when the intermediate is subsequently reacted with an appropriate hydroquinone to form vitamin E. The method further includes reacting the intermediate compound with a hydroquinone to form vitamin E. Preferably, the intermediate compound contains a sufficient number of carbon atoms to form both the methyl and trimethyltridecyl substituents in the 2-position of the chromane ring moiety of vitamin E. More preferably the intermediate compound is selected from the group consisting of phytol and isophytol. The intermediate compound can be prepared by oxidizing farnesol to farnesal. Examples of oxidation of an alcohol to an aldehyde can be found in "Advanced Organic Chemistry Part B Reactions and Synthesis" 2nd Ed., Carey and Sundberg, Plenum Press, 1983, pp. 481-490, which is incorporated herein by reference in its entirety. For example, farnesol can be oxidized to farnesal using manganese dioxide; chromium oxides such as chromium trioxide and dichromates; silver oxide; Swern oxidation conditions; and Oppenauer oxidation conditions. In addition, farnesol can be oxidized via a catalytic air oxidation using a catalyst as disclosed by Marko et al . , Science, 1996, 274, 2044. Generally, this air oxidation of farnesol to farnesal involves using a catalytic amounts of cuprous chloride, 1 , 10-phenanthroline, di-t- butylhydrazodicarboxylate, and excess potassium carbonate in a relatively non-polar solvent such as toluene or benzene at about 80 °C. The method of producing vitamin E from farnesol can further include forming a methyl ketone from farnesal. The methyl ketone can be formed by a variety of methods including aldol condensation with an appropriate ketone such as acetone or its equivalents. For example, aldol condensation of farnesal with acetoacetate followed by a decarboxylation reaction provides the same methyl ketone product as an aldol condensation of farnesal with acetone. The methyl ketone can also be formed using an appropriate Wittig or Horner-Emmons-Wadsworth reagents. Use of these reagents are disclosed, for example, in "Advanced Organic Chemistry", 3rd Ed., J. March, John Wiley & Sons, 1985, pp. 845-854, which is incorporated by reference herein in its entirety. The method of producing vitamin E from farnesol can further include reducing olefin moieties in the methyl ketone to form an alkyl methyl ketone. A reduction of olefin moieties is discussed above in the section regarding production of vitamin E from GG and is incorporated herein by reference. Preferably, the alkyl methyl ketone is 6, 10, 14-trimethyl pentadecan-2-one. The alkyl methyl ketone is then converted to an allylic alcohol. The allylic alcohol can be produced by adding an acetylide such as lithium acetylide, sodium acetylide and magnesium halide acetylide and partially reducing the resulting acetylene group to a vinyl group. Alternatively, the allylic alcohol can be formed directly by other methods well known in the art, such as by reacting the alkyl methyl ketone with a vinyl anion such as vinyl magnesium halide, vinyl lithium or vinyl sodium. Formation of vitamin from an allylic alcohol is discussed above with regard to production of vitamin from geranylgeraniol. A particularly preferred embodiment of synthesizing vitamin E from farnesol is illustrated in Fig. 3. Farnesol 3-8 is oxidized to farnesal 3-9 under Oppenauer oxidation conditions using aluminum isopropoxide and acetone. Farnesal 3-9 is then converted to dehydrofarnesyl acetone 3-10 by an aldol condensation reaction with acetone. Reduction of olefin moieties on dehydrofarnesyl acetone 3- 10 by hydrogenation then produces 6, 10, 14-trimethyl pentadecan-2-one 3-11. Addition of acetylide to the ketone 3-11 then generates propargylic alcohol 3-12 which is partially reduced using Lindlar hydrogenation condition to produce isophytol 3-13. Reaction of isophytol 3-13 with 2, 3, 5-trimethyl hydroquinone 3-5 in the presence of an acid catalyst then produces vitamin E. 6.0 Production of Gamma-tocopherol With reference to Fig. 10, a further embodiment of the present invention is a method for the economical preparation of synthetic gamma-tocopherol. This process includes subjecting a 4-chromanone tocotrienol having the formula of compound 10 to catalytic hydrogenation to reduce the three side-chain double bonds and the 4-keto group to provide gamma-tocopherol 11. The starting compound 10 is known and can be produced as follows. Farnesylacetone 12 and 2, 5-dihydroxy-3, 4-dimethylacetophenone 13 are allowed to react in the presence of a basic catalyst to provide the 4-chromanone tocotrienol compound 10. This reaction is known in the art. The general method was described by Kabbe and Heitzer (Synthesis 1978, 888), and this exact reaction was published by Pearce et al . (J. Med. Chem. 37, 526 (1994) . Furthermore, chromanone 10 was isolated from a natural source and disclosed by Lane et al . in U.S. Patent No. 5,591,772 (1997). In contrast, the step of hydrogenating 4-chromanone tocotrienol is both novel and unexpected. Kabbe and Heitzer (Synthesis 1978, 888) reported that in the alpha-tocopherol series, 4-chromanone was converted to alpha-tocopherol through a three-step sequence. First, the ketone group of 4-chromanone was reduced to an alcohol using sodium borohydride and then water was eliminated to give a tetraene. This compound was then subjected to catalytic hydrogenation to yield alpha-tocopherol. The use of such a multistep sequence involving the expensive reagent sodium borohydride is clearly undesirable, but necessary. It has now been determined that 4-chromanone prepared using the procedure of Kabbe and Heitzer is not converted to alpha-tocopherol by catalytic hydrogenation alone. Attempts to carry out this conversion led instead to formation of a saturated ketone. It was thus not possible to reduce the carbonyl group of the 4-chromanone by catalytic hydrogenation. It is therefore unexpected and surprising that the homologous gamma-series hydrogenation of a ketone 10 to tocopherol 11 can be carried out in excellent yield by means of a simple, inexpensive one-step catalytic hydrogenation over nickel or copper chromite catalysts. Such a method of conversion is much preferable to the multistep process involving a hydride reducing agent as taught by Kabbe and Heitzer. The catalytic hydrogenation of 4-chromanone tocotrienol 10 to gamma-tocopherol 11 can be done using heterogeneous catalysts such as Raney nickel or copper chromite at elevated temperature and hydrogen pressure. Catalysts may be used at a level of about 0.001 to 0.3 parts by weight with respect to the 4-chromanone tocotrienol, with or without an inert solvent such as methanol, ethanol, isopropanol, aliphatic esters, ethers, and the like. The reaction may be carried out at temperatures in the range of about 50°C to about 250°C, and more preferably, in the range of about 135°C to about 175°C. The reaction may be carried out at hydrogen pressures ranging from about 100 psi to about 3000 psi of hydrogen, and preferably ranging from about 400 psi to about 750 psi of hydrogen. The reaction time can vary between about 0.5 to 48 hours. Catalysts other than Raney nickel and copper chromite may be utilized in the process of this invention. Such catalysts may include, but are not limited to, precious metal catalysts such as supported or homogeneous platinum, palladium, rhodium, platinum oxide and their derivatives, and Raney cobalt. 7.0 Biological production of phytol from GGPP or GG. The present invention provides methods for the chemical conversion of GG to phytol or a mixture of phytol and isophytol. Phytol or a phytol plus isophytol mixture can then be reacted with a hydroquinone in the presence of an acid to form vitamin E, as described elsewhere herein. Recently, the gene encoding the enzyme geranylgeranyl reductase was cloned from Arabidopsis thaliana ecotype Columbia [Keller et al., Eur. J. Biochem. 251:413-417 (1998)]. This enzyme catalyzes the stepwise reduction of geranylgeranyl-chlorophyll to phytyl-chlorophyll as well as the reduction of GGPP to phytyl diphosphate. With regard to the present invention, a geranylgeranyl reductase is used in a biological system to substitute for the chemical conversion of GG to phytol. For example, geranylgeranyl reductase is expressed in an erg9 mutant strain of S . cerevisiae that also expresses a GGPP synthase activity. The reductase reacts with GGPP formed in vivo to produce phytyl diphosphate. A phosphatase then converts the phytyl diphosphate to phytol, as occurs in the farnesol- and GG- producing strains described in earlier sections. The resulting microorganism produces phytol directly from a growth substrate such as glucose in a single fermentation. Alternatively, for a geranylgeranyl reductase able to use GG as a substrate, a biological process is provided where GG is produced by fermentation (as described in earlier sections) and purified to the extent necessary to use it as a feedstock for a biotransformation process. The biotransformation uses geranylgeranyl reductase to convert GG to phytol in one step. This biotransformation uses either isolated geranylgeranyl reductase or whole cells containing geranylgeranyl reductase activity. The enzyme or cells are immobilized on a support or by cross-linking to enhance the biotransformation. It is anticipated that geranylgeranyl reductase would be modified by genetic manipulations to enhance its activity for the production of phytol in an industrial biological process. The phytol formed in a biological process using geranylgeranyl reductase is recovered and purified to the extent necessary to allow reaction with a hydroquinone in the presence of an acid to afford vitamin E. The following Examples are provided to illustrate embodiments of the present invention and are not intended to limit the scope of the invention as set forth in the claims . EXAMPLES Example 1 This example describes the creation of erg9 mutants by chemical mutagenesis of S. cerevisiae strain ATCC 28383 using nitrous acid. As noted above, one way of increasing yields of farnesol or GG is to decrease or eliminate squalene synthase activity. In S. cerevisiae, squalene synthase is encoded by the ERG9 gene. A. Mutagenesis Strain 28383 was obtained from the ATCC. It is the parent of strain 60431 used below in some experiments for comparative purposes (also obtained from ATCC) . Strain 60431 is an erg9-l mutant that produces farnesol. A kill curve was performed using nitrous acid with ATCC 28383. Using information derived from the kill curve, a mutagenesis of ATCC 28383 with nitrous acid was performed as follows. The 28383 cells were incubated overnight at 30°C in YPD medium (1% Bacto-yeast extract, 2% Bacto- peptone, and 2% glucose) with shaking. The cells were washed and mutagenized. After mutagenesis, the cells were allowed to recover by culturing them in YPDC (YPD plus 4 mg/L cholesterol) at 22°C overnight. The culture was then washed and plated onto YPDC agar (YPDC plus 2% Bacto-agar) containing various levels of nystatin (20, 30, 40, 50 mg/L) . These cultures were incubated for two weeks at 22°C. The antifungal polyene antibiotic nystatin inhibits cell wall synthesis in growing cells by binding specifically to ergosterol, which, in turn, results in an alteration of selective permeability. Some strains that are resistant to nystatin have been shown to have decreased production of ergosterol. Nystatin has little, if any, affinity for cholesterol which, when supplied exogenously, can be used by sterol auxotrophs as efficiently as ergosterol . Approximately 3,000 nystatin-resistant colonies were obtained. They were screened for temperature sensitivity (ts) and sterol auxotrophy. To determine temperature sensitivity, mutagenized cells were grown on YPDC at a permissive temperature (22°C) and subsequently replica plated to YPD agar and incubated at a restrictive temperature (37°C) . Any cells which fail to grow at the higher temperature would include those with both a conditionally lethal and a constitutively lethal defect in the sterol pathway. Temperature sensitive mutants were screened for sterol auxotrophy by replica plating to YPD agar (lacking cholesterol) and incubation overnight at 28°C. Of the 3,000 nystatin-resistant colonies, 170 were saved after confirmation of ts and sterol auxotrophy. B. Tube Assays The 170 strains were initially evaluated in tube assays for the production of farnesol and other intermediates of the isoprenoid pathway as follows. Cells were cultured in 10 ml YPDC in tubes with screw caps for 48 hours at 28°C with shaking. The cells were centrifuged for 5-10 minutes at 2800 rpm, and the supernatant was transferred to another tube. The cells were washed once with 5 ml distilled water and centrifuged again for 5-10 minutes at 2800 rpm. The cell pellet was extracted by adding 2.5 ml 0.2% pyrogallol (in methanol) and 1.25 ml 60% KOH (in distilled H 2 0) , vortexing to mix, and incubating in a 70-75°C water bath for 1.5 hours. After this saponification, 5 ml hexane were added, and the tube was recapped and vortexed for 15- 30 seconds. The tube was centrifuged at 2800 rpm for 5 minutes to separate the phases. The hexane layer was recovered. If necessary, the sample can be concentrated by evaporating solvent under nitrogen and adding back an appropriate amount of hexane for analysis. To extract the supernatant, 5 ml of hexane were added to the supernatant, and the tube was recapped and vortexed for 15-30 seconds. The tube was centrifuged at 2800 rpm for 25 minutes to separate phases. The hexane layer was recovered, and the sample was concentrated by evaporating under nitrogen and adding back an appropriate amount of hexane for analysis. The hexane extracts from this primary screen were analyzed by thin layer chromatography (TLC) with confirmation by gas chromatography (GC) /mass spectrometry (MS) for the presence of farnesol and other intermediates of the isoprenoid pathway. TLC was performed on reversed- phase C18 silica gel plates using 6:4 (v/v) ethylacetate/acetonitrile (EtOAc/MeCN) as the mobile phase and 2% (w/v) phosphomolybdic acid (PMA) in ethanol for detection. GC/MS was performed using a Hewlett Packard 5890 GC and a 5970 series mass selective detector. The column used was a Restek Rtx-5MS (15 m length, 0.25 mm ID, lμm film system. Thirteen mutants were identified as producers of farnesol or other intermediates. C. Shake Flask Assays These thirteen mutants were then screened in shake flasks, along with the parental strain, 28383, and the farnesol producing strain, 64031. Fifty ml of YPDC medium in 250 ml baffled Erlenmeyer flasks were inoculated with overnight cultures to an initial OD at 600 nm of 0.05 and incubated with shaking at 28°C. The flasks were sampled, and OD at 600 nm, dry weight and sterol content were determined. To measure dry weight, 5 ml of the culture were centrifuged at 8,000 rpm. The cells were washed twice with distilled H 2 0, and the cell pellet was resuspended in 3-5 ml distilled H 2 0 and transferred to a pre-weighed dry weight pan. The pan was placed in 100°C oven for 24 hours, then cooled in a desiccator, weighed on an analytical balance, and the dry weight in g/L determined from the formula: [Total weight (pan + cells) - pan weight] x 200 = dry weight in g/L. For sterol determination, 20 ml of culture were processed, the cell pellet and supernatant extracted, and farnesol and other sterols measured as described above. Seven of the 13 mutants appeared to produce intermediates in the ergosterol pathway and were evaluated further in other shake flask experiments (see below) . All 13 mutants had been selected by resistance to the highest levels of nystatin. Overnight cultures were used to inoculate 50 ml of YPDC medium in triplicate shake flasks for each of the seven mutant strains (MBNA1-1, MBNA1-5, MBNA1-9, MBNA1-10, MBNAl-11, MBNAl-13, MBNAl-14,), the parental strain 28383 and mutant strain 64031. The cells and medium were extracted separately at 24, 48, and 72 hours into hexane, as described above. Dry weight analysis (performed as described above) was performed at each of these time points to determine cell density. The hexane extracts were analyzed by GC/MS for their farnesol, squalene, cholesterol, and ergosterol levels. The farnesol results are presented in Table 3 below. Low levels of farnesol were found in the culture supernatants with much higher levels accumulating in the cells. Strain MBNA1-1 produced 1% farnesol and also made 0.1% ergosterol at 72 hours. Strain MBNA1-5 did not make any farnesol, but produced 0.3% squalene. Strain MBNA1-9 produced 0.64% farnesol in 48 hours. MBNA1-10, MBNAl-11, and MBNAl-14 produced very low levels of farnesol in the cells and appeared to make ergosterol. MBNAl-13 showed the highest farnesol production (2.5%) based on cell dry weight (42,187 ng/ml culture) and did not show any ergosterol production. Thus, among the farnesol-producing strains (MBNA1-1, MBNA1-9 and MBNAl-13), there appeared to be different degrees of blockage in the ergosterol pathway, since MBNA1-1 and MBNA1-9 produced lower levels of farnesol and did not require ergosterol for growth, and MBNAl-13 produced the highest level of farnesol and had a strict requirement for sterol supplementation for growth. The parental strain 28383 showed ergosterol production up to 0.4% (no farnesol production), and erg9 mutant strain 64031 showed farnesol accumulation to approximately 0.4%. TABLE 3 Characterization of New Mutants in Shake Flask Experiment D . Enzyme Analysis For all enzyme assays , cells were grown in YPDE medium . (YPD medium containing 5 mg/L ergosterol ) . The cells were harvested by centrifugation. One gram of cells (wet weight) was suspended in 4 ml of 0.1 M Tris • HCl, pH 7.0. The cell suspension was then disrupted by passage through a French pressure cell (20,000 psi) . The resulting (lysed) cell suspension was then centrifuged (15,000 x g) and the supernatant (cell free extract) was used directly for enzyme assays unless noted otherwise. The mutants were assayed for squalene synthase activity. The squalene synthase assay involved incubation of a cell-free extract with FPP in the presence the reduced form of nicotinamide adenine dinucleotide phosphate, (NADPH) , extraction into ethyl acetate, and squalene detection by GC. Specifically, 0.1 M Tris/HCl pH7 (XμL) , 0.1 M DTT (2μL), 0.1 M MgCl 2 (lOμL), 0.1 M NADPH (4μL), 1 mg/mL FPP (6μL), and cell-free extract (7000 x g supernatant) (YμL) , where X + Y = 178 μL to make 200 μL total, were combined. This mixture was incubated in glass tubes at 37°C