BIOPRODUCTION OF PARA-HYDROXYCINNAMIC ACID

Abstract: The present invention provides several methods for biological production of <i>para</i>-hydroxycinnamic acid (PHCA). The invention is also directed to the discovery of new fungi and bacteria that possess the ability to convert cinnamate to PHCA. The invention relates to developing of a new biocatalyst for conversion of glucose to PHCA by incorporation of the wild type PAL from the yeast <i>Rhodotorula glutinis</i> into <i>E. coli</i> unerlining the ability of the wildtype PAL to convert tyrosine to PHCA. The invention is also directed to developing a new biocatalyst for conversion of glucose to PHCA by incorporation of the wildtype PAL from the yeast <i>Rhodotorula glutinis</i> plus the plant cytochrome P-450 and the cytochrome P-450 reductase into <i>E. coli</i>. In yet another embodiment, the present invention provides for the developing of a new biocatalyst through mutagenesis of the wild type yeast PAL which possesses enhanced tyrosine ammonia-lyase (TAL) activity.

Description: TITLE BIOPRODUCTION OF PARA-HYDROXYCINNAMIC ACID This application claims the benefit of U.S. Provisional Application 60/147,719 filed on August 6, 1999. FIELD OF THE INVENTION This invention relates to the field of molecular biology and microbiology. More specifically, this invention describes a new, genetically engineered biocatalyst possessing enhanced tyrosine ammonia-lyase activity. BACKGROUND OF THE INVENTION Phenylalanine ammonia-lyase (PAL) (EC 4.3.1.5) is widely distributed in plants (Koukol et al., J. Biol. Chem. 236:2692-2698 (1961)), fungi (Bandoni et al., Phytochemistry 7:205-207 (1968)), yeast (Ogata et al., Agric. Biol. Chem. 31:200-206 (1967)), and Streptomyces (Ernes et al., Can. J. Microbiology 48:613-622 (1970)), but it has not been found in Escherichia coli or mammalian cells (Hanson and Havir In The Enzymes, 3 rc * ed.; Boyer, P., Ed.; Academic: New York, 1967; pp 75-167). PAL is the first enzyme of phenylpropanoid metabolism and catalyzes the removal of the (pro-3S)-hydrogen and -NH 3 + from L-phenylalanine to form tπm_-cinnamic acid. In the presence of a P450 enzyme system, /rαm-cinnamic acid can be converted to/>αrα-hydroxycinnamic acid (PHCA) which serves as the common intermediate in plants for production of various secondary metabolites such as lignin and isoflavonoids. In microbes however, cinna ic acid and not the PHCA acts as the precursor for secondary metabolite formation. No cinnamate hydroxylase enzyme has so far been characterized from microbial sources. The PAL enzyme in plants is thought to be a regulatory enzyme in the biosynthesis of lignin, isoflavonoids and other phenylpropanoids (Hahlbrock et al., Annu. Rev. Plant Phys. Plant Mol. Biol. 40:347-369 (1989)). However, in the red yeast, Rhodotorula glutinis (Rhodosporidium toruloides), this lyase degrades phenylalanine as a catabolic function and the cinnamate formed by the action of this enzyme is converted to benzoate and other cellular materials. The gene sequence of PAL from various sources, including Rhodosporidium toruloides, has been determined and published (Edwards et al., Proc. Natl. Acad. Set., USA 82:6731-6735 (1985); Cramer et al., Plant Mol. Biol. 12:367-383 (1989); Lois et al., EMBOJ. 8:1641-1648 (1989); Minami et al., Eur. J Biochem. 185:19-25 (1989); Anson et al., Gene 58:189-199 (1987); Rasmussen & Oerum, DNA Sequence, 1 :207-211 (1991). The PAL genes from various sources have been over-expressed as active PAL enzyme in yeast, Escherichia coli and insect cell culture (Faulkner et al., Gene 143:13-20 (1994); Langer et al., Biochemistry 36:10867-10871 (1997); McKegney et al., Phytochemistry 41:1259-1263 (1996)). PAL has received attention because of its potential usefulness in correcting the inborn error of metabolism phenylketonuria (Bourget et al., FEBS Lett. 180:5-8 (1985); U.S. 5,753,487), in altering tumor metabolism (Fritz et al. J Biol. Chem. 251 :4646-4650 (1976)), in quantitative analysis of serum phenylalanine (Koyama et al., Clin. Chim. Acta, 136:131-136 (1984)) and as a route for synthesizing L-phenylalanine from cinnamic acid (Yamada et al., Appl. Environ. Microbiol. 42:773 (1981), Hamilton et al., Trends in Biotechnol. 3:64-68 (1985) and Evans et al., Microbial Biotechnology 25:399-405 (1987)). In plants, the PAL enzyme converts phenylalanine to trøns-cinnamic acid which in turn is hydroxylated at the para position by cinnamate-4-hydroxylase to make PHCA (Pierrel et al., Eur. J. Biochem. 224:835 (1994); Urban et al., Eur. J Biochem. 222:843 (1994); Cabello-Hurtado et al., J. Biol. Chem. 273:7260 (1998); and Teutsch et al., Proc. Natl. Acad. Sci. USA 90:4102 (1993)). However, since further metabolism of cinnamic acid in microbial systems does not usually involve its para hydroxylation to PHCA, information regarding this reaction in microorganisms is scarce. Information available indicates that PAL from some plants and micro-organisms, in addition to its ability to convert phenylalanine to cinnamate, can accept tyrosine as substrate. In such reactions the enzyme activity is designated tyrosine ammonia lyase (TAL). Conversion of tyrosine by TAL results in the direct formation of PHCA from tyrosine without the intermediacy of cinnamate. However, all natural PAL/TAL enzymes prefer to use phenylalanine rather than tyrosine as their substrate. The level of TAL activity is always lower than PAL activity, but the magnitude of this difference varies over a wide range. For example, the parsley enzyme has a K ^ for phenylalanine of 15-25 μM and for tyrosine 2.0 - 8.0 mM with turnover numbers 22/sec and 0.3/sec respectively (Appert et al., Ewr. J Biochem. 225:491 (1994)). In contrast, the maize enzyme has a __M for phenylalanine only fifteen times higher than for tyrosine, and turnover numbers about ten-fold higher (Havir et al., Plant Physiol. 48: 130 (1971)). The exception to this rule, is the yeast, Rhodosporidium, in which a ratio of TAL catalytic activity to PAL catalytic activity is approximately 0.58 (Hanson and Havir In The Biochemistry of Plants; Academic: New York, 1981; Vol. 7, pp 577-625). The above mentioned biological systems provide a number of enzymes that may be useful in the production of PHCA, however, the efficient production of this monomer has not been achieved. The problem to be overcome therefore is the design and implementation of a method for the efficient production of PHCA from a biological source using an inexpensive substrate or fermentable carbon source. Applicants have solved the stated problem by engineering both microbial and plant hosts to produce PHCA, either by the overexpression of foreign genes encoding PAL and p450/p-450 reductase system or by the expression of genes encoding mutant and wildtype TAL activity. SUMMARY OF THE INVENTION The object of the present invention is bioproduction of PHCA, a compound that has potential as a monomer for production of Liquid Crystal Polymers (LCP). There are two potential bio-routes for production of PHCA from glucose and other fermentable carbon substrates: 1) Conversion of phenylalanine to cinnamic acid to PHCA. This route requires the enzyme PAL as well as a cytochrome P-450 and a cytochrome P-450 reductase (Scheme 1). 