for 40 min. Then, it was extracted with 0.15 mL ethyl acetate. The extract was transferred to plastic vials and centrifuged at 15,000 x g for 5 min. The ethyl acetate extract was analyzed using GC/MS. Table 4 shows squalene synthase levels for mutants MBNA1-1, MBNA1-9, MBNAl-13, and ATCC strains 64031 and 28383. Squalene synthase activity was 0.12 μg squalene formed/min x mg protein for the wild-type organism 28383. The activity levels for the other four strains were less than the detectable limits of this assay. Reduced squalene synthase levels would be expected for MBNA1-1, MBNA1-9 and 64031 since they have been characterized as being partially-blocked mutants that produce farnesol and low amounts of ergosterol. MBNAl-13 is a farnesol-producing mutant which cannot grow without added sterol, so this blocked mutant would be expected to have no detectable level of squalene synthase. The extracts of these strains were reassayed with higher concentrations of cell-free extract and longer incubation times. Once again, squalene synthase was not detected in any of the mutants. TABLE 4 ND = Not detected An enzyme analysis was performed for the farnesol- producing strains (MBNA1-1, MBNA1-9 and MBNAl-13) and their parental strain, 28283. The enzyme levels compared were those of the acetoacetyl CoA thiolase, HMG-CoA synthase, HMG-CoA reductase, FPP synthase, and a phosphatase. Cell- free extracts were prepared as described above. For the FPP synthase assay, 0.1 M DTT (2μL) , 0.1 M MgCl 2 (2μL), 1 mg/mL IPP (6 μL) , 1 mg/mL GPP (6 μL) , cell- free extract (Y) , and 0.1 M Tris/HCl (pH 7.0) (X μL) , where X + Y = 84 μL, were combined, and incubated at 37°C for 15 min. This mixture was then extracted twice with 0.3 mL hexane to remove pre-existing farnesol. Next, 0.1 mL of 2 x glycine buffer (0.2 M glycine, 2 mM MgCl 2 , 2mM Zn Cl 2 ) , pH 10.4, and 33 units of alkaline phosphatase were added, and the mixture was incubated at 37°C for an hour. The mixture was extracted with 0.1 mL of ethyl acetate and dried with sodium sulfate. Farnesol was determined with GC. A no-phosphatase control was included in each assay. HMG-CoA reductase catalyzes the reaction of HMG-CoA with NADPH to form mevalonate, nicotinamide adenine dinucleotide phosphate (NADP) and CoA (see Fig. 1) . For these assays, the cell-free extracts were prepared as described above except that the disrupted cell suspensions were centrifuged at 7,000 x g instead of 15,000 x g. The reaction was followed by monitoring consumption of HMG-CoA by high performance liquid chromatography (HPLC) . For the assay, a reaction mixture containing (in a final volume of 0.1 ml) 0.1 M Na 2 H 2 P 2 0 7 , pH 6.5, 2 mM DTT, 1 mM NADPH, 0.4 mM HMG-CoA, and cell-free extract (the volume of extract was varied, with the balance of the 0.1 ml reaction made up with 0.1 M Na 2 H 2 P 2 0 7 , pH 6.5) was incubated at 37°C for 15 minutes. The reaction was monitored with HPLC (Luna C18 (Phenomenex) reversed-phase column using a gradient of 0% Solvent B for 1 min. followed by 0-11 % B over 42 min. Solvent A was 86:14 (v/v) 40mM potassium phosphate (pH 6.0) /methanol. Solvent B was methanol. The wavelength for detection was 260 nm) . HMG-CoA synthase converts acetoacetyl CoA and acetyl CoA to HMG-CoA and CoA. The assay monitors the production of HMG-CoA by HPLC. For the assay, 0.1 M Na 2 H 2 P 2 0 7 , pH 6.5, (X μL) , 20 mM acetoacetyl CoA (4 μL) , 20 mM acetyl CoA (2 μL) , and cell-free extract (Y μL) , where X + Y is 94 μL (total volume 100 μL) , were combined and incubated at 37°C for 5 minutes. Then, the reaction mixture was heated at 60°C for 5 minutes to inactive the enzyme, followed by centrifugation in a microfuge at full speed for 5 minutes. The supernatant was analyzed by HPLC. Acetoactyl CoA thiolase catalyzes a reversible reaction whereby, in the forward direction, two molecules of acetyl CoA are reacted to form acetoacetyl CoA and CoA. The assay monitors the formation of acetyl CoA (reverse reaction) by HPLC. For the assay, 0.1 M Na 2 H 2 P 2 0 7 , pH 6.5, (X μL) , 20 mM acetoacetyl CoA (2 μL) , 20 mM CoA (3 μL) , and cell-free extract (Y μL) , where X + Y is 95 μL (total volume 100 μL) , were combined and incubated at 37°C for 5 minutes. Then, the reaction mixture was centrifuged in a Microcon-10 (Amicon) centrifuge to separate the enzyme from the product. The supernatant was analyzed by HPLC. The phosphatase assay quantitates phosphatase activity by measuring the formation of p-nitrophenol (increased absorbance at 400 nm) . For the phosphatase assay, 0.1 M Tris-HCI, pH 7 (X ul) , 1 M MgCl 2 (2 ul) , 50 mM p-nitrophenyl phosphate (10 ul) and cell-free extract (Y ul) , where X + Y = 1 mL, were combined and incubated at 37°C for 15 minutes, after which the absorbance at 400 nm was measured. Table 5 shows the levels for each of the five enzymes in these four strains. The acetoacetyl CoA thiolase levels were comparable in all of these strains. The HMG-CoA synthase and HMG-CoA reductase levels appeared to be two to three times higher in the mutant strains. The FPP synthase levels were the same or lower in the mutants than in 28383. The phosphatase levels appeared to be elevated three to four fold in the mutant strains compared to the parent . Since all of these strains were isolated by classical mutagenesis, it is possible that other mutations exist in these strains, besides the erg9 mutation. TABLE 5 E. ERG9 Genetic Analysis Chromosomal DNA was prepared from strains ATCC 28383, MBNAl-1, MBNAl-9 and MBNAl-13 according to the method described in Sherman et al . (Sherman, F., G.R. Fink, and J.B. Hicks, 1989, Methods in Yeast Genetics, Cold Spring Harbor Laboratories, Cold Spring Harbor, NY) . The genomic DNA was digested with the restriction enzymes Apal and Nsil , and subjected to Southern blot analysis using a biotinylated ERG9 DNA fragment as a probe. The ERG9 probe consisted of a 2044 bp ERG9 DNA fragment isolated from an agarose gel after digestion of the plasmid pT M103 with Apal and Nsil . pT M103 consists of the ERG9 gene and flanking sequences extending from position #10916 to #13868 of GenBank Accession #U00030 sequence. This plasmid was constructed by polymerase chain reaction (PCR) amplification of the ERG9 gene and flanking regions using the following two oligonucleotides: 5'-oligo = VE107-5 CTC AGT ACG CTG GTA CCC GTC AC (denoted herein as SEQ ID NO:l) 3'-oligo = VE105-3 gat gga TCC CAA TAT GTG TAG CTC AGG (denoted herein as SEQ ID N0:2) Capital letters designate DNA sequences from ERG9 flanking region, while small letters designate bases added to create restriction sites. VE107-5 contains sequences from position #10905 to position #10928 of GenBank Accession #U00030 sequence. VE105-3 contains the reverse complement of sequences from position #13868 to position #13847. The amplification conditions were as follows: Template DNA was genomic DNA isolated from strain S288C (Yeast Genetic Stock Center, Berkeley, CA) 2 min. 94°C/1 cycle 1 min. 94°C, lmin. 52°C, 1.5 min. 74°C/30 cycles 5 min. At 74°C/1 cycle The 2969 bp ERG9 DNA generated from this PCR reaction was digested with Kpnl and BamHl, then ligated to Kpnl , BamHl digested YEp352 to generate plasmid pTWM103. YEp352 is a yeast/E. coli shuttle vector (Hill, J.E., Myers, A.M., Koerner, T.J., and Tzagaloff, A., 1986, Yeast/£. coli Shuttle Vectors with Multiple Unique Restriction Sites, Yeast 2: 163-167) . DNA for the ERG9 probe described above was obtained by digesting TWM103 with Apal and Nsil , and purifying the 2044 bp fragment containing the ERG9 gene and flanking sequences. The ERG9 DΝA was then biotinylated using random primer extension (ΝEBlot Phototope Kit, New England BioLabs, Beverly, MA) . Approximately 1 μg of biotinylated ERG9 probe was hybridized to the Southern blot of Apal, Nsi l digested genomic DNA from strains ATCC 28383, MBNAl-1, MBNAl-9, and MBNAl-13. The blot revealed that all four strains contained a single hybridizing sequence located on a 2044 bp fragment. To clone the ERG9 genes from these four strains, genomic DNA from each was again digested with Apal and Nsil . The yeast/£. coli shuttle vector pRS315 (Sikorski, R.S., and P. Hieter, 1989, A System of Shuttle Vectors and Yeast Host Strains Designed for Efficient Manipulation of DNA in Saccharomyces cerevisiae, Genetics, 122 : 19-27) was digested with Apal and Pstl (Nsil and Pstl have compatible cohesive ends) . The digested DΝAs were separated on an agarose gel, and chromosomal DΝA fragments in the size range from approximately 1.6 kb to approximately 3 kb, as well as the 3895 bp band corresponding to digested pRS316 were cut from the gel and purified using GeneClean (BIO 101, Inc., Visa, CA) . The purified genomic DΝA fragments from each of the four strains was ligated to pRS316, and transformed into E. coli . Transformants containing the pRS316/.ERG9 clones were identified by colony hybridization using the ERG9 probe described above. ERG9 clones derived from each of the four strains were isolated in this manner. The cloned ERG9 genes from each strain were sequenced by ACGT, Inc., Νorthbrook, IL, using an Applied Biosystems, Inc. automated DΝA sequencer, Model ABI 100. The sequence of the ERG9 gene from ATCC 28383 was identical to the sequence deposited in GenBank (Accession #U00030) . The erg9 genes from MBNA1-2 and MBNAl-9 were found to have the same mutation, namely, a change from G to A at position #12386 of GenBank Accession #U00030, which changes a TGG codon to a TGA stop codon. This causes termination of the ERG9 protein at 237 amino acids instead of the normal 444 amino acids found in the wild-type ERG9 protein. The erg9 gene from MBNAl-13 was found to contain a deletion of a C at position #12017 of GenBank Accession #U00030, which causes a frameshift and early termination of the ERG9 protein at 116 amino acids, with the last two amino acids being different from the wild-type ERG9 protein (due to the frameshift) . The erg9 alleles from MBNAl-1 and MBNAl-9 retain low levels of activity. This was determined by transforming an ergosterol-requiring erg9 deletion mutant with plasmids that carry the mutant erg9 genes from MBNAl-1 and MBNAl-9. The presence of the cloned genes in the erg9 deletion strains allowed these transformants to grow, albeit slowly, on medium lacking ergosterol. The erg9 allele from MBNAl-13 did not show any residual activity when tested in this manner. The erg9 deletion strain grew at wild-type levels when transformed with the ERG9 allele from ATCC 28383. F. Description of Secondary Mutations Saccharomyces cerevisiae does not normally import ergosterol from its environment under aerobic conditions. However, the isolated erg9 mutants were able to grow aerobic-ally when supplemented with ergosterol or cholesterol, and therefore, must contain secondary mutations that allow aerobic sterol uptake to occur. The methods used to isolate ergosterol pathway mutants, such as the erg9 mutant MBNAl-13, included not only a selection for ergosterol pathway mutants, but a selection for cells that import sterols under aerobic conditions as well, since only mutants with mutations in both a sterol pathway gene and a sterol uptake gene would have survived. In Example 3 below, the difficulty encountered when attempting to obtain erg9 knockout mutations by molecular methods, even in a strain carrying the upc2 mutation, which is reported to allow uptake of sterols under aerobic conditions (Lewis, T.L., G.A. Keesler, G.P. Fenner and L.W. Parks, 1988, Pleiotropic mutations in Saccharomyces cerevisiae affecting sterol uptake and metabolism, Yeast 4 . : 93-106) is described. It appears that the upc2 mutation does not confer efficient aerobic sterol uptake in an erg9 mutant, and that the strains described in Example 3 acquired additional spontaneous mutations (at a low frequency rate) that improve their ability to take up sterols aerobically. Having the appropriate mutations that enhance aerobic uptake of ergosterol and cholesterol in an otherwise wild type strain allow one to isolate erg9 mutations in that strain at a much higher frequency than would be obtained with a non-sterol uptake mutant strain. In order to demonstrate that the erg9 mutant strain MBNAl-13 (and derivatives of this strain) had acquired a mutation (s) that enhances uptake of sterols under aerobic conditions (referred to as sterol uptake enhancement or sue mutations) , the frequency of creating an erg9 knockout in the MBNAl-13 background, which contains the sterol uptake mutation, to the frequency of obtaining the erg9 knockout mutation in the ATCC 28383 parental background, which presumably lacks the sterol uptake mutation, was compared. This was done with the following two strains representing each strain background. S E23-ΔHE9 ( ura3, his3, sue) was derived from MBNAl-13 and contains a repaired ERG9 gene. S Y5-ΔH1 ( ura3, his3) is an auxotrophic mutant derived from strain ATCC 28383. The construction of S E23-ΔHE9 and SWY5-ΔH1 is described in detail in Section G below. Since S E29-ΔHE9 was derived from MBNAl-13, this strain served as the host carrying the sue mutation, whereas S Y5-ΔH, which was derived from ATCC 28383, served as the host without the sue mutation. Both strains were transformed with equal amounts (approximately 1 μg) of the erg9Δ : :HIS3 DNA fragment obtained by digesting pKML19-41 (plasmid construction described in Example 3) with BamHl and Xmal , and purifying the resulting 2.1 kb fragment. Cells were transformed with this 2.1 kb fragment using the LiAc transformation procedure (Gietz, R.D., R.H. Schiestl, A.R. Willems and R.A. Woods, 1995, Studies on the transformation of intact yeast cells by the LiAc/SS-DNA/PEG procedure, Yeast 1_1: 355-360) , and transformants were selected on SCE- ura medium. SCE medium contains 0.67% Bacto yeast nitrogen base (without amino acids) , 2% dextrose, 20 mg/L adenine sulfate, 20 mg/L uracil, 20 mg/L L-tryptophan, 20 mg/L L- histidine, 20 mg/L L-arginine, 20 mg/L L-methionine, 30 mg/L L-tyrosine, 30 mg/L L-leucine, 30 mg/L L-isoleucine, 30 mg/L L-lysine, 50 mg/L L-phenylalanine, 100 mg/L L- glutamic acid, 100 mg/L L-aspartic acid, 150 mg/L L-valine, 200 mg/L L-threonine, 400 mg/L L-serine and 5 mg/L ergosterol. For agar plates, 2% Bacto agar is added to the SCE medium. SCE-ura medium is SCE lacking uracil. A total of 24 HIS + colonies arose from the transformation of SWY5-ΔH1, while 401 HIS + colonies were obtained from SWE23-ΔHE9. Since it was possible for the erg9Δ : :HIS3 gene to integrate at loci other than the ERG9 locus (and therefore allowing the cells to remain prototrophic for ergosterol) , twenty of each type of transformant were tested for an ergosterol requirement by plating onto YPD medium (lacks ergosterol) . All 20 of the HIS + colonies derived from SWY5-ΔH were able to grow on YPD which indicated that they still contained a functional ERG9 gene, and suggested that the erg9Δ : :HIS3 gene was not integrated at the ERG9 locus. On the other hand, none of the 20 HIS + colonies derived from SWE23-ΔHE9 were able to grow on YPD indicating that the erg9Δ : :HIS3 DNA had replaced the wild type ERG9 gene in this strain background at a relatively high frequency. To verify this, nine HIS + colonies of each strain were analyzed by PCR to determine the types of ERG9 alleles present in their genomes. Genomic DNA was prepared as described in Sherman et al . (1989) . The oligonucleotides used for the analysis are given below. 5' oligo = 250 UpBam gcgcatCCACGGGCTATATAAA (SEQ ID NO: 3) 3' oligo = 1764 LoBam gcggatCCTATTATGTAAGTACTTAG (SEQ ID NO: 4) PCR conditions were as follows: 94°C, 3 min. 94°C, 30 sec; 50°C, 30 sec; 72°C, 3 min.; 30 cycles 72°C, 7 min. Oligonucleotides 250 UpBam contains sequences corresponding to position #11555 to #11570 of the GenBank Accession #J05091 sequence. Oligo 1764LoBam contains the reverse complement of sequences from position #13049 to #13068 of the same GenBank sequence file. In all 9 of the HIS + transformants of SWE23-ΔHE9, the PCR product was 2.1 kbp indicating that the ERG9 gene had been replaced by the erg9Δ : :HIS3 gene. In 8 of the 9 HIS + transformants of SWY5- ΔH1, the PCR products were 2.1 kbp and 1.5 kbp, indicating that the wild type ERG9 gene remained intact and that the erg9Δ : :HIS3 DNA had integrated elsewhere in the genome. The ninth HIS + transformant showed only the 1.4 kbp PCR product, also indicating that the ERG9 gene was intact in this strain. In this case, the HIS3 gene is believed to have integrated into the genome without carrying all of the erg9 sequences with it. These results show that during the course of isolating strain MBNAl-13, an additional mutatio (s), referred to herein as sue, arose in the strain. Based on the results described in Example 3 below, the sue mutation appear to be different from the previously reported upc2 mutation and confers more efficient uptake of sterols. G. Derivation of New Strains from MBNAl-13 In order to use the erg9 mutant strain MBNAl-13 for molecular genetic manipulations, the strain was further developed so that it carried auxotrophic markers suitable for this purpose. MBNAl-13 was mutagenized using ethyl methane sulfonate using standard procedures and mutants resistant to 5-fluoroorotic acid (5-FOA) were obtained by plating the mutagenized cells on medium containing 5-FOA. The use of 5-FOA selection was described in Sikorski and Boeke, 1991 (Sikorski, R.S. and Boeke, J.D., 1991, In Vitro Mutagenesis and Plasmid Shuffling: From Cloned Gene to Mutant Yeast, Methods in Enzymology 194: 302-318). This selection method allowed for the isolation of strains containing mutations in the URA3 gene, coding for orotidine-5'-phosphate decarboxylase. Several resistant strains were isolated that exhibited 5-FOA resistance (i.e., a ura " phenotype) . To determine which of these strains contained a mutation specifically in the URA3 gene, the ura " strains were transformed with pRS316 (Sikorski and Hieter, 1989) , which contains the intact URA3 gene, using the LiOAc transformation procedure (Gietz et al . , 1995). Several strains were identified whose lack of growth on medium lacking uracil was restored by pRS316, indicating that those strains carried the ura3 mutation. One of these strains, EMS9-23 (ura3, erg9) was chosen for further modification. Strain EMS9-23 was genetically altered to contain deletions in leu2 , trpl, or his3 genes using gene transplace ent plasmids described in Sikorski and Hieter 91989) , and the pop-in/pop-out gene replacement procedure described in Rothstein (1991) (Rothstein, R., 1991, Targeting, Disruption, Replacement, and Allele Rescue: Integrative DNA Transformation in Yeast, Methods in Enzymology 194: 281-301). The leu2, trpl and his3 mutants derived from MBNA 1-13 were named SWE23-ΔL1, SWE23-ΔT1 and SWE23-ΔH1, respectively. Strain SWE23-ΔH1 was further manipulated to exchange the original erg9 frameshift mutation (see Section E) with the erg9Δ : :HIS3 allele. This was done by transforming SWE23-ΔH1 (using the LiOAc procedure) with approximately 5 μg of a linear DNA fragment containing the erg9Δ : :HIS3 cassette (the construction of the erg9Δ : :HIS3 cassette is described in detail in Example 3). The erg9Δ : :HIS3 cassette was obtained by digesting pKML19-40 with BamHl and Xmal , and purifying the 2.1 kbp DNA fragment containing the erg9Δ : :HIS3 fragment. Transformants of SWE23-ΔH1 in which the erg9 frameshift allele had been replaced by the erg9Δ : :HIS3 allele were selected by plating the transformants on SCE medium lacking histidine. One of the resulting strains is referred to as SWE23-ΔE91. Strain SWE23-DH1 was further modified so as to contain mutations in the leu2 and trpl genes. These mutations were introduced using the gene transplacement plasmids (Sikorski and Hieter, 1981) and the pop-in/pop-out gene replacement procedure (Rothstein 1991) described above. One of the resulting strains is referred to as SW23-DH1 #42, and contains erg9, ura3, his3, leu2, trpl , and sue mutations. Strain SW23-DH1 #42 was further modified to exchange the original erg9 frameshift mutation with the erg9D: :HIS3 allele. This was done by transforming SW23-DH1 #42 (using the LiOAc procedure) with approximately 5 mg of a linear DNA fragment containing the erg9D: :HIS3 cassette as described above. HIS+ transformants in which the erg9 frameshift mutation had been replaced by the erg9D: :HIS3 allele were selected on SCE-his medium. One of the resulting strains is referred to as SW23B, and carries mutations in the following genes : ura3 , leu2, trpl, his3 , erg 9 : : HI S3 , sue . A summary of the strains derived from MBNAl-13 and their respective farnesol production in shake flask cultures is given in Table 6. The strains were grown overnight in YPDE medium (30°C with shaking at 180 rpm) . These cultures were used to inoculate 25 ml of YPDE medium in a 250 ml flask such that the initial OD 600 was 0.05. The cells were grown for 72 hours at 30°C (with shaking at 180 rpm) . Samples of the whole broth (i.e., cells plus culture medium) were analyzed for dry cell weight and farnesol as described in Section C above. Table 6 Growth and Farnesol Production in Strains Derived from MBNAl-13 Strains MBNAl - 13 , EMS9 - 23 and SWE23 -ΔE91 were further evaluated for growth and farnesol production in 1-L fermentors using the method described in Section H below . EMS9 -23 and SWE23 -ΔE91 were each transformed with plasmid SUBSTΠTITE SHEET (RULE 26) YEp352, which contains the cloned URA3 gene. This obviated the need to add uracil to the fermentation medium for these two strains. Fig. 4 and Table 7 summarize the results of these fermentations. MBNAl-13 and EMS9-23/YEp352 performed similarly. Although the growth of SWE23-ΔE91/YEp352 lagged behind the other two strains, it did reach a cell density and farnesol production level comparable to the other strains . Table 7 Comparison of MBNAl-13 and Strains Derived from it in 1-L Fermentors Strains EMS9-23 and SWE23-ΔH1 were further manipulated by repairing their erg9 mutations back to wild type function. This was done by transforming the two strains (using the LiOAc transformation procedure) with approximately 5 μg of a DNA fragment containing the intact ERG9 gene. The ERG9 gene DNA fragment was obtained by digesting pTWM103 (see Section E above) with Sacl and BamHl, and purifying the 2.5 kb DNA fragment containing the ERG9 gene. Transformants of EMS9-23 and SWE23-ΔH1 in which the erg9 frameshift mutation had been replaced by the wild type ERG9 gene were obtained from each strain by selecting for cells that could grow on YPD medium lacking ergosterol. One erg9-repaired strain derived from EMS9-23, designated SWE23-E9, and one erg9-repaired strain derived from SWE23- ΔH1, designated SWE23-ΔHE9, were chosen for further study. In separate experiments, auxotrophic mutations were introduced into the parental strain ATCC 28383. A spontaneous ura3 mutant of ATCC 28383 was obtained after plating cells on medium containing 5-FOA as described above. Mutants resistant to 5-FOA were transformed with pRS316 (described above) to identify those that had spontaneously acquired a mutation specifically in their URA3 gene. One strain, SWY5 , exhibited a stable ura " phenotype (low reversion frequency) , and was chosen for further study. SWY5 was further manipulated to carry the his3 mutation by using the gene transplacement plasmid YRpl4/his3-Λ200 described by Sikorski and Hieter (Sikorski and Hieter, 1989) and the pop-in/pop-out gene replacement procedure described by Rothstein (Rothstein, 1991) . One his3 mutant derived from SWY5, designated SWY5-ΔH, was chosen for further study. Table 8 lists the repaired and auxotrophic strains described and their genotypes . Table 8 Repaired and Auxotrophic Strains related to ATCC 28383 and MBNAl-13 To test whether the erg9 mutant MBNAl-13 had acquired any additional nutritional requirements during the course of its isolation, a growth experiment was conducted in shake flasks to compare the parental strain ATCC 28383, the erg9 mutant strain EMS9-23 and the erg9-repaired strain SWE23-E9. The cultures were grown in YPD medium at 30°C with shaking at 180 rpm. The EMS9-23 culture was also supplemented with 5 mg/L ergosterol . Growth was monitored by OD 600 . The results of this experiment, presented in Fig. 5, show that the growth of the erg9 mutant was reduced, but that the growth of the wild-type parent strain 28383 and the ergS-repaired strain SWE23-E9 grew similarly. The slightly lower final OD 600 in the SWE23-E9 culture was probably due to the fact that this strain is a uracil auxotroph, and the concentration of uracil in the YPD medium was not optimal. These results indicate that the major cause of the growth defect in the erg9 mutants is the erg9 mutation itself. Other mutations in the erg9 mutants, such as the sue mutation(s), do not have a significant effect on growth. SUBSTITUTESR1ET (RULE 26) H. One-Liter Fermentation Strains MBNAl-13, EMS9-23/YEp352 and SWE23-ΔE91/YEp352 were grown in one-liter fermentors under fed-batch conditions as described below. Under these conditions, farnesol production by these strains ranged from 5.5-6.0% of dry cell weight (data shown in Section G above) in 191- 239 hours. Fermentation Conditions And Materials: The one-liter fementation was performed by first autoclaving for 45 minutes at 121°C, in the fermenter, the following solution: (NH 4 ) 2 S0 4 10.0 g/L KH 2 P0 4 10.0 g/L CaCl 2 -2H 2 0 0.5 g/L NaCI 0.5 g/L MgS0 4 -7H 2 0 3.0 g/L yeast extract (Difco) 2.0 g/L salt solution 20.0 mL defoamer (Dow 1520) 4.0 drops deionized water 500 mL. After autoclaving, the following sterile solutions were added: glucose solution (50%) w/v) 5.0 mL vitamin solution 15.0 mL ergosterol solution 0.2 mL. The glucose and vitamin solutions were sterilized by passage through a 0.45 micron filter. The ergosterol solution is considered sterile (see below) . Glucose feed solution (made up in deionized water) glucose solution (60% w/v) 360 mL yeast extract solution (12.5% w/v) 80 mL ergosterol solution 5.8 mL Glucose, yeast extract sterilized by autoclaving; ergosterol considered sterile. Inoculum 1 mL cell suspension frozen in 10% glycerol inoculated into 250 mL YPDE medium in 1000 mL baffled flask, incubated 48 hours at 29°C and 150 rpm; used 30 mL inoculum per fermenter. Fermentation conditions 28°C pH 4.5 Agitation 300 - 1000 rpm, aeration 50-200 mL/min as required to maintain dissolved oxygen at 10-60% of air saturation. Glucose feed solution added after initial glucose was depleted. Addition rate to achieve a growth rate of 0.04 hr "1 considering that cell yield on glucose is 0.25. Maximum feed rate = 3.5 ml/hr. Salt solution (given per liter in deionized water) FeS0 4 -7H 2 0 0 . 28 g ZnS0 4 -7H 2 0 0 . 29 g CuS0 4 -5H 2 0 0 . 08 g Na 2 Mo0 4 -2H 2 0 0 . 24 g CoCl 2 - 6H 2 0 0 . 24 g MnS0 4 -H 2 0 0 . 17 g HCl 0 . 10 mL Vitamin solution (given per liter in deionized water) biotin 10 mg Ca-pantothenate 120 mg inositol 600 mg pyridoxine-HCl 120 mg thiamine-HCl 120 mg Ergosterol solution ethanol 20 L IGEPAL 20 mL ergosterol 0 . 4 g Heat at 50°C with mixing until dissolved, store at - 20°C. IGEPAL is 1,3,3 tetramethyl butyl phenoxy (ethoxy) 8 ethanol (Sigma Chemical Company, St. Louis, MO, Product IGEPAL CA- 630, Cat. # I 3021) . Example 2 This example describes the production of erg9 mutants by chemical mutagenesis of S. cerevisiae strain 64031 using ethylmethane sulfonate (EMS). Strain 64031 (obtained from ATCC) is an erg9-l mutant that produces low levels of farnesol (see Example 1), and additional mutagenesis produced mutants exhibiting improved yields of farnesol. A kill curve was performed using EMS, and a mutagenesis of 64031 was performed as described in Example 1. Selection was also performed as described in Example 1. A total of 163 strains were found to be nystatin- resistant, ts, sterol auxotrophs. They were cultured in tubes and shake flasks, and farnesol production was determined as described in Example 1. The amounts of farnesol produced in the shake flask cultures are presented in Table 9. TABLE 9 Example 3 In Example l.G. above, the creation of an erg9Δ : HIS3 mutant of MBNAl-13 was described. In this example, the construction of other haploid S. cerevisiae strains (not derived from MBNAl-13) containing an erg9 deletion: : HIS3 insertion allele is described. The ERG9 gene was PCR amplified using genomic DNA isolated from strain S288C (according to the method of Sherman et al . ) as template and the following two primers: 5' oligo = gag cat CCA CGG GCT ATA TAAA (SEQ ID NO:5); 250 BamUp 3' oligo = tec ccc eg GGC GCA GAC TTC ACG CTC (SEQ ID NO: 6) ; 1712 XmaLo The PCR amplified ERG9 DNA was digested with BamHl and Xmal , then ligated to BamHl, Xmal digested pRS316 (Yeast/ E. coli shuttle vector, Sikorski and Hieter, 1989) . The PCR conditions were: 94 °C for 1 min. - 1 cycle 94 °C for 30 sec. j 58 °C for 1 min f 30 cycles 72 °C for 1 min. 72 °C for 2 min.- 1 cycle The ERG9 gene cloned in this manner extends from position #11555 to position #13047 of GenBank Accession #U00030, and the resulting clone was named pJMB98-12. The construction of the deletion in ERG9 and the insertion of HIS3 DNA was done as follows: The HIS3 gene was obtained by digesting the HIS3 containing plasmid pRS403 (Stratagene, LaJolla, CA) with _5co47III and Sspl, and purifying the 1226 bp fragment containing the HIS3 gene. The plasmid pJMB98-12 was digested with Van91I, then treated with T4 DNA polymerase to make it blunt-ended. The plasmid was further digested with Hpal so that an internal 589 bp fragment within ERG9 was deleted. Into this site was ligated the 1226 bp .Eco47III, Sspl fragment containing the HIS3 gene. The resulting plasmid, pKML19-41, has the HIS3 gene cloned within the deleted ERG9 gene, with the HIS3 coding sequence in the same orientation as the ERG9 coding sequence. To transform yeast with this erg9Δ : HIS3 DNA, the plasmid pKML19-41was digested with Smal and Xbal , and the 2141 bp fragment containing the erg9A : HIS3 gene was isolated. DNA was purified from agarose gel slices by using GeneClean. Approximately 5 μg of purified erg9 : : HIS3 DNA was used to transform diploid strain CJ3A X CJ3B (a/ , ura3/ ura3 , his3/his3, leu2/ leu2 , trpl/ trpl , upc2/upc2, obtained from Dr. L. Parks, N.C. State University, Raleigh, NC) using the lithium acetate transformation procedure described in Gietz, et al . (1995). CJ3A X CJ3B is homozygous for the upc2 mutation. This mutation allows sterol uptake under aerobic conditions (Lewis, et al . , 1988) . It was believed that the upc2 mutation would allow the easy production of a haploid strain carrying a mutation in the erg9 gene. The histidine auxotrophy was necessary to select for strains carrying the plasmids that contain the functional HIS3 gene. The transformed cells were plated onto SCE medium (described in Example l.F.) lacking histidine (SC-His) to select for HIS + transformants. Hundreds of transformants were obtained. These HIS + cells were then patched onto SC-His and allowed to grow for two more days. The transformants were then patched onto sporulation medium (Sherman, et. al, 1986). Sporulation medium contains (per liter of distilled water) : 1% potassium acetate, 0.1% Bacto yeast extract, 0.05% dextrose and 2% Bacto agar. The patches were then allowed to grow and sporulate for 3-5 days. A portion of the cells was removed and placed in a solution of lyticase to digest the ascus cell wall. The cells were then spread in a thin line onto a YPD + 2 mg/L ergosterol (YPDE) plate. The sporulated diploid cells form tetrads containing four spores, and the individual spores were separated using a micromanipulator . These individual haploid spores will germinate with each containing a single copy of the chromosomes . A 2:2 segregation was expected for erg9Δ : :HIS3 knockouts in this strain. Two spores should be viable on YPD since they would contain the copy of the chromosome which was not disrupted (meaning they would not need ergosterol since they have a functioning ERG9 gene and would be able to grow on YPD because histidine is present in the medium) . The other two spores should grow on SC-His + 2 mg/L ergosterol (SCE-His) since, if the erg9Δ : :HIS3 DNA integrated at the ERG9 site, the cells would require ergosterol, but would grow without histidine. Tetrads from some of the pKML19-41 transformants were analyzed for phenotypic determination of the erg9 knockout. The results showed that only two of the four spores were viable when grown aerobically. When these were replica- plated to YPD these two spores survived, but they did not survive on SC-His or SCE-His. This indicated a 2:2 segregation and that the two surviving spores were of the parental type or auxotrophic for histidine. This indicated that the two that did not survive aerobically probably contained the erg9 :HIS3 knockout. PCR analysis confirmed the results of an erg9Δ : :HIS3 knockout in several of the strains. Total DNA was isolated using a rapid DNA isolation method from several of the diploid transformants that showed the 2:2 segregation. The total DNA was then used as template for PCR amplification with primers complementing sequence 5' and 3' to the ERG9 gene in the chromosome. The oligonucleotides used for this analysis were as follows: 5 '-oligo = 250 Bam Up (described above) 3 '-oligo = 3ERG9-1 = gat ccg eg GCT CAA GCT AGC GGT ATT ATG CC (SEQ ID NO: 7) 3ERG9-1 contains sequences corresponding to the reverse complement of sequences from position #14812 to position #14790 of the GenBank Accession #U00030 sequence. Oligonucleotide 250 Bam Up lies within the sequence of the ERG9 clone used to construct the erg9Δ : :HIS3 allele, whereas oligonucleotide 3ERG9-1 lies downstream of the boundary of the cloned ERG9 DNA. ERG9 sequences amplified from genomic DNA by these two primers must represent ERG9 genes located at the actual chromosomal ERG9 locus, and will not amplify erg9λ : :HIS3 sequences that integrated at other chromosomal locations. The results showed two bands at 3.271 and 3.908 kb, indicating the presence in the diploid strains of one functional copy of the ERG9 gene and one interrupted copy that is kb 637 bp larger due to the HIS3 gene insertion. Southern blot analysis also was performed to verify the erg9Δ : :HIS3 interruption in the diploids. Genomic DNA from a parental diploid strain carrying two normal copies of ERG9 gene was compared to three different transformants believed to carry one normal ERG9 gene and one disrupted ERG9 gene. The DNA was digested with either Ace I or Xba I, separated by gel electrophoresis, transferred to an Immobilon S membrane, and probed with specific probes to examine the ERG9 genes present. The probe in this case was a 1.4 kb fragment containing a portion of the ERG9 gene. The probe used for Southern blot analysis of genomic DNA was prepared from the PCR amplified ERG9 gene using oligonucleotides 250 Bam Up and 1712 Xma Lo (described above).- Plasmid pJMB98-12 was used as template. PCR conditions were: The amplified ERG9 DNA was purified and biotinylated, as described above. Approximately 1 μg of biotinylated probe was used to hybridize to the blot. Hybridization of the probe to the specific DNA bands under stringent conditions identified complementary sequence being present. For the parental diploid, CJ3AxCJ3B, a single band was seen at 2.1 kb for the Ace I digest and a single band at 2.8 kb was seen with the Xba I digest. The putative erg9Δ : :HIS3 knockouts each contained two bands : bands at 2.1 kb and 1.3 kb for the Ace I digest; and bands at 2.8 kb and 3.4 kb for the Xba I digest. These results indicated the presence of one copy of the wild-type ERG9 gene along with an erg9Δ : :HIS3 disruption in the transformed diploids. Attempts were then made to grow the haploid cells anaerobically on YPDE agar. Strains that are blocked in the ergosterol pathway can take up sterols under anaerobic conditions. Two of the spores grew rapidly under anaerobic conditions (ERG9, his-) and two grew very slowly ( erg9Δ : :HIS3) . The spores of three of the strains erg9Δ : : E1S3 (KML505, KML510, and KML521) that grew anaerobically on plates were grown in liquid medium under anaerobic conditions and showed farnesol production. Upon further incubation of the original YPDE plates aerobically, it appeared that a few of the haploid strains that tested positive for farnesol production under anaerobic growth were growing. Three such viable spores (derived from KML505) arose after prolonged aerobic incubation. These aerobically-growing strains, designated as BKY1-2D, BKY1- 7C, and BKY1-8D, all produced farnesol under aerobic conditions. The parent strain KML510 (a/α, ura3/ura3, his3/his3, trpl /trpl , Ieu2/leu2, upc2/upc2, ERG9/erg9Δ : :HIS3) containing either pJMB98-12 or pRS316 were sporulated and tetrads were dissected onto YPDE plates. The plates were incubated under aerobic conditions, and the following patterns of spore growth were observed. Tetrad analysis of KML510/p MB98-12 were done with 20 tetrads. 