2) Conversion of tyrosine to PHCA in one step without the intermediacy of cinnamate (Scheme 1). This route requires the enzyme TAL which is likely to be very similar to PAL but with a higher substrate specificity for tyrosine. This route does not require the cytochrome P-450 and the cytochrome P-450 reductase. Operation of the TAL route therefore requires generation of a biocatalyst with increased TAL activity to function through the TAL route. Scheme 1 phenylalanine The present invention describes methods for bioproduction of PHCA through conversion of: 1) cinnamate to PHCA; 2) glucose to phenylalanine to PHCA via the PAL route and 3) through generation of a new biocatalyst possessing enhanced tyrosine ammonia-lyase (TAL) activity. The evolution of TAL requires isolation of a yeast PAL gene, mutagenesis and evolution of the PAL coding sequence, and selection of variants with improved TAL activity. The instant invention further demonstrates the bioproduction of PHCA from glucose through the above mentioned routes in various fungi and bacteria. It is an object of the present invention therefore to provide a method for the production of PHCA comprising: (i) contacting a recombinant host cell with a fermentable carbon substrate, said recombinant cell lacking a P-450/P-450 reductase system and comprising a gene encoding a tyrosine ammonia lyase activity operably linked to suitable regulatory sequences (ii) growing said recombinant cell for a time sufficient to produce PHCA; and (iii) optionally recovering said PHCA. Within the context of the invention a fermentable carbon substrate may be selected from the group consisting of monosaccharides, oligosaccharides, polysaccharides, carbon dioxide, methanol, formaldehyde, formate, and carbon-containing amines and the host cell from the group consisting of bacteria, yeasts, filamentous fungi, algae and plant cells. Similarly provided are recombinant host cells lacking a cytochrome P-450/P-450 reductase system and comprising a gene encoding a tyrosine ammonia lyase activity operably linked to suitable regulatory sequences. Additionally provided is a method for the production of PHCA comprising: (i) contacting a recombinant yeast cell with a fermentable carbon substrate , said recombinant cell comprising: a) a gene encoding a plant P-450 P-450 reductase system; and b) a gene encoding a yeast PAL activity operably linked to suitable regulatory sequences; (ii) growing said recombinant cell for a time sufficient to produce PHCA; and (iii) optionally recovering said PHCA. It is another object of the present invention to provide a method for identifying a gene encoding a TAL activity comprising: (i) contacting a recombinant microorganism comprising a foreign gene suspected of encoding a TAL activity with PHCA for a time sufficient to metabolize PHCA; and (ii) monitoring the growth the recombinant microorganism whereby growth of the organism indicates the presence of a gene encoding a TAL activity. Similarly a method for identifying a gene encoding a TAL activity is provided comprising: (i) fransforming a host cell capable of using PHCA as a sole carbon source with a gene suspected of encoding a TAL activity to create a transformant; (ii) comparing the rate of growth of the transformant with an un- transformed host cell capable of using PHCA as a sole carbon source wherein an accelerated rate of growth by the transformant indicates the presence of a gene encoding a TAL activity. BRIEF DESCRIPTION OF THE DRAWINGS AND SEQUENCE DESCRIPTIONS AND BIOLOGICAL DEPOSITS Figure 1 is a plasmid map of the vector PCA12Km, derived from pBR322, and used for the construction of the PAL expression vector PCA18Km. Figure 2 is a plasmid map of the vector pETAL containing the mutal PAL/TAL enzyme. Figure 3 shows the SDS-PAGE of purified mutant PAL enzyme and the cell crude extracts used as the starting materials for purification of the mutant PAL enzyme. Figure 4 is a plasmid map of the expression vector pGSWlδ used for the expression of the mutant PAL/TAL enzyme in yeast. Applicants made the following biological deposits under the terms of the Budapest Treaty on the International Recognition of the Deposit of Microorganisms for the Purposes of Patent Procedure at the American Type Culture Collection (ATCC) 10801 University Boulevard, Manassas, VA 20110-2209: International Depositor Identification Depository Reference Designation Date of Deposit E. coli pKK223-3 PAL in DH10B PTA 407 July 21, 1999 S. cereviseae containing wild-type PAL PTA 408 July 21, 1999 S. cereviseae Aro4GSW PTA 409 July 21, 1999 The invention can be more fully understood from the following detailed description and the accompanying sequence descriptions which form a part of this application. Applicant(s) have provided 14 sequences in conformity with 37 C.F.R. 1.821-1.825 ("Requirements for Patent Applications Containing Nucleotide Sequences and or Amino Acid Sequence Disclosures - the Sequence Rules") and consistent with World Intellectual Property Organization (WIPO) Standard ST.25 (1998) and the sequence listing requirements of the EPO and PCT (Rules 5.2 and 49.5(a-bis), and Section 208 and Annex C of the Adminstrative Instructions). SEQ ID NOs: 1 -6 are primers used for vector construction. SEQ ID NO:7 is the nucleotide sequence encoding the wildtype R. glutinis PAL enzyme. SEQ ID NO: 8 is the deduced amino acid sequence encoded by the nucleotide sequence encoding the wildtype R. glutinis PAL enzyme. SEQ ID NO: 9 is the nucleotide sequence encoding the mutant R. glutinis PAL enzyme having enhanced TAL activity. SEQ ID NO: 10 is the deduced amino acid sequence encoded by the nucleotide sequence encoding the mutant R. glutinis PAL enzyme having enhanced TAL activity. SEQ ID NO:l 1 is the nucleotide sequence encoding the H. tuber osus cytochrome p-450 enzyme. SEQ ID NO: 12 is the deduced amino acid sequence encoded by the nucleotide sequence encoding the H. tuber osus cytochrome p-450 enzyme. SEQ ID NO: 13 is the nucleotide sequence encoding the H. tuber osus p-450 reductase enzyme. SEQ ID NO: 14 is the deduced amino acid sequence encoded by the nucleotide sequence encoding the H. tuber osus p-450 reductase enzyme. DETAILED DESCRIPTION OF THE INVENTION The present invention describes biological methods for the production of PHCA. In one embodiment various bacteria and fungi were discovered that have the ability to convert trø/w-cinnamate to PHCA. In another embodiment yeast PAL was transformed into a host E. coli and conversion of glucose to PHCA was demonstrated. In an alternate embodiment yeast PAL and the Jerusalem Artichoke plant cytochrome P-450 and the cytochrome P-450 reductase genes were incorporated into yeast host strain and the recombinant yeast had the ability to convert glucose to PHCA. In an additional embodiment a new bio-catalyst possessing enhanced tyrosine ammonia-lyase (TAL) activity was developed and the gene encoding this activity was used to transform a recombinant host for the production of PHCA. The evolution of TAL required isolation of functional PAL gene, construction of a weak expression vector, mutagenesis and evolution of the PAL coding sequence, and selection of variants with improved TAL activity. The evolved TAL enzyme enables microorganisms to produce PHCA from tyrosine in a single step. The following abbreviations and definitions will be used for the interpretation of the specification and the claims. "Phenyl ammonia-lyase" is abbreviated PAL. "Tyrosine ammonia-lyase" is abbreviated TAL. "Pαr -hydroxycinnamic acid" is abbreviated PHCA. "Cinnamate 4-hydroxylase" is abbreviated C4H. As used herein the terms "cinnamic acid" and "cinnamate" are used interchangeably. The term "TAL activity" refers to the ability of a protein to catalyze the direct conversion of tyrosine to