16 tetrads gave rise to two viable, fast-growing spores and two nonviable spores. All viable spores were his " , erg + . Three tetrads gave rise to two viable, fast- growing spores, one viable, slow-growing spore, and one non-viable spore. The viable, fast-growing were all his " , erg + . The viable, slow-growing spores were all his + , erg " . One tetrad did not give rise to any viable spores. All of the his + , erg " spores were also ura " , indicating that p MB98- 12 did not segregate into these spores during meiosis. One of the his + , erg " spores was used for further studies, and was named BTY19-9C. Tetrad analysis of KML510/pRS316 was done with 20 tetrads. 18 tetrads gave rise to two viable, fast-growing spores and two non-viable spores. Two tetrads gave rise to two viable, fast-growing spores, one viable, slow-growing spore, and one non-viable spore. All fast-growing spores were his " , erg + . All slow-growing spores were his + , erg " . All his + , erg " spores were also ura " , indicated that pRS316 did not segregate into these spores during meiosis. One of the his + , erg " spores was studied further, and was named BTY20-2A. To confirm that BTY19-9C and BTY20-2A did not carry the wild-type ERG9 gene, a PCR experiment was conducted using genomic DNA isolated from the two strains, and the oligonucleotides VE104-5 and VE105-3. 5 'oligo = VE104-5 = gac tct AGA AGC GGA AAA CGT ATA CAC 3 'oligo = VE105-3 = described above VE104-5 contains sequences corresponding to position #11631 to 116541 of GenBank Accession #U00030 sequence. The predicted PCR product size for a functional ERG9 gene was 2.23 kb, and for the erg9Δ : :HIS3 disruption, 2.87 kb. Strains BTY19-9C and BTY20-2A had a PCR product of approximately 2.87 kb, which indicated the presence of the erg9Δ : :HIS3 disruption. Five strains (BKY1-2D, BKY1-7C, BKY1-8D, BTY19-9C and BTY20-2A) were evaluated for farnesol production in shake flasks. Strains BKY1-7C and BTY20-2A gave the best production of farnesol of the five strains, but BKY1-7C grew very slowly. Transformants KML505, KML510, and KML521 were transferred to sporulation medium. Tetrads were dissected onto YPDE and allowed to grow for extended periods of time under aerobic conditions to look for growth of additional spores beyond the anticipated 2:2 segregation (viable : nonviable ) . Two additional spores were viable after further incubation under aerobic conditions. These two strains, BJY7-5D and BJY8-1A, produced farnesol in a tube screen. Strains BJY7-5D and BJY8-1A were evaluated in shake flasks. BJY8-1A gave the best farnesol production (0.29 mg/ml, 4.7% based on cell dry weight) after 72 hours incubation. BJY7-5D gave 0.18 mg farnesol/ml, (3.5% based on cell dry weight) . Example 4 This example shows the overexpression of HMG CoA reductase in strains with and without a functional ERG9 gene. HMG CoA reductase has been proposed to be the key enzyme regulating the flow of carbon through the isoprenoid pathway. In S. cerevisiae, two genes, HMG1 and HMG2 , code for the two isozymes of HMG CoA reductase, designated HMGlp and HMG2p. Regulation of HMG CoA reductase is achieved through a combination of transcriptional and translational regulation as well as protein degradation. The segments of the HMG1 and HMG2 genes that encode the catalytic domains of the HMGlp and HMG2p isozymes have been cloned under transcriptional control of the strong promoter from the GPD (glyceraldehyde-3-phosphate dehydrogenase) gene. The plasmids containing these constructions (pRH127-3 and pRH124-31, containing the catalytic domains of HMGlp and HMG2p, respectively) were obtained from R. Hampton, U.C. San Diego. Strains of S. cerevisiae overexpressing the catalytic domain of HMGlp were reported to have an elevated flow of carbon through the isoprenoid pathway. This increased carbon flow was manifested as squalene and ergosterol overproduction (Donald, K.A.G., Hampton, R.Y., and Fritz, I.B., 1997, Effects of Overproduction of the Catalytic Domain of 3-Hydroxy-3Methylglutaryl Coenzyme A Reductase on Squalene Synthesis in Saccharomyces cerevisiae . Applied and Environmental Microbiology 63:3341-3344) . A. HMG CoA Reductase Overexpression in Strains with a Functional ERG9 Gene In " order to confirm that overexpressing HMG CoA reductase would result in increased carbon flow through the isoprenoid pathway in the strains derived from ATCC 28383, similar to other strains of S. cerevisiae (Donald, et. al . , 1997), the strain SWY5, a ura3 mutant of the parental strain ATCC 28383, and SWE23-E9, the erg9 repaired version of EMS9-23 (strains described in Example l.G. above), were transformed with plasmids pRH127-3 and pRH124-31. Transformations were performed using the LiOAc procedure (Gietz, et. al . , 1995) . Control strains carrying the empty vector YEp352 were also constructed. Representative transformants were tested for squalene and ergosterol production in a shake flask experiment. Cells were grown in 50 ml SCE-ura medium at 30°C, with shaking at 180 rpm for 48 hours. At 24 hours, 10 ml of the culture was withdrawn, and the cells harvested for HMGCoA reductase assays as described in Example I.D. At the end of the 48- hour growth period, an aliquot of the cultures was used to inoculate flasks containing 50 ml YPD medium such that the starting OD 600 of the cultures was 0.1. The cultures in YPD medium were grown for 72 hours at 30°C, with shaking at 180 rpm, and then analyzed for dry cell weight, squalene and ergosterol accumulation. The extraction method used for this analysis was as follows. Ten ml of the culture was pelleted by centrifugation at 1,500 x g for 10 minutes. The cell pellet was resuspended in 1 ml of deionized water, and the cells were repelleted. Cell pellets were resuspended in 1 ml of deionized water and disrupted by agitation with zirconium silicate beads (0.5 mm diameter). The broken cell suspension was saponified with 2.5 ml of a 0.2% solution of pyrogallol (in methanol) and 1.25 ml of 60% potassium hydroxide solution at 75 degrees C for 1.5 hours. The samples were then extracted with 5 ml of hexane, vortexed for 3 minutes and centrifuged at 1,000 x g for 20 minutes to separate the phases. The hexane layer was then analyzed by GC-MS as described in Example l.B. The data from this experiment are shown in Table 10. Compared to the control strains carrying only the Yep352 vector, the strains that overexpress the catalytic domains of either HMGlp or HMG2p contained high levels of HMGCoA reductase activity and elevated levels of squalene. However, neither of the strains overexpressing HMGlp or HMG2p contained significantly increased levels of ergosterol. Nevertheless, these data show that increasing the activity of HMG CoA reductase in the MBNAl-13 strain lineage increases the carbon flow through the isoprenoid pathway. Table 10. Effect of Amplified HMGCoA Reductase Activity on Squalene and Ergosterol Production in Strains Having a Normal Isoprenoid Pathway B. HMG CoA Reductase Overexpression in an erg9 Mutant Having shown that amplification of HMGlp or HMG2p increased carbon flow to squalene, whether overexpression of HMGl or HMG2 would increase farnesol production in a strain carrying the erg9 mutation was tested. Strain SWE23-ΔE91 (described in Example l.G.) was transformed with plasmids pRH127-3 or pRH124-31. Transformation of SWE23- ΔE91 was accomplished using the LiOAc transformation procedure (Gietz et al, 1996). Approximately 2.5 μg of pRH127-3 or pRH124-31 DNA were used in each transformation. Transformants were selected on SCE-ura plates, and several were chosen and restreaked for purification on SCE-ura plates. To test the effect of amplified HMG CoA reductase on farnesol production, representative transformants were grown for 48 hours in liquid SCE-ura medium. A control strain, SWE23-ΔE91/YEp352, was also included in the experiment. At the end of the 48 hours growth period, aliquots of the cultures were used to inoculate flasks containing 50 ml of YPDE medium such that the initial OD 600 was 0.5. These cultures were grown for 72 hours at 30°C, with shaking at 180 rpm. At the end of the incubation period, samples were analyzed for dry cell weight and farnesol concentration. To confirm that the HMG CoA reductase genes were being overexpressed in the transformants, 20 ml of the cultures grown in SCE-ura were harvested by centrifugation at 1500 x g for 10 minutes, and HMG CoA reductase activity measured using the permeabilized cell method described in Example I.D. The data from this experiment are shown in Table 11. Table 11. Effect of Elevated HMG CoA Reductase Activity on Farnesol Production in an erg9:.-HIS3 Mutant Grown in Shake Flask Cultures. In both S E23-ΔE91/pRH127-3 and S E23-ΔE91/pRH124-31, the levels of HMG CoA reductase activity were elevated. However, the farnesol production in these strains was lower than the control strain SWE23-ΔE91/YEp352. This unexpected result was observed several times in independent experiments . Despite the failure of amplified HMG CoA reductase activity to increase farnesol production in an erg9Δ : :HIS3 strain grown in shake flask cultures, the strains listed in Table 12 were tested for farnesol production in 1-L fermentors using the protocol described in Example l.H. Under these conditions, the expected result was observed; the strains overexpressing HMG CoA reductase produced significantly more farnesol than the control strain. The data are summarized in Figure 6 and Table 12. The elevation of HMG CoA reductase activity in strains SWE23- ΔE91/pRH127-3 and SWE23-ΔE91 /pRH124-31 was confirmed by direct enzyme assay using the permeabilized cell method. This is illustrated by the reductase activities at specific time points during the fermentation (shown in Table 12) . Table 12. Effect of Elevated HMG CoA Reductase Activity on Farnesol Production in Example 5 This example describes the overexpression of various GGPP synthases in erg9 mutants. In order to convert FPP produced in erg9 mutant strains to GGPP (the precursor of desired product, GG) , the genes coding for various GGPP syntheses in erg9 mutants were overexpressed. The genes cloned for this purpose were the BTSl gene from Saccharomyces cerevisiae, the crtE gene from Erwinia uredovora , the al -3 gene from Neurospora crassa , and the ggs gene from Gibberella fujikuroi . Plasmids carrying these genes were constructed as follows. To clone the BTSI1 gene, genomic DNA was prepared from S. cerevisiae strain S288C according to the method described in Sherman, et. al . (1986). The gene was amplified by PCR using the following two oligonucleotides. 5' oligo = VElOO-5 gactctAGAGTTTACGAGTCTGGAAAATC (SEQ ID NO:8) 3 'oligo = VE101-3 gtaggATCCATGGAATTGAGCAATAGAG (SEQ ID NO : 9) The PCR conditions were: 94°C, 3 minutes; 94°C, 1 minute; 52°C, 1 minute; 74°C, 1.5 minutes; 30 cycles; then 74°C, 7 minutes (1 cycle) . The PCR product was digested with Xjbal and BamHl and ligated into Xbal , BamHl digested pPGK315 to generate pTWMlOl. The plasmid pPGK315 contains the S. cerevisiae PGK promoter and terminator separated by a multiple cloning site. Cloning the BTSl gene into pPGK315 as described above placed the BTSl gene under control of the strong PGK promoter. Plasmid pPGK315 was constructed by digesting plasmid pRS315 with SacII and Smal, then treating with T4 DNA polymerase to create blunt ends. The plasmid was religated to generate pRS315-DSS. Plasmid pRS315DSS was then digested with Xhol and ligated with a 994 bp Sail, Xhol fragment obtained from plasmid pPGKMCS that contained the PGK promoter and terminator separated by a multiple cloning site. Plasmid pPGKMCS was constructed by digesting pPGK (Kang et . al . , 1990, Mol. Cell. Biol., 10:2582) with EcoRI and BamHl, then ligating with the following two annealed oligonucleotides. 5' oligo = AATTCCAAGCTTGCGGCCGCTCTAGAACGCGTG (SEQ ID NO: 10) 3 'oligo = GATCCACGCGTTCTAGAGCGGCCGCAAGCTTG (SEQ ID NO: 11) Plasmid pT MllO-11 was constructed by ligating a 2397 bp Kpnl-Sall fragment containing the PGK promoter/BTSl/PGK terminator (obtained by digestion of PTWMllO with Kpnl and Sail) into Xpnl-Sail-digested YEp352. To clone the crtE gene, genomic DNA was isolated from E. uredovora strain 20D3 using the PureGene genomic DNA Isolation Kit (Gentra Systems, Inc., Minneapolis, MN) The crtE gene was amplified using the genomic DNA and the following two oligonucleotides. 5'oligo = 20D3Up gaat t cGTTTATAAGGACAGCCCGA (SEQ ID NO:12) 3 'oligo = 20D3LO ctgcagTCCTTAACTGACGGCAGCGA (SEQ ID NO: 13) Oligo 20D3Up contains sequences corresponding to position #206 to #224 of the Genbank Accession #D90087 sequence. Oligo 20D3Lo contains the reverse complement of sequences from position #1117 to #1136 of the same Genbank sequence file. The amplified DNA was ligated into the Srfl site of pCR-Script SK(+) (Stratagene, La Jolla, CA) to generate plasmid pSWl-B. This plasmid was then digested with BcoRI and Sad, and the 973 bp fragment containing the crtE gene was purified and ligated into .EcoRI-SacI digested pAD314- 956 to generate plasmid pSW2B. Plasmid pSW2-B was digested with BamHl to generate a 2199 bp fragment containing the ADH1 promoter, crtE coding sequence, and ADH1 terminator, and this fragment was ligated into Ba H digested YEp352 to generate pSW4A, which placed the crtE gene in the orientation opposite to that of the URA3 gene in the plasmid, and pSW4B, which placed the crtE gene in the same orientation as the URA3 gene. Plasmid pADH313-956 was generated in the following manner. Plasmid pRS313 (Sikorski and Hieter, 1989) was digested with Sad and Xbal , treated with T4 DNA polymerase to create blunt ends, then relegated to generate plasmid pDSX313. This plasmid was digested with Smal and Apal, treated with T4 DNA polymerase to create blunt ends, and then relegated to generate pDSXSA313. Plasmid pAAH5 (Ammerer, G., 1983, Meth. Enzymol. 101:192-201) , which carries the ADH1 promoter and terminator separated by a Hindll l site, was digested with ifindlll, then ligated to the following two annealed oligonucleotides to introduce a multiple cloning site and create pAAH5-MCS . 5' oligo =MCS1 AGCTGAATTCGAGCTCGGTACCCGGGCTCTAGAGTC GACCTGCAGGCATGCA (SEQ ID NO: 14) 3* oligo = MCS2 AGCTTGCATGCCTCCAGGTCGACTCTAGAGCC CG GGTACCGAGCTCGAATTC (SEQ ID NO:15) A PCR reaction containing pADH313-MCS as template and the following two oligonucleotides was performed, and a 1232 bp PCR product containing the ADH1 promoter, multiple cloning site, and ADH1 terminator was obtained. 5 'oligo = ADH1A gacggatCCGTGGAATATTTCGGATATCC (SEQ ID NO : 16) 3 'oligo = ADH1B ctcggatccGGACGGATTACAACAGGTATTGTCC (SEQ ID NO:17) Oligo ADH1A contains sequences corresponding to position #16 to #37 of the Genbank Accession #V01292 sequence. Oligo ADH1B contains the reverse complement of sequences from position #2092 to #2116 of the same Genbank sequence file. The 1232 bp PCR product was digested with BamHl and ligated into BamHl digested pDSXSA313 to generate plasmid pADH313-956. To clone the N. crassa al -3 gene, genomic DNA was isolated from N. crassa strain ATCC 14692 using the method described by Borges et al. in the methods section of the Fungal Genetics Stock Center's web site (www.kumc.edu/research/fgsc/fgn37/borges.html). The gene was amplified by PCR using the following two oligonucleotides . 5 'oligo = VE118-5 cagaatTCACCATGGCCGTGACTTCCTCCTC (SEQ ID NO: 18) 3 'oligo = VE119-3 caagatctCATACATTCAATCCTCATGGACAC (SEQ ID NO: 19) Oligo VE118-5 contains sequences corresponding to position #1216 to #1240 of the Genbank Accession #U20940 sequence. Oligo VE119-3 contains the reverse complement of sequences from position #2576 to #2599 of the same Genbank sequence file. The amplified DNA was ligated into the Srfl site of pCR-Script SK(+) (Stratagene, La Jolla, CA) to generate pSW7-l and pSW7-2, two independent PCR clones of the al -3 gene. These two plasmids were then digested with EcoRl and Bglll, and the 1393 bp fragment containing the al -3 gene was purified and ligated into EcoRI, BamHl digested pPGK (Kang et. al., 1990) to generate pSW9-l and pSW9-2, with the al-3 sequence in each derived from pSW7-l and pSW7-2, respectively. To clone the ggs gene, genomic DNA was prepared from Gibberella fujikuoi strain ATCC 12617, using the same procedure described above for Neurospora . The ggs gene was amplified by PCR using the following two oligonucleotides. 5 'oligo = VE120-5 gagaattCTTAACACGCATGATCCCCACGGC (SEQ ID NO:20) 3 '-oligo = VE121-3 ctggatcCGTCAAATCCGTGAATCGTAACGAG (SEQ ID NO:21) Oligo VE120-5 contains sequences corresponding to position #607 to #630 of the Genbank Accession #X96943 sequence. Oligo VE121-3 contains the reverse complement of sequences from position #1908 to #1932 of the same Genbank sequence file. The amplified DNA was ligated into the Srfl site of pCR-Script SK(+) to generate pSW8-l and pSW8-2, two independent PCR clones of the ggs gene. These two plasmids were then digested with EcoRI and BamHl, and the 1335 bp fragment containing the ggs gene was purified and ligated into EcoRI, BamHl digested pPGK to generate pSWlO-1 and pSW10-2, with the ggs sequence in each derived from pSW8-l and pSW8-2, respectively. Strain EMS9-23 (ura3, erg9, described in Example l.G.) was transformed with the plasmids described above using the LiOAc method, and transformants were selected on SCE-ura plates. Transformants were picked and restreaked on SCE- ura plates for purification. Representative transformants were tested for GG production. The strains were grown at 30°C for 48 hours in liquid SCE-ura medium, then used to inoculate flasks containing YPDE medium, such that the initial OD 600 was 0.5. These cultures were incubated at 30°C with shaking for 72 hours and analyzed for dry cell weight, farnesol and GG levels. A second set of flasks containing 20 ml of SCE-ura medium was also inoculated from the same starting cultures and was grown for 48 hours. The cells from these flasks were harvested, washed with 10 ml 50 mM BisTris-Propane buffer, pH 7.0, and repelleted. The cell pellets were then used to prepare permeabilized cell suspensions for GGPP synthase assays. The cells were permeabilized by resuspending in 1 ml of 50 mM Bis-Tris- Propane buffer, pH 7.0, containing 0.1% Triton X100, and frozen at 80°C until needed. After thawing, the permeabilized cells were used for GGPP synthase assays. The GGPP synthase assay mixture contained 0.05M Bis-Tris propane buffer, pH 7.0 (Xμl) , 0.1M dithiothreitol (lμl), 1 mg/ml FPP (5 μl) , 1 mg/ml IPP (5 μl) and permeabilized cells (Y μl), where X + Y = 87 μl. A control reaction was included in which the FPP and IPP were omitted. The assay mixtures were incubated at 37 °C for 20 minutes. 0. 1 ml of 2X glycine buffer (0.2M glycine, 2mM MgCl 2 , 2mM ZnCl 2 , pH 10.4) and 63 units of alkaline phosphatase (Sigma Chemical Co., St. Louis, MO) were added, and the mixtures were incubated for 60 minutes at 37 °C. The mixtures were then extracted with 0.2 ml 1:1 hexane: ethyl acetate, and analyzed for GG by GC/MS. GGPP synthase activity is expressed as nmol GGPP formed/min/mg protein. The dry cell weights, farnesol production, GG production and GGPP synthase activities for the strains are summarized in Table 13. The control strain, EMS923/YEp352 , which lacks a cloned GGPP synthase, made 8.7% farnesol (based on dry cell weight) and essentially no GG. The four other strains, each of which overexpressed a different cloned GGPP synthase, produced approximately the same amount of farnesol as the control (8.0 - 9.74%) and produced levels of GG ranging from 0.62 - 1.73%. Table 13. GG Production in Shake Flask Cultures of Strains Overexpressing Four Different Cloned GGPP Synthase Genes. The effect of amplification of GGPP synthase activity on GG production was further evaluated in I-L fermentors. Strain EMS9-23 was transformed with plasmid pTWMIlO-11, carrying the cloned S. cerevisiae BTSl gene. Strain SWE23- ΔE91 (described in Example l.G. above) was transformed with either Yep352 (vector control) or pSW4A-3 (an individual isolate of plasmid pSW4A, carrying the cloned crtE gene) . Strains SWE23-ΔE9l/YEp352 , EMS9-23/pTWM110-ll and SWE23- ΔE91/pSW4A-3 were grown in 1-liter fermentors using the method described in Example I.H., and growth, farnesol production and GG production were compared. The results are shown in Figure 7 and Table 14. The growth .of the three strains was similar. Strain SWE23- ΔE91/YEp352 produced 2.32 g/L farnesol in 236 hours, and did not produce any detectable GG. EMS9-23/pTWM110-ll produced 2.1 g/L farnesol in 239 hours and also produced 0.42 g/L GG in the same time period. Strain SWE23- ΔE9l/pSW4A-3 produced 2.47 g/L farnesol in 236 hours and also produced 0.59 g/L GG in the same period. The GGPP synthase activity in the control strain was below detectable limits. The production of GG by strains EMS9- 23/pTWM110-ll and SWE23-ΔE9l/pSW4A-3 correlated to increased GGPP synthase activity. Table 14. Growth, Farnesol and GG Production in Strains Overexpressing GGPP Synthases and Grown in 1-L Fermentors Example 6 This example illustrates the effect of overexpressing the ERG20 gene which encodes FPP synthase. To determine the effects of elevating FPP synthase levels in erg9 mutants, the ERG20 gene coding for FPP synthase from Saccharomyces cerevisiae was cloned for overexpression. The ERG20 gene was amplified by PCR using genomic DNA from S . cerevisiae strain S288C (prepared according to the method described in Sherman et al . , 1986) . and the following two oligonucleotides. 5' oligo = BamFPPUp ggccggatccATATTACGTAGAAATGGCTTCAG (SEQ ID NO: 22) 3 ' oligo = XhoFPPLo gccgctcgagGGTCCTTATCTAGTTTG (SEQ ID NO: 23) Oligo BamFPPUp contains sequences corresponding to position #790 to #810 of the Genbank Accession # J05091 sequence. Oligo XhoFPPLo contains the reverse complement of sequences from position #1891 to #1907 of the same Genbank sequence file. The PCR product was digested with BamHl and Xhol , and ligated into a vector containing the S. cerevisiae GPD (glyceraldehyde-3-phosphate dehydrogenase) promoter and PGK terminator. The promoter/terminator vector was obtained by digesting a plasmid containing the catalytic domain of the S. cerevi siae HMG2 gene cloned between the GPD promoter and PGK terminator, namely pRH124- 31 (described in Example 4), with BamHl and Sail to remove the HMG2 DNA. The 6.3 kb band corresponding to the promoter/terminator vector was purified and ligated to the 1129 bp fragment containing ERG20 to generate pJMB1931 and pJMB19-32. Plasmids pJMB19-31 and pϋ " MB19-32 were used to transform strain SWE23-ΔE91 (ura3, his3, erg9Δ : :HIS3) using the LiOAc method, and transformants were selected on SCE- ura plates. Transformants were picked and restreaked on SCE-ura plates for purification. To determine the effects of FPP synthase overexpression in erg9 mutant strains, representative transformants constructed as described above were grown in shake flask cultures and compared for growth, farnesol production, GG production and FPP synthase and GGPP synthase activities. The strains were grown with shaking at 30°C for 48 hours in liquid SCE-ura medium, then used to inoculate flasks containing YPDE medium, such that the initial OD 600 was 0.5. These cultures were incubated at 30°C with shaking for an additional 72 hours and analyzed for dry cell weight, farnesol and GG levels. A second set of flasks containing 20 ml of SCE-ura medium was also inoculated from the same starting cultures and was grown for 48 hours. The cells from these flasks were harvested, washed with 10 ml 50 mM BisTris-Propane buffer, pH 7.0, and repelleted. The cell pellets were then used to prepare permeabilized cell suspensions for FPP and GGPP synthase assays. The cells were permeabilized by resuspending in 1 ml of 50 mM Bis-Tris-Propane buffer, pH 7.0, containing 0.1% Triton X100, and frozen at 80°C until needed. After thawing, the permeabilized cells were used for assays. The GGPP synthase assay mixture was the same as described in Example 5. The FPP synthase assay mixture contained 0.05 M Bis-Tris propane buffer, pH 7.0 (X μl) , 0.1M dithiothreitol (1 μl), 0.5M MgCl 2 (2μl) , 1 mg/ml IPP (6 μl), 1 mg/ml geranyldiphosphate (GPP) (6 μl) , and permeabilized cells (Y μl) , where X + Y = 85 μl. A control reaction was included in which the IPP and GPP were omitted. The assay mixtures were incubated at 37 °C for 15 minutes. 0. 1 ml of 2X glycine buffer (0.2M glycine, 2mM MgCl 2 , 2mM ZnCl 2 , pH 10.4) and 63 units of alkaline phosphatase (Sigma Chemical Co., St. Louis, MO) were added, and the mixtures were incubated for 60 minutes at 37 °C. The mixtures were then extracted with 0.2 ml 1:1 hexane: ethyl acetate, and analyzed for Farnesol by GC/MS . FPP synthase activity is expressed as nmol FPP formed/min/mg protein. The data presented in Table 15 show that overexpression of FPP synthase did not increase farnesol production, but did, unexpectedly, increase GG production in these shake flask cultures. The level of GG produced by S E23-ΔE91/pJMB19-31 or SWE23-ΔE91/pJMB19-32 was even higher than observed for the strain (EMS923/pT M110-ll) overexpressing the S. cerevisiae BTSl (GGPP synthase) gene. Table 15. GG production in erg9 mutants overexpressing FPP synthase and GGPP synthase The effect of amplification of FPP synthase activity on GG production was further evaluated in 1-L fermentors. Strains S E23-ΔE91/YEp352 (control), EMS9-23/pS 4A3 ( crtE, GGPP synthase) and S E23-ΔE91/pJMB19-32 (ERG20, FPP synthase) were grown in 1-liter fermentors using the method described in Example I.H., and growth, farnesol production, GG production and GGPP synthase activity were compared (Figure 8 and Table 16) . The growth of the three strains was similar, although S E23-ΔE91/p MB19-32 lagged behind before growing at a rate similar to the other strains. Strain SWE23-ΔE91/YEp352 produced 2.31 g/L farnesol in 258 hours, and did not produce any detectable GG. EMS9- 23/pSW4A3 produced 2.52 g/L farnesol and 0.57 g/L GG in 258 hours. Strain SWE23-ΔE91/pJMB19-32 produced 1.95 g/L farnesol in 258 hours and also produced 0.59 g/L GG in the same period. The unexpected GG production by SWE23- ΔE91/pJMB19-32 correlated to increased GGPP synthase activity in this strain (see below) . No GGPP synthase activity was detected in the control strain S E23-ΔE91 /YEp352. Strain EMS9-23/pSW4A3, expressing the E. uredovora crtE (GGPP synthase) gene showed relatively high GGPP synthase activity (1.7 nmol/min/mg in cells from the 258-hour time point) . As expected, strain SWE23-ΔE91/pJMB19-32, which overexpresses the S. cerevisiae FPP synthase, contained FPP synthase activity that was elevated >10-fold at all time points across the fermentation compared to a control having only normal levels of FPP synthase (data not shown) . Surprisingly, however, strain S E23-ΔE91/pJMB19-32 also had elevated GGPP synthase activity (Table 16) . This activity undoubtedly accounts for the unexpected GG production by this strain. The elevated GGPP synthase activity detected in strain SWE23-ΔE91/pJMB19-32 could be a result of the overexpression of FPP synthase inducing the activity of the GGPP synthase (the BTSl gene product) . It is also possible, however, that the FPP synthase has some low level of GGPP synthase activity which is revealed in this strain because- of the high degree of overproduction of the FPP synthase . Table 16. Effect of Amplified FPP Synthase on Growth, Farnesol and GG Production of Strains Grown in 1-L Fermentors Example 7 This example evaluates several farnesol extraction procedures . In the first experiment, a comparison was made between extraction of the whole broth (cells plus medium) and separate extractions of the cell pellet and medium under various conditions for MBNAl-13 (farnesol producer) and ATCC 28383 (ergosterol producer) (see Example 1) . A 10 ml sample of culture was extracted generally as described in Example 1, but with the changes indicated in Table 17 below. Method 1 in Table 17 is the same as the extraction method described in Example 1. It was found that, for farnesol extraction, a whole broth extraction was just as efficient as a separate cell and medium extraction for methods- 1, 2, 3, 5 and 7. The most farnesol was extracted by method 5, which is just a 2 ml addition of 0.2% pyrogallol in methanol prior to extracting the whole broth into hexane. The second highest extraction was method 1. TABLE 17 Next, experiments were conducted to determine the effects of the type of extraction solvent (method 1, whole broth) , times used for extraction (method 1, hexane extraction, whole broth) , and the amount of methanol added prior to extraction (method 1, hexane extraction, whole broth) . The results are presented in the Tables 17-19 below. Table 17 * Solvent peak coeluted with farnesol, making quantification of farnesol impossible using this method. Table li Table 19 Further work was done to optimize and simplify the extraction procedure for farnesol, and to adapt the procedure for extraction of GG from fermentation broths. This work resulted in the final extraction protocol described below. 1. Whole fermentation broth is used undiluted or diluted appropriately with water to a final volume of 2.0 ml in a 15 ml teflon capped glass test tube. 2. 2.0 ml of hexane is added. 3. 2.0 ml of methanol is added. 4. The tube is vortexed at high speed for 3.5 minutes . 5. The sample is centrifuged at 2,800 rpm in a table top centrifuge for 25-30 minutes to separate the phases . 6. The supernatant (organic phase) is removed and placed in a 2.0 ml teflon capped glass GC/MS vial for determination of farnesol and GG by GC/MS. Example 8 This example illustrates the production of geranylgeraniol-2, 3-epoxide, wherein the epoxidization is conducted in toluene using tert-butylhydroperoxide in the presence of vanadium. A solution of 5.0 grams of geranylgeraniol (0.0172 mole) in 25 ml of toluene was treated with 50 mg of vanadium tris (acetylacetonate) (0.8 mole%) and stirred at reflux under nitrogen. 5.76 ml of 3.3 molar tert- butylhydroperoxide in toluene (0.019 mole) was added dropwise. At the end of the addition, heating was discontinued and the mixture was allowed to cool to room temperature. Analysis by thin layer chromatography disclosed complete conversion of starting material to a single product. The reaction mixture was treated with about 50 ml of about 5% aqueous sodium sulfite solution, stirred 10 minutes and decanted. The organic phase was washed with water, 5% NaHC0 3 , brine, and dried over MgS0 4 . Removal of solvent under reduced pressure afforded 5.28 g (98%) of pale yellow oily product. NMR analysis supported the desired structure of geranylgeraniol-2, 3-epoxide. Example 9 This example illustrates the production of epoxyphytol by hydrogenation of geranylgeraniol-2, 3- epoxide . The total product from Example 6 was dissolved in 50 ml of ethanol, treated with 0.2 gram of 5% palladium on carbon catalyst, and hydrogenated at 1 atm H 2 for 72 hrs. (treatment for about 4 hrs at 40 psi H 2 , 40 deg C is more convenient) . The mixture was filtered (celite) and stripped of solvent to give 5.03 gram (95%) product as a colorless oil, identical by chromatography and NMR spectroscopy with an authentic sample of epoxyphytol prepared by epoxidation of phytol. Example 10 This example illustrates the preparation of a phytol/isophytol mixture from epoxyphytol. A solution of 5.0 grams of epoxyphytol (0.016 mole) from Example 7 and 4.72 grams of triphenylphosphine (0.018 mole) in 50 ml of toluene was treated with 80 mg of methylrhenium trioxide and stirred under reflux for two hours. Thin layer chromatography analysis indicated the absence of starting material and the presence of isophytol, phytol, and a trace of front-running olefins. The mixture was cooled, filtered through a small pad of silica gel to remove catalyst, and stripped of solvent to give 5.0 grams of crude product. Silica gel chromatography afforded 0.4 grams of phytadienes (7.4%) and 3.9 grams (83%) of a 3:1 mixture of isophytol and phytol . Subsequent runs of this experiment were conducted using less catalyst (20-40 mg) and catalyst removal by washing with aqueous sodium carbonate solution (the yellow hydrolysis product Re0 4 " goes into the water layer immediately) . Crude products from this procedure were essentially free of phytadienes (nmr, vpc) . Distillation gave the phytol/isophytol mixture in greater than 90% yield. Example 11 This example illustrates the production of gamma- tocopherol . A solution of 18.9 grams (0.0446 mole) of 4- chromanone tocotrienol 10 in 200 ml of ethyl alcohol was treated with 2 grams (ethanol-wet weight) of Raney nickel catalyst and hydrogenated with agitation at 500 psi of hydrogen and 150 degrees C for 7 hrs. The reaction was cooled, vented, the catalyst filtered off and the filtrate stripped of solvent under vacuum to leave 18.9 grams of a light yellow viscous oily product. Analysis of the product by proton NMR, mass spectroscopy, and IR spectroscopy established that it was gamma-tocopherol; assay by quantitative gas chromatography disclosed a composition of 97.07 wt % gamma-tocopherol, the remainder being ethanol. The yield was 98.9% of theory. Example 12 This example is a comparative example to illustrate that the procedure for preparation of gamma-tocopherol of Example 9 does not work for the preparation of alpha- tocopherol . A solution of 6.2 grams of 4-chromanone 14 in 200 ml of ethanol was treated with 2 grams (wet wt.) of Raney nickel catalyst and hydrogenated at 150°C, 500 psi hydrogen, with agitation for 7 hours. The workup as described in Example 9 gave 6.1 grams of a yellow syrup which was shown by proton NMR analysis to have a structure of a saturated ketone (no olefinic protons observed; protons at position 3, alpha to carbonyl, quartet, j=12 hz, 2.66 ppm) ; IR analysis showed the presence of the carbonyl group (1663 cm -1 ) and the mass spectrum showed m/e 444 (calc. for 11, 444) . Gas chromatographic analysis did not detect the presence of any alpha-tocopherol in the crude product. Example 13 The following example demonstrates the effect of HMG CoA reductase amplification on GG production by a strain over-expressing GGPP synthase. In this experiment, a strain was constructed that contained a single copy of a plasmid integrated into its genome that allows the cells to over-express GGPP synthase. The integrating plasmid is known as pSW35-42, and was constructed as follows. Plasmid pSW4A (see Example 5) was digested with BamHl to generate a 2199 bp fragment containing a fusion of the ADH1 promoter, crtE coding sequence, and ADH1 terminator. This fragment was then ligated into BamHl digested YIp351 (Hill et al, 1986, Yeast/E. coli Shuttle Vectors with Multiple Unique Restriction Sites, YEAST 2:163-167) to generate pSW35-42. To construct a strain containing pSW35-42, this plasmid was digested with the restriction endonuclease BstEII to introduce a single cut within the LEU2 gene. The linearized plasmid was purified and used to transform strain SWE23-DL1 using the LiOAc method. Transformants in which pSW35-42 had integrated at the LEU2 locus were selected on medium lacking leucine. One of the resulting transformed strains is referred to as SWE23-DL1 : :pSW35-42. This strain was then transformed with either YEp352 (an empty vector control, Hill et al, 1986, YEAST 2:163-167) or with pRH124-31 (contains the catalytic domain of the HMG2 gene, see Example 4), which resulted in strains SWE23-DL1: :pSW35-42/YEp352 and SWE23-DL1 : :pSW35-42/pRH124, respectively. Strain SWE23-DL1 : :pSW35-42/YEp352 over-expresses GGPP synthase while SWE23-DL1: :pSW35-42/pRH124 over-expresses GGPP synthase and HMG CoA reductase. Fermentation experiments of strains SWE23-DL1: :pSW35-42/pRH124 and SWE23-DL1 : :pSW35-42/Yep352 were conducted to compare the GG production by these two strains. The strains were tested for GG production in 1-L fermentors using the protocol described in Example l.H. The fermentation data are presented in Table 20. This experiment shows that the fermentation of SWE23-DL1: :pSW35-42/pRH124 accumulated more GG than the fermentation of SWE23-DL1 : :pSW35-42/Yep352, and demonstrates that elevation of HMG CoA reductase activity in a strain designed to produce GG resulted in a further elevation of GG levels as compared to a similar strain with un-amplified HMG CoA reductase. TABLE 20 A second approach to achieve over-expression of HMG CoA reductase and GGPP synthase in the same strain was accomplished by cloning both genes into a high copy-number yeast vector, and transforming this plasmid into an erg9 mutant strain. The plasmid used for this purpose is referred to as pSW46-l, and this was constructed as follows. Plasmid pSW4A (see Example 5) was digested with EcoRI and SacJ and the 0.9 kb fragment containing the crtE gene was purified and ligated into EcoRI, Sacl digested pADH313-956 to generate pSW38-10. Two regions of this plasmid were deleted by digestion with restriction enzymes, filling the ends of the DNA using Pfu polymerase, and ligating to reform the circular plasmid. The regions deleted in this manner were between the NdeJ and SpeJ sites, and between the Hindlll and PstJ sites. The resulting plasmid is referred to as pSW43-5. Plasmid pSW43-5 was digested with BamHl, and the resulting 2199 bp