PHCA. The term "PAL activity" refers to the ability of a protein to catalyze the conversion of phenylalanine to cinnamic acid. The term "P-450/P-450 reductase system" refers to a protein system responsible for the catalytic conversion of cinnamic acid to PHCA. The P-450/P-450 reductase system is one of several enzymes or enzyme systems known in the art that perform a cinnamate 4-hydroxylase function. As used herein the term "cinnamate 4-hydroxylase" will refer to the general enzymatic activity that results in the conversion of cinnamic acid to PHCA, whereas the term "P-450/P-450 reductase system" will refer to a specific binary protein system that has cinnamate 4-hydroxylase activity. The term "PAL/TAL activity" or "PAL/TAL enzyme" refers to a protein which contains both PAL and TAL activity. Such a protein has at least some specificity for both tyrosine and phenylalanine as an enzymatic substrate. The term "mutant PAL/TAL" refers to a protein which has been derived from a wild type PAL enzyme which has greater TAL activity than PAL activity. As such, a mutant PAL/TAL protein has a greater substrate specificity for tyrosine than for phenylalanine. The term "catalytic efficiency" will be defined as the k^K j ^ of an enzyme. "Catalytic efficiency" will be used to quantitate the specificity of an enzyme for a substrate. The term "k^" is often called the "turnover number". The term "k^t" is defined as the maximum number of substrate molecules converted to products per active site per unit time, or the number of times the enzyme turns over per unit time, kcat = Vmax / [E], where [E] is the enzyme concentration (Ferst In Enzyme Structure and Mechanism, 2 nd ed.; W.H. Freeman: New York, 1985; pp 98-120). The term "aromatic amino acid biosynthesis" means the biological processes and enzymatic pathways internal to a cell needed for the production of an aromatic amino acid. The term "fermentable carbon substrate" refers to a carbon source capable of being metabolized by host organisms of the present invention and particularly carbon sources selected from the group consisting of monosaccharides, oligosaccharides, polysaccharides, and one-carbon substrates or mixtures thereof. The term "complementary" is used to describe the relationship between nucleotide bases that are capable to hybridizing to one another. For example, with respect to DNA, adenosine is complementary to thymine and cytosine is complementary to guanine. Accordingly, the instant invention also includes isolated nucleic acid fragments that are complementary to the complete sequences as reported in the accompanying Sequence Listing as well as those substantially similar nucleic acid sequences. "Gene" refers to a nucleic acid fragment that expresses a specific protein, including regulatory sequences preceding (5' non-coding sequences) and following (3' non-coding sequences) the coding sequence. "Native gene" or "wild type gene" refers to a gene as found in nature with its own regulatory sequences. "Chimeric gene" refers any gene that is not a native gene, comprising regulatory and coding sequences that are not found together in nature. Accordingly, a chimeric gene may comprise regulatory sequences and coding sequences that are derived from different sources, or regulatory sequences and coding sequences derived from the same source, but arranged in a manner different than that found in nature. "Endogenous gene" refers to a native gene in its natural location in the genome of an organism. A "foreign" gene refers to a gene not normally found in the host organism, but that is introduced into the host organism by gene transfer. Foreign genes can comprise native genes inserted into a non-native organism, or chimeric genes. "Coding sequence" refers to a DNA sequence that codes for a specific amino acid sequence. "Suitable regulatory sequences" refer to nucleotide sequences located upstream (5 * non-coding sequences), within, or downstream (3 1 non-coding sequences) of a coding sequence, and which influence the transcription, RNA processing or stability, or translation of the associated coding sequence. Regulatory sequences may include promoters, translation leader sequences, introns, and polyadenylation recognition sequences. "Promoter" refers to a DNA sequence capable of controlling the expression of a coding sequence or functional RNA. In general, a coding sequence is located 3 1 to a promoter sequence. Promoters may be derived in their entirety from a native gene, or be composed of different elements derived from different promoters found in nature, or even comprise synthetic DNA segments. It is understood by those skilled in the art that different promoters may direct the expression of a gene in different tissues or cell types, or at different stages of development, or in response to different environmental conditions. Promoters which cause a gene to be expressed in most cell types at most times are commonly referred to as "constitutive promoters". It is further recognized that since in most cases the exact boundaries of regulatory sequences have not been completely defined, DNA fragments of different lengths may have identical promoter activity. The term "operably linked" refers to the association of nucleic acid sequences on a single nucleic acid fragment so that the function of one is affected by the other. For example, a promoter is operably linked with a coding sequence when it is capable of affecting the expression of that coding sequence (i.e., that the coding sequence is under the transcriptional control of the promoter). Coding sequences can be operably linked to regulatory sequences in sense or antisense orientation. The term "expression", as used herein, refers to the transcription and stable accumulation of sense (mRNA) or antisense RNA derived from the nucleic acid fragment of the invention. Expression may also refer to translation of mRNA into a polypeptide. "Antisense inhibition" refers to the production of antisense RNA transcripts capable of suppressing the expression of the target protein. "Overexpression" refers to the production of a gene product in transgenic organisms that exceeds levels of production in normal or non-transformed organisms. "Co-suppression" refers to the production of sense RNA transcripts capable of suppressing the expression of identical or substantially similar foreign or endogenous genes (U.S. Patent No. 5,231,020). "RNA transcript" refers to the product resulting from RNA polymerase-catalyzed transcription of a DNA sequence. When the RNA transcript is a perfect complementary copy of the DNA sequence, it is referred to as the primary transcript or it may be a RNA sequence derived from posttranscriptional processing of the primary transcript and is referred to as the mature RNA. "Messenger RNA (mRNA)" refers to the RNA that is without introns and that can be translated into protein by the cell. "cDNA" refers to a double-stranded DNA that is complementary to and derived from mRNA. "Sense" RNA refers to RNA transcript that includes the mRNA and so can be translated into protein by the cell. "Antisense RNA" refers to a RNA transcript that is complementary to all or part of a target primary transcript or mRNA and that blocks the expression of a target gene (U.S. Patent No. 5,107,065). The complementarity of an antisense RNA may be with any part of the specific gene transcript, i.e., at the 5' non-coding sequence, 3' non-coding sequence, introns, or the coding sequence. "Functional RNA" refers to antisense RNA, ribozyme RNA, or