fragment containing the ADH1 promoter, crtE gene, and ADH1 terminator (referred to as the ADHp/crtE/ADHt fragment) was purified and ligated into the BamHl site of YEp352. The resulting plasmid is referred to as pSW44-17, and differs from pSW4A in that it contains one instead of two PstJ sites. Plasmid pRH124-31 was digested with Xbal and PstJ and the 3.2 kB fragment containing the GPD promoter, HMG2 catalytic domain gene, and the PGK terminator (referred to as the GPDp/HMG2cat/PGKt fragment) was cloned into Xbal, Pstl digested pSW44-17 to generate pSW46-l. This plasmid replicates to high copy number in yeast and contains both HMG2 and crtE genes, providing for over-expression of HMG CoA reductase and GGPP synthase. Plasmid pSW46-l was transformed into the erg9 mutant strain SWE-DE91, and URA+ transformants were isolated. Several of the resulting transformants were tested in a shake flask experiment and were compared to a strain that over-expresses only GGPP synthase (EMS9-23/pSW4A) . The results from that experiment are presented in Table 21, and demonstrate that higher levels of GG accumulate in strains that over-express both HMG CoA reductase and GGPP synthase when compared to a strain that over-expresses only GGPP synthase. TABLE 21 These data support the idea that over-expression of HMG CoA reductase in a strain that is capable of producing elevated levels of GG leads to a further increase in the amount of GG produced. Example 14 The following example describes the production of more stable strains that over-exress HMG CoA reductase. As described in Example 4, strains were constructed that over-expressed HMG CoA reductase due to the presence of high-copy number replicating plasmids containing the HMGl cat or HMG2cat genes. Since replicating plasmids can frequently be lost during cell division, this mitotic instablity of the replicating plasmids can lead eventually to cultures with a high proportion of cells containing only normal HMG CoA reductase levels. In order to obtain more stable strains that over-expressed HMG CoA reductase, copies of the gene coding for the catalytic domain of HMG2p were integrated into the genome of strain SW23B. This was accomplished by first constructing a plasmid that allowed for multiple integrations of the HMG2 gene into the spacer region of the rRNA gene. This approach is modeled after the rDNA integration method described by Lopes et al, 1989 (Lopes, T. S., Klootwijk, J., Veenstra, A. E., van der Aar, P. C, van Heerikhuizen, H., Raue, H. A., and Planta, R. J. 1989. High-copy-number integration into the ribosomal DNA of Saccharomyces cerevisiae : a new vector for high-level expression. Gene 79:199-206). PCR was used to amplify two regions of the rDNA locus that lie in the intergenic region between the gene coding for the 35S rRNA and the gene coding for the 5S rDNA, referred to here as the rDNA spacer region. The oligonucleotides used to amplify the first of the two rDNA spacer region fragments contained sequences corresponding to bases # 11161 to #11130 and the reverse complement of #10311 to #10330 of Gene Bank Accession #Z73326. The oligonucleotide sequences are listed below. The lower case letters are used to indicate bases that were altered or added to create restriction endonuclease recognition sites, which are indicated in parentheses following the oligonucleotide sequence. SEQ ID NO:24: R6XbaI Lo 5' -tctagaGGCACCTGTCACTTTGGAAAAAAAATATACGC-3' (Xbal) SEQ ID NO:25: R7SacII Up 5' -ccgcggGCCGGAAATGCTCTCTGTTC-3' (SacII) The DNA fragment generated from PCR amplification using these two oligonucleotides is referred to herein as the R6/R7 fragment. The R6/7 fragment generated by PCR was cloned initially into the plasmid pCR-Script to generate pSW48-l, then cut from this plasmid by digestion with Xbal and SacII. The resulting 759 bp fragment was then cloned into Xbal, SacII digested pBluescript SK- (Stratagene) to generate pSW49-l. The oligonucleotides used to amplify the second rDNA spacer region fragment contained sequences corresponding to bases #11247 to #11272 and the reverse complement of #12054 to #12072 of Gene Bank Accession #Z73326. The sequences of these oligonucleotides are listed below. SEQ ID NO : 26 : R5Sal UpB 5' CACgtCgACCATTCAAACTTTACTAC-3' ( Sail) SEQ ID NO: 27: R4ApaI LoB 5' -GAGGGCccGGTCCAGACAT-3' (ApaJ) The DNA fragment generated from PCR amplification using the two oligonucleotides listed above is referred to herein as the R4/R5 fragment. The R4/R5 fragment generated by PCR was digested with ApaJ and Sail, and ligated into ApaJ, SalJ digested pSW49-l to generate pSW52-ll. PCR was used to amplify the TRP1 gene such that the gene carried an incomplete promoter. The incomplete promoter was intended to reduce expression of the TRP1 gene, and thereby provide a means of selection for high copy number integration of the final expression cassette. The oligonucleotides used to the TRP1 gene contained sequences corresponding to bases #53 to #73 and the reverse complement of #804 to #823 of Gene Bank Accession #J01374. The oligonucleotide sequences are listed below. SEQ ID NO:28: TRP1 SmaUp 5' -cccgggTATTGAGCACGTGAGTATACG-3' (S aJ) SEQ ID NO: 29: TRP1 BamLo 5' -ggatccGGCAAGTGCACAAACAATAC-3' ( BamHl) In the next step, pSW50-l was digested with BamHl and S aJ, and the resulting 779 bp TRP1 fragment was purified. Plasmid pRH124-31 was digested with PstJ and SmaJ to generate a 3261 bp fragment containing the GPD promoter, HMG2 cat gene, and the PGK terminator (referred to as the GPDp/HMG2cat/PGKt fragment) , and this fragment was purified. The TRP1 fragment and the GPDp/HMG2cat/PGKt fragment were ligated into Pstl, BamHl digested pSW52-ll in a three fragment ligation to generate pSW58-77 and pSW58-45. The DNA fragment containing the R6/R1- TRP1-GPD p/HMG2cat /PGK t-R4/R5 gene fusions was cut from pSW58-77 by digestion with the restriction endonucleases Kpnl and SacJ. The 5671 bp fragment corresponding to the integrating construct was purified and used to transform strain SW23B. Transformants were selected on SCE-trp medium. Strains isolated in this manner were screened for elevation of HMG CoA reductase activity and by Southern blot analysis for elevation of HMG2 gene copy number. Strains were identified that carried one copy of the integrating construct, two copies of the integrating construct, three copies of the integrating construct, and eight copies of the integrating construct, and are referred to as SW23B#19, SW23B#31, SW23B#40, and SW23B#74, respectively. Table 22 gives the specific activity of HMG CoA reductase as determined by in vi tro enzyme assays, and copy number of the HMG cat gene as determined by Southern blotting. The HMG CoA reductase assay was previously described (Quain, D. E. and Hasla , J. M. 1979. The Effects of Catabolite Derepression on the Accumulation of Steryl Esters and the Activity of β-Hydroxymethylglutaryl-CoA Reductase in Saccharomyces cerevisiae . J. Gen . Microbiol . 111:343-351) . TABLE 22 These strains require exogenously supplied leucine and uracil for growth due to the leu2 and ura3 mutations in these strains. To eliminate the need to supply these nutrients during fermentation experiments, the strains were transformed with a plasmid, pTWM138, containing functional copies of URA3, LEU2, and TRPl . The presence of this plasmid in these strains allowed the strains to grow without leucine and uracil supplementation. Fermentation experiments were carried out to compare farnesol production by these strains. Also included in this experiment was the strain SWE23-DE91/pRH124-31 which contains the GPDp/HMG2cat /PGKt gene fusion on a high copy number plasmid (see Example 4.B) . The strains were tested for farnesol production in 1-L fermentors using the protocol described in Example l.H, and the data from this experiment are presented in Table 23. TABLE 23 These data support the idea that strains with elevated levels of HMG CoA reductase produce more farnesol than a strain with normal levels of HMG CoA reductase. The data also indicate that a strain containing eight integrated copies of the HMG2cat gene produce essentially as much farnesol as a strain that carries more than 20 extrachromosomal copies of the HMG2cat gene as is the case with strain SW23B/pRH124-31. A strain containing a single integrated copy of the HMG2 cat gene produced more farnesol than the control strain, but slightly less than strains with more copies of the HMG2cat gene. In addition, the strains containing elevated HMG CoA reductase levels accumulated mevalonate in the culture while the strains with normal levels of HMG CoA reductase did not. This suggests that a step downstream of HMG CoA reductase limits carbon flux in the pathway once the HMG CoA reductase enzyme activity has been elevated (see Example 15) . Carbon flux through the pathway is restricted by the activity of one of the enzymes downstream of HMG CoA reductase resulting in mevalonate accumulation in the medium. Example 15 This example shows the effects of over-expression of multiple isoprenoid pathway genes in a strain that has an erg9 mutation and elevated levels of HMG CoA reductase. As shown in Examples 4 and 14, elevation of HMG CoA reductase levels led to higher carbon flux through the isoprenoid/sterol pathway. Over-expression of other isoprenoid pathway genes in strains containing amplified HMG CoA reductase may further increase carbon flux through this pathway. Amplification of isoprenoid pathway genes in strains that have elevated levels of HMG CoA reductase as well as a defective erg9 gene may result in further elevation of farnesol levels. Also, amplification of isoprenoid pathway genes may result in further elevation of GG levels in strains that have a defective erg9 gene and have elevated levels of HMG CoA reductase and GGPP synthase. To test these ideas, plasmids were constructed that allowed for the over-expression of multiple isoprenoid pathway genes. One of the plasmids provided for the over-expression of mevalonate kinase, phosphomevalonate kinase, and diphosphomevalonate decarboxylase, coded by the ERG12, ERG8, and ERG19 genes respectively. This plasmid is referred to as pSW77-69, and was constructed from DNA fragments obtained from a number of plasmids containing single isoprenoid pathway genes. The construction of those plasmids is described first. PCR was used to amplify the ERG12 gene for cloning. The oligonucleotides used to amplify the ERG12 gene contained sequences corresponding to bases #2827 to #2846 and the reverse complement of #5247 to #5229 of Gene Bank Accession #Z49809. The sequences of the two oligonucleotides are given below. The lower case letters are used for bases that were altered or added to create restriction endonuclease recognition sites, which are indicated in parentheses following the oligonucleotide sequence. SEQ ID NO:30: E12.4SN 5'-CCAAATATAACtCGAGCTTTG-3 (Xhol) SEQ ID NO: 31: E12.SALI3 5' -GCAAAGTcCaCCACCGCAG-3 (Sail) The ERG12 gene was amplified using the two oligonucleotides E12.4SN and E12.SALI3 and genomic DNA from strain ATCC 28383. The resulting DNA was cloned into pCR-Script at the Sfrl site to generate pSW68. The oligonucleotides used to amplify the ERG19 gene contained sequences corresponding to bases #911 to #937 of Gene Bank Accession #Z71656 and the reverse complement of bases #1930 to #1962 of Gene Bank Accession #Z71658. The sequences of the two oligonucleotides are given below. SEQ ID NO: 32: E19 SMAI 5'-GCCACGTGCCCcCGGGTTTCTCTAGCC-3' (SmaJ) SEQ ID NO: 33: E19 SACI3 5' -GGAAAAGagCtCGATAATTATTGATGATAGATC-3' (SacJ) The ERG19 gene was amplified using the two oligonucleotides E19 SMAI, E19 SACI3, and genomic DNA from strain ATCC 28383. The resulting DNA was cloned into pCR-Script at the SfrJ site to generate pSW69. The oligonucleotides used to amplify the ERG8 gene contained sequences corresponding to bases #2729 to #2749 and the reverse complement of #5177 to #5196 of Gene Bank Accession #Z49939. The sequences of the two oligonucleotides are given below. SEQ ID NO : 34 : E8.2135N 5'-CCGTTTTGGATccTAGATCAG-3' (BamHl) SEQ ID NO:35: E8SMAI3 5'-gttcccGGGTTATTGTCCTGCATTTG-3' (SmaJ) The ERG8 gene was amplified using the two oligonucleotides E8.2135N, E8SMAI3, and genomic DNA from strain ATCC 28383. The resulting DNA was cloned into pCR-Script at the SfrJ site to generate pSW71. Plasmid pSW71 was digested with BamHl and Smal, and the resulting 2459 bp fragment containing the ERG8 gene was purified. Plasmid pSW69-3 was digested with SmaJ and Sad, and the resulting 2239 bp fragment containing the ERG19 gene was purified. The high , copy number yeast vector YEp352 (containing a URA3 selection marker) was digested with BamHl and SacJ and purified. The three purified DNA fragments were ligated together to generate pSW76-ll. Next, pSW68 was digested with SaiJ and Xhol and the resulting 2400 bp band containing the ERG12 gene was purified and ligated into SaiJ digested pSW76-ll to generate pSW77-69. This plasmid contains ERG12, ERG8, and ERG19, and provides for over-expression of mevalonate kinase, phosphomevalonate kinase, and diphosphomevalonate decarboxylase . Another plasmid provided for the over-expression of mevalonate kinase, phospho- evalonate kinase, diphosphomevalonate decarboxylase, and IPP isomerase, coded by ERG12, ERG8, ERG19, and IDI1 genes respectively. This plasmid is referred to as pSW78-68, and was constructed as follows. The IDI1 gene was amplified by PCR for cloning. The oligonucleotides used to amplify the JDJ1 gene contained sequences corresponding to bases #19577 to #19604 and the reverse complement of #17477 to #17502 of Gene Bank Accession #U43503. The sequences of the two oligonucleotides are given below. SEQ ID NO:36: ISO SACI5 5'-AAGAGctcATCTGATAATAGATCAAGCG-3' (SacJ) SEQ ID NO: 37: ISO SACI3 5'-AGGAGCTCAACGACAATAAATGGCTG-3' (SacJ) The J J1 gene was amplified using the two oligonucleotides ISO SACI5, ISOSACI3, and genomic DNA from strain ATCC 28383. The resulting DNA was cloned into pCR-Script at the SfrJ site to generate pSW73. Plasmid pSW73 was digested with SacJ and the resulting 2117 bp fragment containing the J J1 gene was ligated with SacJ digested pSW77-69 to generate pSW78-68. This plasmid contains ERG12, ERG8, ERG19, and IDI1 , and provides for over-expression of mevalonate kinase, phosphomevalonate kinase, diphosphomevalonate decarboxylase, and IPP isomerase . Another plasmid provided for the over-expression of acetoacetyl CoA thiolase and HMG CoA synthase, coded by the ERG1 0 and ERG13 genes, respectively. This plasmid is referred to as pSW79-29, and was constructed as follows. PCR was used to amplify the ERG13 and ERG1 0 genes for cloning. The oligonucleotides used to amplify the ERG13 gene contained sequences corresponding to the reverse complement of bases #21104 to #21127 and bases #18270 to #18292 of Gene Bank Accession #Z50178. The sequences of the two oligonucleotides are given below. SEQ ID NO: 38: E13 XBAI5 5'-GTCCTctAGATCTTGAATGAAATC-3' { Xbal) SEQ ID NO: 39: E13 SACI3 5'-CTTTGAGCtcGTACAAGAAGCAG-3' (SacJ) The ERG13 gene was amplified using the two oligonucleotides E13 XBAI5, E13 SACI3, and genomic DNA from strain ATCC 28383. The resulting DNA was cloned into pCR-Script at the SfrJ site to generate pSW72. The oligonucleotides used to amplify the ERG1 0 gene contained sequences corresponding to bases #4073 to #4093 and the reverse complement of #6542 to #6565 of Gene Bank Accession #U36624. The sequences of the two oligonucleotides are given below. SEQ ID NO:40: ElO HIND5 5'-CTAAGCttTGCGCCCGTGAAG-3' (Hindlll) SEQ ID NO: 41: ElO XBAI3-2 5' -GTTCTAGAAGTTTTCAAAGCAGAG-3' ( Xbal) . The ERG10 gene was amplified using the two oligonucleotides ElO HIND5, ElO XBAI3-2, and genomic DNA from strain ATCC 28383. The resulting DNA was cloned into pCR-Script at the SfrJ site to generate pS 70. Plasmid pS 70 was digested with Xbal and Hindlll, and the resulting 2482 bp fragment containing the ERG10 gene was purified. Plasmid pS 72-4 was digested with XbaJ and Sad, and the resulting 2850 bp fragment containing the ERG13 gene was purified. The two purified DNA fragments were then ligated together with Sad, Hindlll digested YEp351 (JE!72 selectable marker) to generate pS 79-30. This plasmid contains the ERG13 and ERG10 genes and allows for the over-expression of acetoacetyl CoA thiolase and HMG CoA synthase. Strain S 23B#74 (contains eight integrated copies of the HMG2 cat gene, see Example 14) was transformed with pSW77-69 and pS 78-68, and transformants were selected on SCE-ura medium. The resulting strains are referred to as SW23B#74/pS 77-69 and S 23B#74/pSW78-68, respectively. These strains require added leucine for growth due to the leu2 mutation. To eliminate the need to supplement these strains with leucine during fermentation experiments, they were transformed with a linear fragment of DNA containing a functional LEU2 gene, and LEU+ transformants were isolated. These strains are referred to as S 23B#74L/pS 77-69 and S 23B#74L/pS 78-68, respectively. S 23B#74 was also transformed with pS 79-30, and transformants were selected on SCE-leu medium. S 23B#74/pS 79-30 requires uracil since it contains a mutation in the ura3 gene. To eliminate the need to supplement these strains with uracil during fermentation experiments, this strain was transformed with a linear fragment of DNA containing a functional URA3 gene, and URA+ transformants were isolated. This strain is referred to as S 23B#74U/pSW79-30. SW23B#74 was also transformed with both pS 78-68 and pSW79-30, and transformants were isolated that were capable of growing on SCE-ura, -leu medium indicating that the transformants contained both plasmids. The resulting strain is referred to as S 23B#74/pSW78-68/pSW79-30. Fermentation experiments were carried out with the strains described above to examine the effect of these gene amplifications on farnesol production. The strains were tested in 1-L fermentors using the protocol described in Example l.H, and data from these experiments are presented in Table 24. TABLE 24 These data show that a strain which over-expresses HMG CoA reductase accumulates the isoprenoid pathway intermediate mevalonate in the culture medium. Since mevalonate accumulation is not observed in strains with normal levels of HMG CoA reductase, this demonstrates that carbon flux through the isoprenoid pathway has been increased by HMG CoA reductase amplification to the point where another step subsequent to HMG CoA reductase limits the conversion of pathway intermediates. Furthermore, over-expression of the first three enzymes in the isoprenoid pathway, namely acetoacetyl CoA thiolase, HMG CoA synthase, and HMG CoA reductase (coded by ERG 13 , ERG10 , and HMG2cat, respectively) led to even higher accumulation of mevalonate in the medium. This demonstrates that carbon flux into the isoprenoid pathway has been increased further by amplification of the first three steps, and emphasizes that one of the enzymes downstream of HMG CoA reductase limits conversion of isoprenoid pathway intermediates. Since mevalonate serves as a precursor to farnesol and GG, the modifications described above can be used to increase carbon flux into the isoprenoid pathway, and, if the mevalonate can be more efficiently metabolized, can lead to increased farnesol and GG accumulation. In regard to this last point, enzymes downstream of HMG CoA reductase were amplified in a strain that over- expressed HMG CoA reductase. The enzymes amplified were HMG CoA reductase, mevalonate kinase, phosphomevalonate kinase, diphosphomevalonate decarboxylase, and IPP isomerase (coded by HMG2cat, ERG12, ERG8, ERG19, and JDJ1, respectively) . These strains accumulated less mevalonate when compared to strains over-expressing only HMG CoA reductase, indicating that the increased flux through the isoprenoid pathway resulting from HMG CoA reductase over- expression was accommodated by elevated levels of the downstream enzymes. Although elevated farnesol levels were not observed in the experiment described above, this may be due to the low level of mevalonate available for conversion. However, these data suggest that amplification of one or more of the enzymes downstream of HMG CoA reductase in a strain with amplified levels of the first three pathway enzymes may lead to increased accumulation of farnesol and GG since flux to mevalonate is greatly increased in these strains. It is likely that over- expression of one or more genes downstream of HMG CoA reductase in a strain that over-expresses acetoacetyl CoA thiolase, HMG CoA synthase, and HMG CoA reductase will lead to significant increases in farnesol and GG accumulation. EXAMPLE 16 This example describes an experiment in which squalene synthase is blocked by zaragozic acid in a strain with an intact and functional sterol pathway, including a functional ERG9 gene, and the effect of this squalene synthase inhibitor on farnesol and GG accumulation is observed. Zaragozic acids are a family of compounds that act as potent inhibitors of squalene synthase (Bergstrom, J. D., Dufresne, C, Bills, G. F., Nallin-Omstead, M., and Byrne, K. 1995. Discovery, Biosynthesis, and Mechanism of Action of the Zaragozic Acids: Potent Inhibitors of Squalene Synthase. Ann. Rev. Microbiol. 49:607-639). They are capable of inhibiting cholesterol biosynthesis in mammals and ergosterol biosynthesis in fungi. Since ergosterol is necessary for fungal cell growth, zaragozic acids are potent fungicidal compounds. Strain SWE23-E9 ( ura3, sue; see EXAMPLE l.G) was used in this experiment because it contained the sue mutation that provided for the uptake of sterols under aerobic conditions. This allowed the yeast to grow in ergosterol-supplemented medium when squalene synthase was blocked by zaragozic acid. A strain without the sue mutation would not be able to take up sterols, including ergosterol, from the medium, and therefore could not grow in the presence of zaragozic acid. S E23-E9 containing either an empty vector (Yep352) or plasmids that allow for the over-expression of HMG Co A reductase (pRH124-31), GGPP synthase (pS 4A) , or both HMG Co A reductase and GGPP synthase (pS 46-l) were tested in shake flasks by first growing the strains in SCE-ura medium for 48 hr to select for the plasmids. Samples of these cultures were then inoculated into YPDE medium or YPDE medium containing zaragozic acid at 100 μg/ml. The YPDE (+/- zaragozic acid) cultures were incubated at 30°C for 48 hr, then analyzed for dry cell weight and farnesol accumulation. The data from this experiment are shown in Table 25. All of the cultures treated with zaragozic acid exhibited elevated accumulation of farnesol relative to the untreated cultures. GG accumulation was not measured in this experiment. TABLE 25 In a separate experiment, S E23-E9 containing either an empty vector (Yep352) or a plasmid that allows for over-expression of both HMG Co A reductase and GGPP synthase (pS 46-l) were tested in shake flasks by first growing the strains in SCE-ura medium for 48 hr to select for the plasmids. Samples of these cultures were then inoculated into YPDE medium or YPDE medium containing zaragozic acid at 100 mg/ml. The YPDE (+/- zaragozic acid) cultures were incubated at 30°C for 72 hr, then analyzed for dry cell weight and GG. The data are presented in Table 26. The culture of S E23-E9/pSW46-l treated with zaragozic acid exhibited a higher level of GG as compared to the same strain grown in the absence of zaragozic acid. These experiments demonstrate that strains without mutations in the sterol biosynthetic pathway can be induced to accumulate farnesol by blocking the pathway using a squalene synthase inhibitor. The amount of farnesol or GG accumulated by the zaragozic acid treated cultures was much less than the amount accumulated by strains with completely defective erg9 genes indicating that a genetic block of squalene synthase is more effective than a block induced by a squalene synthase inhibitor. TABLE 26 Example 17 An alternative pathway leading to FPP has been described in a number of bacteria and plants, and is referred to as the non-mevalonate or Rohmer pathway (Eisenreich, W., Schwarz, M., Cartayrade, A., Arigoni, D., Zenk, M. H., and Bacher, A., 1998. The Deoxyxylulose Phosphate Pathway of Terpenoid Biosynthesis in Plants and Microorganisms. Chem. Biol. 5: R221-233. Paseshnichenko, V. A., 1998. A New Alternative Non-Mevalonate Pathway for isoprenoid Biosynthesis in Eubacteria and Plants. Biochemistry (Mosc) 63:139-148). Some of the enzymes of the non-mevalonate pathway and their genes have been identified and studied in E. coli , and these include the deoxyxylulose-5-phosphate synthase, deoxyxylulose-5- phosphate reductase, IPP isomerase, and FPP synthase, coded by the dxr, dxs, idi, and ispA genes, respectively. In order to construct strains of E. coli that accumulate elevated levels of farnesol, plasmids were constructed for the over-expression in E. coli of the genes listed above. In some cases, additional genes adjacent to the known isoprenoid pathway gene were included in the cloned DNA. The idi gene coding for IPP isomerase was PCR amplified using the two oligonucleotides listed below and genomic DNA isolated from E. coli strain 3110. The oligonucleotides used to amplify the idi gene contained sequences corresponding to bases #42309 to #42335 and the reverse complement of #43699 to #43726 of Gene Bank Accession #U28375. The lower case letters are used for bases that were altered to create restriction endonuclease recognition sites, which are indicated in parentheses following the oligonucleotide sequence. A natural EcoRI site was used in VE145-5. SEQ ID NO: 42: VE145-5 5'-GGGATTCGAATTCTGTCGCGCTGTAAC-3' (EcoRI) SEQ ID NO: 43: VE146-3 5'-TGggATCcGTAACGGCTTTAGCGAGCTG-3' (BamHl) The idi PCR product was digested with EcoRI and BamHl, and ligated into EcoRI, BamHl digested pUC19. The resulting clone is referred to as pHS-0182. The dxr gene was PCR amplified using the two oligonucleotides listed below and genomic DNA isolated from E. coli strain W3110. The oligonucleotides used to amplify a region of DNA which included the frr, dxr, and yaeS genes contained sequences corresponding to bases #2131 to #2150 and the reverse complement of #5297 to #5315 of Gene Bank Accession #D83536. SEQ ID NO: 44: DXR17.SN GATTCCGCGTAAGgATCcCG (BamHl) SEQ ID NO: 45: DXR3179.ASN CCAGCATctAGACCACCAG {Xbal) The resulting PCR product was digested with BamHl and XjbaJ, and ligated into BamHl, Xbal digested pHS-0182 to generate pHS-0182R. The ispA and dxs genes appear to be part of an operon that possibly include two other genes referred to as xseB and yajO. PCR was used to amplify a region of DNA which included xseB, ispA, dxs, and yaj ' O using the oligonucleotides listed below and genomic DNA isolated from E. coli strain 3110. The oligonucleotides contained sequences corresponding to bases #4157 to #4183 and the reverse complement of bases # 8938 to #48956 of Gene Bank Accession #AE000148. SEQ ID NO: 46: DXS.5619P 5'-gactgcagCTGGCCGCTGGGTATTCTGTCGTAGTT-3' (PstJ) SEQ ID NO: 47: DXS .82OX 5' -gatctagaTCACGCGTACGCAGAAGGTTTTGC-3' (XbaJ) The resulting PCR product was digested with XbaJ and PstJ and ligated to Xbal, Pstl digested pUC19 to generate pHS-dxs. The DNA fragment containing the dxs gene will be cut from pHS-dxs using XbaJ and Pstl, and ligated into Xbal, PstJ digested pHS-0182R to generate a plasmid that contains dxs, dxr, ispA, and idi . The resulting plasmid will be transformed into E. coli , and a transformed strain containing the plasmid will be tested for production of farnesol in shake flask and fermentation experiments. In order to construct strains of E. coli that accumulate elevated levels of GG, a plasmid was constructed for the over-expression in E. coli of GGPP synthase from Erwinia herbicola . The crtE gene coding for GGPP synthase was amplified by PCR using genomic DNA isolated from Erwinia herbicola strain EholO and the following two oligonucleotides. The oligonucleotides contained sequences corresponding to bases #3513 to #3531 and the reverse complement of bases # 4459 to #4481 of Gene Bank Accession #M87280. SEQ ID NO: 48: EholOE Up 5'-gaattcCAATTCAGCGGGTAACCTT-3' (Eco-RJ) SEQ ID NO: 49: EholOE Lo 5'-aagcttTGCTTGAACCCAAAAGGGCGGTA-3' (TJindJJJ) The resulting PCR product was digested with EcoRI and Hindlll, and ligated into pET24d(+) (Novagen) so that expression of the ctrE gene was controlled by the T7 promoter. The resulting plasmid is referred to as pKL19- 63. This plasmid can be transformed into E. coli strains such as BL21(DE3) (available from Novagen) which contains an IPTG inducible gene coding for T7 polymerase. This allows IPTG induction of the crtE gene in this strain. The T7 promoter/ crtE gene fusion can be cut from pKL19-63 using Bglll and Hindlll, and ligated into BamHl, Hindlll digested PACYC184 (Accession #X06403) to construct a plasmid relying on chloramphenicol resistance for selection. This plasmid contains the pl5A origin of replication and would be compatible with plasmids containing the ColEl origin of replication such as the clones carrying the E. coli isoprenoid pathway genes described above. These latter plasmids confer ampicillin resistance, and so E. coli transformants can be obtained that carry both the crtE plasmid and the plasmid containing the dxs, dxr, idi, and ispA genes by transforming E. coii with both plasmids and selecting for resistance to chloramphenicol and ampicillin. Therefore, strains of E. coJi BL21(DE3) will be obtained that contain plasmids for over-expression deoxyxylulose-5- phosphate synthase, deoxyxylulose-5-phosphate reductoisomerase, IPP isomerase, FPP synthase, and GGPP synthase. These strains will be tested for production of GG in shake flask and fermentation experiments. Example 18 The following example describes the construction of strains of Saccharomyces cerevisiae that are engineered to produce elevated levels of farnesol and GG by expressing enzymes corresponding to the non-mevalonate pathway enzymes . Biosynthesis of IPP occurs in many bacteria and plants starting from pyruvate and glyceraldehyde-3-and proceeding through a series of enzymatic steps known as the non- mevalonate pathway, and includes the enzymes deoxyxylulose- 5-phosphate synthase and deoxyxylulose-5-phosphate reductoisomerase. The compound resulting from these two enzymatic steps is 2-C-methyl-D-erythritol 4-phosphate (also known as MEP) , which is further metabolized by unknown enzymes to yield IPP. Plasmids are constructed that express the E. coli dxs and dxr genes in yeast by fusing the coding regions of those genes to promoter elements that allow for expression in yeast. The dxs and dxs genes are amplified by PCR with oligonucleotides that include restriction sites to allow cloning into yeast expression vectors which contain promters such as the ADH1 promoter, PGK promoter, or GPD promoter. The two gene fusions are then combined into a single plasmid by subcloning one gene fusion into the other plasmid. The resulting plasmid containing both genes is then transformed into an erg9 mutant of yeast. The resulting strain is capable of synthesizing MEP, which may be further metabolized to IPP by endogenous enzymes capable of carrying out the desired reactions to IPP. This capability may lead to increased accumulation of IPP, which may cause the cells to accumulate elevated levels of farnesol through the action of the endogenous IPP isomerase and FPP synthase enzymes. If this is done in a strain that also over- expresses GGPP synthase, then elevated levels of GG may accumulate in these strains. Example 19 This example describes the construction of a strain of Saccharomyces cerevisiae that over-expresses a mutated ERG20 gene coding for an FPP synthase enzyme exhibiting altered product specificity. Unlike strains over-expressing wild-type FPP synthase, strains expressing the mutated FPP synthase accumulated more GG than farnesol. Comparison of the amino acid sequences of FPP synthases from a variety of organisms revealed several highly conserved domains including two aspartate rich domains, which are essential for catalytic activity. Researchers have reported that mutations effecting the amino acid located at the fifth position before the first aspartate rich domain can alter the product specificity of the enzyme such that the enzyme readily catalyzes the formation of GGPP as well as FPP. This has been shown for both avian and Bacill us stearothermophilus FPP synthases (Tarshis, L.C., Proteau, P. J., Kellogg, B. A., Sacchettini, J. C, Poulter, C. D. 1996. Regulation of Product Chain Length by Isoprenyl Diphosphate Synthases. Proc. Natl. Acad. Sci. USA 93:15018-15023; Ohnuma, S., Narita, K., Nakazawa, T., Ishida, C, Takeuchi, Y., Onto, C, and Nichino, T. 1996. A Role of the Amino Acid Residue Located on the Fifth Position Before the First Aspartate- rich Motif of Farnesyl Diphosphate Synthase on Determination of the Final Product. J. Biol. Chem. 271:30748-30754; U.S. Patent 5,766,911). In the case of the Bacillus enzyme, the amino acid in the fifth position before the first aspartate rich domain was changed from tyrosine to serine. The avian enzyme contains a phenylalanme in this position. It is thought that aromatic amino acids in that position block extension of the isoprenyl chain beyond fifteen carbons, and that the restriction can be alleviated by replacing the phenylalanme with a less-bulky amino acid such as serine. As in the Bacillus FPP synthases mentioned above, the FPP synthase from Saccharomyces cerevisiae has a tyrosine at the fifth position before the first aspartate rich domain. Site directed mutagenesis was used to alter the sequence of the ERG20 gene to code for a serine instead of a tyrosine at that position. The method used to introduce the mutation relied on PCR amplification of the entire pJMB19-31 plasmid using mutagenic oligonucleotides that introduced the desired mutation, and is outlined in the instruction booklet for the QuikChange Site-Directed Mutagenesis Kit (Stratagene) . The oligonucleotides contained sequences corresponding to bases #1063 to #1097 and the reverse complement of bases # 1063 to #1097 of Gene Bank Accession #J05091. The sequences of the oligonucleotides are given below, with the changes indicated by small case letters. An alteration of A to T was made at position #1084 to change the encoded amino acid from tyrosine to serine. Also, an alteration of T to C was made at position #1074 to create a new PstJ site, which allowed for rapid identification of the mutant gene. This latter mutation was silent in that it did not change the encoded amino acid. SEQ ID NO : 50 : Y95S-SN 5' -GCATTGAGTTGcTGCAGGCTTcCTTCTTGGTCGCC-3' SEQ ID NO: 51: Y95S-ASN 5' -GGCGACCAAGAAGgAAGCCTGCAgCAACTCAATGC-3' The two oligonucleotides were used to amplify pJMB19- 31, and the resulting PCR product was ligated to itself to reform the circular plasmid, except that ERG20 gene now contained the desired mutation. The resulting plasmid is referred to as pHS31.Y95S, and this plasmid was transformed into the erg9 mutant strain SWE23-DE91 to form SWE23- DE91/pHS31.Y95S. Shake flask experiments were carried out to compare farnesol and GG production by strains over- expressing the wild-type ERG20 gene and the mutated ERG20 gene. Strains were grown overnight in SCE-ura, and this was used to inoculate flasks containing YPDE medium. These cultures were grown at 30°C for 72 hr, then harvested for dry cell weight and isoprenoid analysis. The data from this experiment is presented in Table 27. TABLE 27 These data show that the farnesol :GG ratio is dramatically altered by over-expression of the tyr to ser mutant of the ERG20 gene in an erg9 mutant strain. The strain over-expressing the mutant ERG20 gene exhibited proportionally more GG than the strain over-expressing the wild-type ERG20 gene. In addition, the total amount of GG produced by the strain over-expressing the mutant ERG20 was higher while the total amount of farnesol was lower as compared to the strain over-expressing the wild-type ERG20 gene. The decrease in farnesol level was not completely reflected in the GG pool, suggesting that some of the FPP may be converted to other compounds besides GG. Alternatively, it is possible that feedback inhibition plays a role in regulating the amount of GG accumulated by these strains. The foregoing description of the invention has been presented for purposes of illustration and description. Furthermore, the description is not intended to limit the invention to the form disclosed herein. Consequently, variations and modifications commensurate with the above teachings, and the skill or knowledge of the relevant art, are within the scope of the present invention. The embodiments described hereinabove are further intended to explain best modes known of practicing the invention and to enable others skilled in the art to utilize the invention in such, or other, embodiments and with the various modifications required by the particular applications or uses of the invention. It is intended that the appended claims be construed to include alternative embodiments to the extent permitted by the prior art.