other RNA that is not translated yet has an effect on cellular processes. "Transformation" refers to the transfer of a nucleic acid fragment into the genome of a host organism, resulting in genetically stable inheritance. Host organisms containing the transformed nucleic acid fragments are referred to as "transgenic" or "recombinant" or "transformed" organisms. The terms "plasmid", "vector" and "cassette" refer to an extra chromosomal element often carrying genes which are not part of the central metabolism of the cell, and usually in the form of circular double-stranded DNA molecules. Such elements may be autonomously replicating sequences, genome integrating sequences, phage or nucleotide sequences, linear or circular, of a single- or double-stranded DNA or RNA, derived from any source, in which a number of nucleotide sequences have been joined or recombined into a unique construction which is capable of introducing a promoter fragment and DNA sequence for a selected gene product along with appropriate 3' untranslated sequence into a cell. "Transformation cassette" refers to a specific vector containing a foreign gene and having elements in addition to the foreign gene that facilitate transformation of a particular host cell. "Expression cassette" refers to a specific vector containing a foreign gene and having elements in addition to the foreign gene that allow for enhanced expression of that gene in a foreign host. The term "Lineweaver-Burk plot refers a plot of enzyme kinetic data for the purpose of evaluating the kinetic parameters, __ and V msκ . Standard recombinant DNA and molecular cloning techniques used here are well known in the art and are described by Sambrook, J., Fritsch, E. F. and Maniatis, T. Molecular Cloning: A Laboratory Manual, 2 nd ed.; Cold Spring Harbor Laboratory: Cold Spring Harbor, New York, 1989 (hereinafter "Maniatis"); and by Silhavy, T. J., Bennan, M. L. and Enquist, L. W. Experiments with Gene Fusions; Cold Spring Harbor Laboratory: Cold Spring Harbor, New York, 1984; and by Ausubel, F. M. et al., In Current Protocols in Molecular Biology, published by Greene Publishing and Wiley-Interscience, 1987. The present invention describes biological methods for the production of PHCA. The method makes use of genes encoding proteins having cinnamate 4-hydroxylase activity (C4H), phenylalanine ammonium-lyase (PAL) activity or tyrosine ammonium lyase (TAL) activity. A cinnamate hydroxylase activity will convert cinnamate to PHCA. Within the context of the present invention a P-450/P-450 reductase system performs this C4H function. A PAL activity will convert phenylalanine to PHCA in the presence of a P-450/P-450 reductase system. These activities are linked according to the following scheme: [PAL] [P-450/P-450 reductase] phenylalanine - cinnamic acid -> PHCA A TAL activity will convert tyrosine directly to PHCA with no intermediate step according to the following scheme: [TAL] tyrosine - PHCA In one embodiment the method utilizes recombinant microbial host cells expressing an activity comprising both PAL and TAL functionalities in the same protein. In this embodiment the host cell lacks the P-450/P-450 reductase system and produces PHCA via the TAL route. In another embodiment, the method utilizes a recombinant host comprising a gene encoding the PAL activity in the presence of the gene encoding the P-450/P-450 reductase system. In an alternate embodiment the invention describes a method for the production of PHCA from cinnamate by organisms selected for their C4H activity. The invention is useful for the biological production of PHCA which may be used as a monomer for production of Liquid Crystal Polymers (LCP). LCP's may be used in electronic connectors and telecommunication and aerospace applications. LCP resistance to sterilizing radiation has also enabled these materials to be used in medical devices as well as chemical, and food packaging applications. Genes: The key enzymatic activities used in the present invention are encoded by a number of genes known in the art. The principal enzymes include cinnamate- 4-hydroxylase (C4H) activity (P-450/P-450 reductase), phenylalanine ammonium lyase (PAL) and tyrosine ammonium lyase (TAL). Phenylalanine Ammonium Lvase (PAL). Tyrosine Ammonium Lyase (TAL) Activities and the P-450 P-450 reductase system: Genes encoding PAL are known in the art and several have been sequenced from both plant and microbial sources (see for example EP 321488 [R. toruloides]; WO 9811205 [Eucalyptus grandis and Pinus radiata]; WO 9732023 [Petunia]; JP 05153978 [Pisum sativum]; WO 9307279 [potato, rice]). The sequence of PAL genes is available (see for example GenBank AJ010143 and X75967). Where expression of a wild type PAL gene in a recombinant host is desired the wild type gene may be obtained from any source including but not limited to, yeasts such as Rhodotorula sp., Rhodosporidium sp. and Sporobolomyces sp.; bacterial organisms such as Streptomyces; and plants such as pea, potato, rice, eucalyptus, pine, corn, petunia, arabidopsis, tobacco, and parsley. There are no known genes which encode an enzyme having exclusively TAL activity, i.e., which will use only tyrosine as a substrate for the production of PHCA. Several of the PAL enzymes mentioned above have some substrate affinity for tyrosine. Thus genes encoding TAL activity may be identified and isolated concurrently with the PAL genes described above. For example, the PAL enzyme isolated from parsley (Appert et al., Eur. J. Biochem. 225:491 (1994)) and corn ((Havir et al., Plant Physiol. 48:130 (1971)) both demonstrate the ability to use tyrosine as a substrate. Similarly, the PAL enzyme isolated from Rhodosporidium (Hodgins DS, J. Biol. Chem. 246:2977 (1971)) also may use tyrosine as a substrate. Such enzymes will be referred to herein as PAL/TAL enzymes or activities. Where it is desired to create a recombinant organism expressing a wild type gene encoding PAL/TAL activity, genes isolated from maize, wheat, parsley, Rhizoctonia solani, Rhodosporidium, Sporobolomyces pararoseus and Rhodosporidium may be used as discussed in Hanson and Havir, The Biochemistry of Plants; Academic: New York, 1981; Vol. 7, pp 577-625, where the genes from Rhodosporidium are preferred. The invention provides a P-450/P-450 reductase system having C4H activity that is useful for the conversion of cinnamate to PHCA. This system is well known in the art and has been isolated from a variety of plant tissues. For example, the reductase as been isolated from Jerusalem Artichoke (Helianthus tuber osus), [embl locus HTU2NFR, accession Z26250.1]; parsley, (Petroselinum crispum) [Koopmann et al., Proc. Natl. Acad. Sci. U A. 94 (26), 14954-14959 (1997), [locus AF024634 accession AF024634.1]; California poppy (Eschscholzia californica), Rosco et al., Arch. Biochem. Biophys. 348 (2), 369-377 (1997), [locus ECU67186 accession U67186.1 ] ; Arabidopsis thaliana, [pir : locus S21531]; spring vetch (Vicia sativά), [pir: locus S37159]; mung bean, (Vigna radiata), Shet et al., Proc. Natl. Acad. Sci. U.S.A. 90 (7), 2890-2894 (1993), [pir: locus A47298]; and opium poppy (Papaver somniferum), [locus PSU67185 accession U67185.1]. The cytochrome has been isolated from the Jerusalem Artichoke (Helianthus tuber osus), [ercibl locus HTTC4MMR , accession Z17369.1]; Zinnia elegans, [swissprot: locus TCMO_ZINEL, accession Q43240] Catharanthus roseus [swissprot: locus TCMO CATRO, accession P48522]; Populus tremuloides [swissprot: locus TCMO_POPTM, accession 024312]J- Op ulus kitakamiensis [swissprot: locus TCMO_POPKI, accession Q43054]; Glycyrrhiza echinata [swissprot: locus TCMO_GLYEC, accession Q96423]; Glycine max [swissprot: locus TCMO_SOYBN, accession Q42797] as well as other sources. Preferred in the instant invention are the genes encoding the P-450/P-450 reductase system isolated from Jerusalem Artichoke (Helianthus tuberosus) as set forth in SEQ ID NO:l 1 and SEQ ID NO: 13. The skilled person will recognize that, for the purposes of the present invention, any cytochrome P-450 P-450 reductase system isolated from a plant will be suitable. As the sequence of the cytochrome gene (SEQ ID NO:l 1) ranges from about 92% identity (Zinnia elegans, Q43240) to about 63% identity (Phaseolus vulgar is, embl locus PV09449, accession Y09449.1) to known P-450 cytochromes in these systems, it is contemplated that any P-450 cytochrome isolated from a plant having at least 63% identity to SEQ ID NO: 11 will be suitable in the present invention. Similarly, as the p-450 reductase in the system (SEQ ID NO13) ranges from about 79% identity (parsley, AF024634.1] to about 68% identity (opium poppy, U67185.1) identity to known reductases P-450's it is contemplated that any P-450 reductase isolated from a plant having at least 68% identity to SEQ ID NO 13 will be suitable in the present invention. Methods of obtaining these or homologous wild type genes using sequence-dependent protocols are well known in the art. Examples of sequence- dependent protocols include, but are not limited to, methods of nucleic acid hybridization, and methods of DNA and RNA amplification as exemplified by various uses of nucleic acid amplification technologies (e.g., polymerase chain reaction (PCR), ligase chain reaction (LCR)). For example, genes encoding homologs or anyone of the mentioned activites (PAL, TAL or the P-450/P-450 reductase system) could be isolated directly by using all or a portion of the known sequences as DNA hybridization probes to screen libraries from any desired plant, fungi, yeast, or bacteria using methodology well known to those skilled in the art. Specific oligonucleotide probes based upon the literature nucleic acid sequences can be designed and synthesized by methods known in the art (Maniatis, supra). Moreover, the entire sequences can be used directly to synthesize DNA probes by methods known to the skilled artisan such as random primers DNA labeling, nick translation, or end- labeling techniques, or RNA probes using available in vitro transcription systems. In addition, specific primers can be designed and used to amplify a part of or full-length of the instant sequences. The resulting amplification products can be labeled directly during amplification reactions or labeled after amplification reactions, and used as probes to isolate full length cDNA or genomic fragments under conditions of appropriate stringency. In addition, two short segments of the literature sequences may be used in polymerase chain reaction protocols to amplify longer nucleic acid fragments encoding homologous genes from DNA or RNA. The polymerase chain reaction may also be performed on a library of cloned nucleic acid fragments wherein the sequence of one primer is derived from the literature sequences, and the sequence of the other primer takes advantage of the presence of the polyadenylic acid tracts to the 3 1 end of the mRNA precursor encoding bacterial genes. Alternatively, the second primer sequence may be based upon sequences derived from the cloning vector. For example, the skilled artisan can follow the RACE protocol (Frohman et al., PNAS USA 85:8998 (1988)) to generate cDNAs by using PCR to amplify copies of the region between a single point in the transcript and the 3' or 5' end. Primers oriented in the 3' and 5' directions can be designed from the literature sequences. Using commercially available 3' RACE or 5' RACE systems (BRL), specific 3' or 5* cDNA fragments can be isolated (Ohara et al., PNAS USA 86:5673 (1989); Loh et al., Science 243:217 (1989)). Mutant PAL/TAL Activities: It is an object of the present invention to provide a mutant PAL/TAL activity having a greater substrate specificity for tyrosine than for phenylalanine. Typically the approach will involve the selection of an organism having a PAL/TAL activity with a higher substrate specificity for tyrosine than for phenylalanine. Generally, the substrate specificity is quantitated by k f -^K^ (catalytic efficiency), calculated on the basis of the number of active sites identified in the enzyme. Phenylalanine ammonia-lyase has a molecular weight of about 330,000 and consists of four identical subunits of about 80 KD (Havir et al., Biochemistry 14:1620-1626 (1975)). It has been suggested that PAL contains a catalytically essential dehydroalanine residue (Hanson et al., Arch. Biochem. Biophys. 141:1-17 (1970)). Ser-202 of PAL from parsley has been indicated as the precursor of the dehydroalanine (Langer et al., Biochemistry, 36:10867-10871 (1997)). The k^ for PAL was calculated using information available from recent studies on the crystal structure of a homologous enzyme, histidine ammonia-lyase (HAL). These studies have revealed that the reactive electrophilic residue in the active site of the enzyme is a 4-methylidene-ididazole-5-one, which is autocatalytically formed by cyclization and dehydration of residues 142-144 containing the Ala-Ser-Gly sequence (Schwede et al., Biochemistry 38:5355-5361 (1999)). Since all tetrameric PAL enzymes studied so far, also contain the Ala-Ser-Gly sequence at each of their active sites, it is likely that each active site of PAL also contains a 4-methylidene-ididazole-5-one formed from this sequence. Within the context of the present invention, the suitable wildtype enzyme selected for mutagenesis has a catalytic efficiency of about 4.14 x 10 3 to 1 x 10 9 M^sec -1 for tyrosine where a catalytic efficiency in a range of about of about 1 x 10 4 M^sec" 1 to about 5 x 10 4 M^sec -1 is preferred. The process of the selection of a suitable PAL TAL enzyme, involves construction of a weak expression vector, mutagenesis and evolution of the PAL coding sequence, and finally selection of variants with improved TAL activity. Mutagenesis of PAL: A variety of approaches may be used for the mutagenesis of the PAL/TAL enzyme. Two suitable approaches used herein include error-prone PCR (Leung et al., Techniques, 1:11-15 (1989) and Zhou et al., Nucleic Acids Res. 19:6052-6052 (1991) and Spee et al., Nucleic Acids Res. 21:777-778 (1993)) and in vivo mutagenesis. The principal advantage of error-prone PCR is that all mutations introduced by this method will be within the PAL gene, and any change may be easily controlled by changing the PCR conditions. Alternatively in vivo mutagenesis, may be employed using commercially available materials such as E. coli XL 1 -Red strain, and the Epicurian coli XL 1 -Red mutator strain from Stratagene (Stratagene, La Jolla, CA, Greener and Callahan, Strategies 7:32-34 (1994)). This strain is deficient in three of the primary DNA repair pathways (mutS, mutD and mutT), resulting in a mutation rate 5000-fold higher than that of wild-type. In vivo mutagenesis does not depend on ligation efficiency (as with error-prone PCR), however a mutation may occur at any region of the vector and the mutation rates are generally much lower. Alternatively, it is contemplated that a mutant PAL/TAL enzyme with enhanced TAL activity may be constructed using the method of "gene shuffling" (U.S. 