Claims: What is claimed is: 1. A method for producing α-tocopherol or α- tocopheryl esters comprising: (a) biologically producing geranylgeraniol; and (b) chemically converting said geranylgeraniol into α-tocopherol or an α-tocopheryl ester by a process comprising: (i) selectively oxidizing the 2, 3-carbon-carbon double bond in geranylgeraniol to produce geranylgeraniol-2, 3-epoxide; (ii) hydrogenating the three remaining carbon-carbon double bonds in said epoxide to produce epoxyphytol; (iii) deoxygenating said epoxyphytol to produce a mixture of phytol and isophytol by reaction with an oxygen acceptor; and (iv) reacting said phytol and isophytol mixture with trimethylhydroquinone to produce α-tocopherol. 2. A method, as claimed in Claim 1, wherein said step of selectively oxidizing is carried out in an inert solvent using t-butyl hydroperoxide in the presence of vanadium or molybdenum as the oxidant. 3. A method, as claimed in Claim 2, wherein said inert solvent is selected from the group consisting of aromatic hydrocarbons, aliphatic hydrocarbons, cycloaliphatic hydrocarbons and aliphatic esters or mixtures thereof. 4. A method, as claimed in Claim 1, wherein said step of hydrogenating is conducted in an inert solvent in the presence of a catalyst selected from the group consisting of Raney nickel, palladium on carbon and platinum on carbon. 5. A method, as claimed in Claim 4, wherein said inert solvent is selected from the group consisting of aliphatic esters, alkanols, aromatic hydrocarbons, aliphatic hydrocarbons and ethers, or mixtures, and wherein said step of hydrogenating is conducted under a pressure of from about 1 atmosphere to about 200 atmospheres at temperatures between about 0°C and about 150°C. 6. A method, as claimed in Claim 4, wherein said catalyst is present at a level of about 0.001 to about 0.5 weight percent based on the starting weight of geranylgeraniol - 2, 3-epoxide. 7. A method, as claimed in Claim 1, wherein said step of deoxygenating is conducted in the presence of a substituted rhenium trioxide catalyst. 8. A method, as claimed in Claim 1, wherein said step of deoxygenating is conducted in an inert solvent using an oxygen acceptor selected from the group consisting of triarylphosphines, tri-C x - C 18 alkylphosphines, triaryl phosphites, tri-Ci - C 18 alkylphosphites, alkali metal hypophosphites, hypophosphoric acid, C α - C 6 alkyl sulfides and C x - C 6 alkylmorpholines and in the presence of a substituted rhenium oxide catalyst. 9. A method, as claimed in Claim 8, wherein said inert solvent is selected from the group consisting of aromatic hydrocarbons, aliphatic hydrocarbons, cycloaliphatic hydrocarbons, aliphatic esters, alcohols and water, or mixtures thereof; wherein the oxygen acceptor is a triarylphosphine; and wherein the catalyst is a C 2 - C ι0 alkylrhenium trioxide. 10. A method, as claimed in Claim 8, wherein triphenylphosphine is the oxygen acceptor and is present at levels of from about 1.0 to about 3.0 moles per mole of the starting epoxyphytol and wherein methylrhenium trioxide is the catalyst and is present at levels of from about 0.01 to about 5.0 weight percent based on the starting epoxyphytol. 11. A method, as claimed in Claim 1, wherein said step of reacting is conducted in the presence of a Lewis acid catalyst. 12. A method, as claimed in Claim 11, wherein said Lewis acid catalyst is zinc chloride. 13. A method for producing alpha-tocopherol from geranylgeraniol, comprising: (a) selectively oxidizing the 2, 3-carbon-carbon double bond in geranylgeraniol to produce geranylgeraniol- 2, 3-epoxide; (b) hydrogenating the three remaining carbon-carbon double bonds in said epoxide to produce epoxyphytol; (c) deoxygenating said epoxyphytol to produce a mixture of phytol and isophytol by reaction with an oxygen acceptor; and (d) reacting said phytol and isophytol mixture with trimethylhydroquinone to produce alpha-tocopherol. 14. A method, as claimed in Claim 13, wherein said step of selectively oxidizing is carried out in an inert solvent using t-butyl hydroperoxide in the presence of vanadium or molybdenum as the oxidant. 15. A method, as claimed in Claim 13, wherein said inert solvent is selected from the group consisting of aromatic hydrocarbons, aliphatic hydrocarbons, cycloaliphatic hydrocarbons and aliphatic esters or mixtures thereof. 16. A method, as claimed in Claim 13, wherein said step of hydrogenating is conducted in an inert solvent in the presence of a catalyst selected from the group consisting of Raney nickel, palladium on carbon and platinum on carbon. 17. A method, as claimed in Claim 16, wherein said inert solvent is selected from the group consisting of aliphatic esters, alkanols, aromatic hydrocarbons, aliphatic hydrocarbons and ethers, or mixtures, and wherein said step of hydrogenating is conducted under a pressure of from about 1 atmosphere to about 200 atmospheres at temperatures between about 0°C and about 150°C. 18. A method, as claimed in Claim 16, wherein said catalyst is present at a level of about 0.001 to about 0.5 weight percent based on the starting weight of geranylgeraniol - 2, 3-epoxide. 19. A method, as claimed in Claim 13, wherein said step of deoxygenating is conducted in the presence of a substituted rhenium trioxide catalyst. 20. A method, as claimed in Claim 13, wherein said step of deoxygenating is conducted in an inert solvent using an oxygen acceptor selected from the group consisting of triarylphosphines, tri-Ci - C 18 alkylphosphines, triaryl phosphites, tri-C - C 18 alkylphosphites, alkali metal hypophosphites, hypophosphoric acid, C x - C 6 alkyl sulfides and Ci - C 6 alkylmorpholines and in the presence of a substituted rhenium oxide catalyst. 21. A method, as claimed in Claim 20, wherein said inert solvent is selected from the group consisting of aromatic hydrocarbons, aliphatic hydrocarbons, cycloaliphatic hydrocarbons, aliphatic esters, alcohols and water, or mixtures thereof; wherein the oxygen acceptor is a triarylphosphine; and wherein the catalyst is a C : - C 10 alkylrhenium trioxide. 22. A method, as claimed in Claim 20, wherein triphenylphosphine is the oxygen acceptor and is present at levels of from about 1.0 to about 3.0 moles per mole of the starting epoxyphytol and wherein methylrhenium trioxide is the catalyst and is present at levels of from about 0.01 to about 5.0 weight percent based on the starting epoxyphytol. 23. A method, as claimed in Claim 13, wherein said step of reacting is conducted in the presence of a Lewis acid catalyst. 24. A method, as claimed in Claim 23, wherein said Lewis acid catalyst is zinc chloride. 25. The method of Claim 1, wherein said step of biologically producing comprises: (a) culturing a microorganism in a fermentation medium, wherein the action of squalene synthase of said microorganism is reduced, and wherein said step of culturing produces a product selected from the group consisting of geranylgeranyl phosphate and geranylgeraniol; and (b) recovering said product. 26. The method of Claim 25, wherein said fermentation medium comprises a squalene synthase inhibitor. 27. The method of Claim 25, wherein said microorganism is genetically modified to decrease the action of squalene synthase. 28. The method of Claim 27, wherein said microorganism is further genetically modified to increase the action of HMG-CoA reductase. 29. The method of Claim 28, wherein the action of HMG-CoA reductase is increased by overexpression of HMG-CoA reductase or the catalytic domain thereof in the microorganism. 30. The method of Claim 29, wherein said microorganism is further genetically modified to increase the action of a protein selected from the group consisting of acetoacetyl Co-A thiolose, HMG-CoA synthase, mevalonate kinase, phosphomevalonate kinase, phosphomevalonate decarboxylase, isopentenyl pyrophosphate isomerase, farnesyl pyrophosphate synthase, D-1-deoxyxylulose 5- phosphate synthase, and 1-deoxy-D-xylulose 5-phosphate reductoisomerase . 31. The method of Claim 30, wherein the microorganism has been genetically modified to increase the action of farnesyl pyrophosphate synthase. 32. The method of Claim 31, wherein the microorganism has been genetically modified to overexpress farnesyl pyrophosphate synthase. 33. The method of Claim 30, wherein the microorganism has been genetically modified to increase the action of geranylgeranyl pyrophosphate synthase. 34. The method of Claim 33, wherein the microorganism has been genetically modified to overexpress geranylgeranyl pyrophosphate synthase. 35. The method of Claim 25, wherein said microorganism is an erg9 mutant. 36. The method of Claim 35, wherein said microorganism comprises a erg9Δ : :HIS3 deletion/insertion allele. 37. The method of Claim 25, wherein said recovering step comprises recovering said product from said microorganism. 38. The method of Claim 25, wherein said product is secreted into said fermentation medium by said microorganism and wherein said step of recovering comprises purification of said product from said fermentation medium. 39. The method of Claim 25, wherein said product is intracellular geranylgeranyl phosphate and geranylgeraniol and said step of recovering comprises isolating said geranylgeranyl phosphate and geranylgeraniol from said microorganis . 40. The method of Claim 25, wherein said product is intracellular geranylgeranyl phosphate and said step of recovering further comprises dephosphorylating said geranylgeranyl phosphate to produce geranylgeraniol. 41. The method of Claim 25, wherein said microorganism is selected from the group consisting of fungi, bacteria and microalgae. 42. The method of Claim 25, wherein said microorganism is a yeast. 43. The method of Claim 42, wherein said yeast is blocked in the ergosterol pathway and is genetically modified to take up exogenous sterols under aerobic conditions. 44. The method of Claim 25, wherein said microorganism has been genetically modified to increase phosphatase action. 45. A method for producing a mixture of phytol and isophytol, comprising reacting epoxyphytol with an oxygen acceptor in the presence of a substituted rhenium trioxide catalyst. 46. A method, as claimed in Claim 45, wherein said step of reacting is carried out in an inert solvent using an oxygen acceptor selected from the group consisting of triarylphosphines, tri C τ - C 18 alkylphosphines, triaryl phosphites, tri-Cx - C 18 alkylphosphites, alkali metal hypophosphites, hypophosphoric acid, C x - C 6 alkyl sulfides and C - C 6 alkylmorpholines and in the presence of a substituted rhenium oxide catalyst. 47. A method, as claimed in Claim 46, wherein said inert solvent is selected from the group consisting of aromatic hydrocarbons, aliphatic hydrocarbons, cycloaliphatic hydrocarbons, aliphatic esters, alcohols and water, and mixtures thereof; wherein the oxygen acceptor is a triarylphosphine; and wherein said catalyst is a C x - C 10 alkylrhenium trioxide. 48. A method, as claimed in Claim 47, wherein the oxygen acceptor is triphenylphosphine and the C x - C 10 alkylrhenium trioxide catalyst is methylrhenium trioxide. 49. A method, as claimed in Claim 47, wherein the oxygen acceptor is used at levels of from about 1.0 to about 3.0 moles per mole of starting epoxyphytol and the catalyst is present at levels of from about 0.01 to about 5.0 weight percent based on the starting epoxyphytol. 50. A method for preparing gamma-tocopherol which comprises catalytic hydrogenation of 4-chromanone tocotrienol . 51. A method, as claimed in Claim 50, wherein said hydrogenation is conducted in the presence of a catalyst selected from the group consisting of Raney nickel, Raney cobalt, copper chromite, and a precious metal heterogeneous or homogeneous catalyst. 52. A method, as claimed in Claim 50, wherein said hydrogenation is conducted in the presence of a catalyst selected from the group consisting of Raney nickel, copper chromite and mixtures thereof. 53. A method, as claimed in Claim 50, wherein said hydrogenation is conducted in the presence of a Raney nickel catalyst. 54. A method, as claimed in Claim 50, wherein said hydrogenation is conducted in a solvent selected from the group consisting of methanol, ethanol, isopropanol, and ethyl acetate. 55. A method, as claimed in Claim 50, wherein said hydrogenation is conducted in an ethanol solvent. 56. A method, as claimed in Claim 55, wherein said hydrogenation is conducted at a hydrogen pressure of from about 100 psi of hydrogen to about 3000 psi of hydrogen. 57. A method, as claimed in Claim 55, wherein said hydrogenation is conducted at a hydrogen pressure of from about 400 psi of hydrogen to about 750 psi of hydrogen. 58. A method, as claimed in Claim 57, wherein said hydrogenation is conducted at a temperature of about 50°C to about 250°C. 59. A method, as claimed in Claim 50, wherein said hydrogenation is conducted at a temperature of about 135°C to about 175°C.

Inventors: HYATT JOHN A, MAURINA-BRUNKER JULIE, MCMULLIN THOMAS W, MILLIS JAMES R, SAUCY GABRIEL G, HYATT, JOHN, A., MAURINA-BRUNKER, JULIE, MCMULLIN, THOMAS, W., MILLIS, JAMES, R., SAUCY, GABRIEL, G.
Applicants: DCV INC, EASTMAN CHEM CO, DCV, INC. DOING BUSINESS AS BIO-TECHNICAL RESOURCES, EASTMAN CHEMICAL COMPANY
Application year: 1999
Main classification: C07C45
IPC codes: C07B61, C07C43, C07C69, C07D301, C07D303, C07D311, C12P7, C12P9