5,605,793; U.S. 5,811,238; U.S. 5,830,721; and U.S. 5,837,458). The method of gene shuffling is particularly attractive due to its facile implementation, and high rate of mutagenesis. The process of gene shuffling involves the restriction of a gene of interest into fragments of specific size in the presence of additional populations of DNA regions of both similarity to or difference to the gene of interest. This pool of fragments will then denature and then reanneal to create a mutated gene. The mutated gene is then screened for altered activity. Wild type PAL/TAL sequences may be mutated and screened for altered or enhanced TAL activity by this method. The sequences should be double stranded and can be of various lengths ranging from 50 bp to 10 kb. The sequences may be randomly digested into fragments ranging from about 10 bp to 1000 bp, using restriction endonucleases well known in the art (Maniatis supra). In addition to the full length sequences, populations of fragments that are hybridizable to all or portions of the sequence may be added. Similarly, a population of fragments which are not hybridizable to the wild type sequence may also be added. Typically these additional fragment populations are added in about a 10 to 20 fold excess by weight as compared to the total nucleic acid. Generally this process will allow generation of about 100 to 1000 different specific nucleic acid fragments in the mixture. The mixed population of random nucleic acid fragments are denatured to form single-stranded nucleic acid fragments and then reannealed. Only those single-stranded nucleic acid fragments having regions of homology with other single-stranded nucleic acid fragments will reanneal. The random nucleic acid fragments may be denatured by heating. One skilled in the art could determine the conditions necessary to completely denature the double stranded nucleic acid. Preferably the temperature is from 80 °C to 100 °C. The nucleic acid fragments may be reannealed by cooling. Preferably the temperature is from 20 °C to 75 °C. Renaturation can be accelerated by the addition of polyethylene glycol ("PEG") or salt. The salt concentration is preferably from 0 mM to 200 mM. The annealed nucleic acid fragments are next incubated in the presence of a nucleic acid polymerase and dNTP's (i.e., dATP, dCTP, dGTP and dTTP). The nucleic acid polymerase may be the Klenow fragment, the Taq polymerase or any other DNA polymerase known in the art. The polymerase may be added to the random nucleic acid fragments prior to annealing, simultaneously with annealing or after annealing. The cycle of denaturation, renaturation and incubation in the presence of polymerase is repeated for a desired number of times. Preferably the cycle is repeated from 2 to 50 times, more preferably the sequence is repeated from 10 to 40 times. The resulting nucleic acid is a larger double-stranded polynucleotide of from about 50 bp to about 100 kb and may be screened for expression and altered TAL activity by standard cloning and expression protocols. (Maniatis supra). Irrespective of the method of mutagenesis it is contemplated that a gene may be evolved having a catalytic efficiency of about 4.14 x 10 3 M^sec -1 to about 1 x 10 9 M _1 sec _1 where an catalytic efficiency of about 12.6 x 10 3 M^sec -1 is typical. Selection of Variants with Improved TAL Activity In order to select for those mutants having genes encoding proteins with enhanced TAL activity, a selection system based on the reversibility of the tyrosine to PHCA reaction was developed. It will be appreciated that the TAL activity responsible for the conversion of tyrosine to PHCA is in a state of equilibrium with the opposite reaction. Mutant genes were cloned by standard methods into E. coli tyrosine auxotrophs, unable to grow in the absence of tyrosine. Transformants were plated on tyrosine minus medium in the presence of suitable concentrations of PHCA. Those colonies which grew under these conditions were picked and analyzed for the presence of the mutant gene. In this fashion, a gene was isolated that had a catalytic efficiency of about 12.6 x 10 3 M _1 sec _1 and a ratio of TAL catalytic activity to PAL catalytic activity of 1.7 compared to 0.5 for the wild type. The skilled person will be able to envision additional screens for the selection of genes encoding enhanced TAL activity. For example, it is well known that Acinetobacter calcoaceticus DSM 586 (ATCC 33304) is able to efficiently degrade ? -coumaric acid (PHCA) and use it as a sole carbon source (Delneri et al., Biochim. Biophys. Acta 1244:363-367 (1995)). The proposed pathway for this degradation is shown as Pathway I; Pathway I /7-hydroxycinnamic acid -> 7-hydroxybenzoic acid - protocatechuic acid The enzymes involved in this proposed pathway are all induced by the addition of PHCA to cell cultures. By transformation of a TAL gene into A. calcoaceticus (ATCC 3304), or into other microorganisms able to use PHCA as a sole carbon source, the above pathway is now modified to show tyrosine as a substrate for PHCA, as illustrated in Pathway II; Pathway II L-tyrosine -> p -hydroxycinnamic acid -> /7-hydroxybenzoic acid -> protocatechuic acid It will be appreciated that cells possessing the elements of Pathway II, when grown on PHCA will show more vigorous growth than those possessing only Pathway I. Thus, this system may be used as a screen for the identification of genes possessing TAL activity. This selection system has the added advantage of avoiding the effects of inhibitory levels of PHCA as the cell contains a pathway to degrade this compound further until the carbon enters central metabolism. Production Organisms: Microbial Hosts The production organisms of the present invention will include any organism capable of expressing the genes required for the PHCA production. Typically the production organism will be restricted to microorganisms and plants. Microorganisms useful in the present invention for the production of PHCA may include, but are not limited to bacteria, such as the enteric bacteria (Escherichia, and Salmonella for example) as well as Bacillus, Acinetobacter, Streptomyces, Methylobacter, Rhodococcus and Pseudomona; Cyanobacteria, such as Rhodobacter and Synechocystis; yeasts, such as Saccharomyces, Zygosaccharomyces, Kluyveromyces, Candida, Hansenula, Debaryomyces, Mucor, Pichia and Torulopsis; and filamentous fungi such as Aspergillus and Arthrobotrys, and algae for example. The PAL, PAL/TAL and the P-450 and P-450 reductase genes of the present invention may be produced in these and other microbial hosts to prepare large, commercially useful amounts of PHCA. Microbial expression systems and expression vectors containing regulatory sequences that direct high level expression of foreign proteins are well known to those skilled in the art. Any of these could be used to construct chimeric genes for production of PHCA. These chimeric genes could then be introduced into appropriate microorganisms via transformation to allow for expression of high level of the enzymes. Vectors or cassettes useful for the transformation of suitable microbial host cells are well known in the art. Typically the vector or cassette contains sequences directing transcription and translation of the relevant gene, a selectable marker, and sequences allowing autonomous replication or chromosomal integration. Suitable vectors comprise a region 5' of the gene which harbors transcriptional initiation controls and a region 3' of the DNA fragment which controls transcriptional termination. It is most preferred when both control regions are derived from genes homologous to the transformed host cell, although it is to be understood that such control regions need not be derived from the genes native to the specific species chosen as a production host. Initiation control regions or promoters, which are useful to drive expression of the relevant genes in the desired host cell are numerous and familiar to those skilled in the art. Virtually any promoter capable of driving these genes is suitable for the present invention including but not limited to CYC1, HIS3, GAL1, GAL10, ADH1, PGK, PHO5, GAPDH, ADCl, TRP1, URA3, LEU2, ENO, TPI (useful for expression in Saccharomyces); AOX1 (useful for expression in Pichia); and lac, trp, 1P L , 1P R , T7, tac, and trc (useful for expression in Escherichia coli). Termination control regions may also be derived from various genes native to the preferred hosts. Optionally, a termination site may be unnecessary, however, it is most preferred if included. Where commercial production of PHCA is desired a variety of fermentation methodologies may be applied. For example, large scale production may be effected by both batch or continuous fermentation. A classical batch fermentation is a closed system where the composition of the media is set at the beginmng of the fermentation and not subject to artificial alterations during the fermentation. Thus, at the beginning of the fermentation the medium is inoculated with the desired microorganism or microorganisms and fermentation is permitted to occur adding nothing to the system. Typically, however, the concentration of the carbon source in a "batch" fermentation is limited and attempts are often made at controlling factors such as pH and oxygen concentration. In batch systems the metabolite and biomass compositions of the system change constantly up to the time the fermentation is stopped. Within batch cultures cells moderate through a static lag phase to a high growth log phase and finally to a stationary phase where growth rate is diminished or halted. If untreated, cells in the stationary phase will eventually die. Cells in the log phase generally are responsible for the bulk of production of end product or intermediate. A variation on the standard batch system is the Fed-Batch system. Fed-Batch fermentation processes are also suitable in the present invention and comprise a typical batch system with the exception that the substrate is added in increments as the fermentation progresses. Fed-Batch systems are useful when catabolite repression is apt to inhibit the metabolism of the cells and where it is desirable to have limited amounts of substrate in the medium. Measurement of the actual substrate concentration in Fed-Batch systems is difficult and is therefore estimated on the basis of the changes of measurable factors such as pH, dissolved oxygen and the partial pressure of waste gases such as CO2. Batch and Fed-Batch fermentations are common and well known in the art and examples may be found in Brock, T. D.; Biotechnology: A Textbook of Industrial Microbiology, 2nd ed.; Sinauer Associates: Sunderland, Massachusettes, 1989; or Deshpande, M. V. Appl. Biochem. Biotechnol. 36:227, (1992), herein incorporated by reference. Commercial production of PHCA may also be accomplished with continuous fermentation. Continuous fermentation is an open system where a defined fermentation medium is added continuously to a bioreactor and an equal amount of conditioned medium is removed simultaneously for processing. Continuous fermentation generally maintains the cultures at a constant high density where cells are primarily in their log phase of growth. Continuous fermentation allows for modulation of any number of factors that affect cell growth or end product concentration. For example, one method will maintain a limiting nutrient such as the carbon source or nitrogen level at a fixed rate and allow all other parameters to moderate. In other systems a number of factors affecting growth can be altered continuously while the cell concentration, measured by the medium turbidity, is kept constant. Continuous systems strive to maintain steady state growth conditions and thus the cell loss due to the medium removal must be balanced against the cell growth rate in the fermentation. Methods of modulating nutrients and growth factors for continuous fermentation processes as well as techniques for maximizing the rate of product formation are well known in the art of industrial microbiology and a variety of methods are detailed by Brock, supra. For production of PHCA via the PAL route in the presence of the P-450/P-450 reductase system any medium that will support the growth of the cells is suitable. Where, however, production of PHCA is desired as part of the natural carbon flow of the microorganism, the fermentation medium must contain suitable carbon substrates. Suitable substrates may include but are not limited to monosaccharides such as glucose, raffinose and fructose, oligosaccharides such as lactose or sucrose, polysaccharides such as starch or cellulose or mixtures thereof and unpurified mixtures from renewable feedstocks such as cheese whey permeate, cornsteep liquor, sugar beet molasses, and barley malt. Additionally the carbon substrate may also be one-carbon substrates such as carbon dioxide, formaldehyde, formate or methanol for which metabolic conversion into key biochemical intermediates has been demonstrated. Plant Hosts Alternatively, the present invention provides for the production of PHCA in plant cells harboring the relevant PAL, PAL/TAL and the P-450 and P-450 reductase genes. Preferred plant hosts will be any variety that will support a high production level of PHCA or PHCA-glucoside conjugate. Suitable green plants will include but are not limited to soybean, rapeseed (Brassica napus, B. campestris), sunflower (Helianthus annus), Jerusalem artichoke (Helianthus tuberosis), cotton (Gossypium hirsutum), corn, tobacco (Nicotiana tabacum), alfalfa (Medicago sativa), wheat (Triticum sp), barley (Hordeum vulgare), oats (Avena sativa, L), sorghum (Sorghum bicolor), rice (Oryza sativa), Arabidopsis, cruciferous vegetables (broccoli, cauliflower, cabbage, parsnips, etc.), melons, carrots, celery, parsley, tomatoes, potatoes, strawberries, peanuts, grapes, grass seed crops, sugar beets, sugar cane, beans, peas, rye, flax, hardwood trees, softwood trees, and forage grasses. Overexpression of the necessary genes of the present invention may be accomplished by first constructing chimeric genes in which the coding regions are operably linked to promoters capable of directing expression of a gene in the desired tissues at the desired stage of development. For reasons of convenience, the chimeric genes may comprise promoter sequences and translation leader sequences derived from the same genes. 3' Non-coding sequences encoding transcription termination signals must also be provided. The instant chimeric genes may also comprise one or more introns in order to facilitate gene expression. Any combination of any promoter and any terminator capable of inducing expression of a coding region may be used in the chimeric genetic sequence. Some suitable examples of promoters and terminators include those from nopaline synthase (nos), octopine synthase (ocs) and cauliflower mosaic virus (CaMV) genes. One type of efficient plant promoter that may be used is a high level plant promoter. Such promoters, in operable linkage with the genetic sequences of the present invention should be capable of promoting expression of the present gene product. High level plant promoters that may be used in this invention include the promoter of the small subunit (ss) of the ribulose-l,5-bisphosphate carboxylase for example from soybean (Berry-Lowe et al., J. Molecular andApp. Gen. 1 :483-498 (1982)), and the promoter of the chlorophyll a/b binding protein. These two promoters are known to be light-induced in plant cells (see for example, Cashmore, A. Genetic Engineering of Plants, an Agricultural Perspective; Plenum: New York, 1983; pp 29-38; Coruzzi et al., J. Biol. Chem. 258:1399 (1983), and Dunsmuir et al., J. Mol Appl. Genetics 2:285 (1983)). Plasmid vectors comprising the instant chimeric genes can then constructed. The choice of plasmid vector depends upon the method that will be used to transform host plants. The skilled artisan is well aware of the genetic elements that must be present on the plasmid vector in order to successfully transform, select and propagate host cells containing the chimeric gene. The skilled artisan will also recognize that different independent transformation events will result in different levels and patterns of expression (Jones et al., EMBO J. 4:2411-2418 (1985); De Almeida et al., Mol. Gen. Genetics 2I8:7S-S6 (1989)), and thus that multiple events must be screened in order to obtain lines displaying the desired expression level and pattern. Such screening may be accomplished by Southern analysis of DNA blots (Southern et al., J. Mol. Biol. 98:503 (1975)), Northern analysis of mRNA expression (Kroczek, J. Chromatogr. Biomed. Appl., 618:133-145 (1993), Western analysis of protein expression, enzymatic activity analysis of expressed gene product, or phenotypic analysis. For some applications it will be useful to direct the gene products of the PHCA producing genes to different cellular compartments. It is thus envisioned that the chimeric genes described above may be further supplemented by altering the coding sequences to encode enzymes with appropriate intracellular targeting sequences such as transit sequences (Keegstra, K., Cell 56:247-253 (1989)), signal sequences or sequences encoding endoplasmic reticulum localization (Chrispeels, J. J., Ann. Rev. Plant Phys. Plant Mol. Biol. 42:21-53 (1991)), or nuclear localization signals (Raikhel, N., Plant Phys. 100:1627-1632 (1992)) added and/or with targeting sequences that are already present removed. While the references cited give examples of each of these, the list is not exhaustive and more targeting signals of utility may be discovered in the future that are useful in the invention. Optionally it is contemplated that PHCA production in plants may be enhanced by the antisense inhibition or co-suppression of genes encoding enzymes down stream of PHCA. These enzymes may serve to transform PHCA into less useful products and prevent PHCA accumulation. Transgenic plants comprising constructs harboring genes encoding these down stream genes in antisense conformation may be useful in enhancing PHCA accumulation. Similarly, the same genes, overexpressed may serve to enhance PHCA accumulation by gene co-suppression. Thus, the skilled person will appreciate that chimeric genes designed to express antisense RNA (U.S. Patent No. 5,107,065) for all or part of the instant down stream genes can be constructed by linking the genes or gene fragment in reverse orientation to plant promoter sequences. Either the co-suppression or antisense chimeric genes could be introduced into plants via transformation whereby expression of the corresponding endogenous genes are reduced or eliminated Methods of Production: The present invention provides several methods for the bio-production of PHCA. In one embodiment cinnamate may be contacted with an organism which contains the requisite C4H activity. These organisms may be wild type or recombinant. Several organisms were uncovered by the present invention as having the ability to convert cinnamate to PCHA including Streptomyces griseus (ATCC 13273, ATCC 13968, TU6), Rhodococcus erythropolis (ATCC 4277), Aspergillus petrakii (ATCC 12337), Aspergillus niger (ATCC 10549) and Arthrobotrys robusta (ATCC 11856). In an alternate embodiment, yeast PAL and the plant cytochrome P-450 and the cytochrome P-450 reductase genes were incorporated into yeast host strains and the recombinant yeast demonstrated the ability to convert glucose to PHCA. Saccharomyces cerevisiae was chosen for this means of production, however it will be appreciated by the skilled artisan that a variety of yeasts will be suitable, including, but not limited to those microbial production organisms described above. Similarly, glucose was employed as a carbon substrate, however a variety of other fermentable carbon substrates may be used. In a preferred embodiment PHCA may be produced from a recombinant microorganism or plant cell which lacks a P-450/P-450 reductase system and harbors a PAL/TAL enzyme where the enzyme has a nώiimum level of TAL activity and the carbon flow is directed from a fermentable carbon source through tyrosine to PHCA. The present invention is further defined in the following Examples. It should be understood that these Examples, while indicating preferred embodiments of the invention, are given by way of illustration only. From the above discussion and these Examples, one skilled in the art can ascertain the essential characteristics of this invention, and without departing from the spirit and scope thereof, can make various changes and modifications of the invention to adapt it to various usage and conditions. EXAMPLES GENERAL METHODS: Procedures required for PCR amplification, DNA modifications by endo- and exonucleases for generating desired ends for cloning of DNA, ligation, and bacterial transformation are well known in the art. Standard molecular cloning techniques used here are well known in the art and are described by Sambrook, J., Fritsch, E. F. and Maniatis, T. Molecular Cloning: A Laboratory Manual, 2 nd ed.; Cold Spring Harbor Laboratory: Cold Spring Harbor, New York, 1989 (hereinafter "Maniatis"); and by Silhavy, T. J., Bennan, M. L. and Enquist, L. W. Experiments with Gene Fusions; Cold Spring Harbor Laboratory: Cold Spring, New York, 1984 and by Ausubel et al., Current Protocols in Molecular Biology; Greene Publishing and Wiley-Interscience; 1987. Materials and methods suitable for the maintenance and growth of bacterial cultures are well known in the art. Techniques suitable for use in the following examples may be found as set out in Manual of Methods for General Bacteriology; Phillipp Gerhardt, R. G. E. Murray, Ralph N. Costilow, Eugene W. Nester, Willis A. Wood, Noel R. Krieg and G. Briggs Phillips, Eds., American Society for Microbiology: Washington, DC, 1994 or by Brock, T. D.; Biotechnology: A Textbook of Industrial Microbiology, 2nd ed.; Sinauer Associates: Sunderland, MA, 1989. All reagents, restriction enzymes and materials used for the growth and maintenance of bacterial cells were obtained from Aldrich Chemicals (Milwaukee, WI), DIFCO Laboratories (Detroit, MI), GIBCO/BRL (Gaithersburg, MD), or Sigma Chemical Company (St. Louis, MO) unless otherwise specified. PCR reactions were run on GeneAMP PCR System 9700 using Amplitaq or Amplitaq Gold enzymes (PE Applied Biosystems, Foster City, CA). The cycling conditions and reactions were standardized according to the manufactures instructions. The meaning of abbreviations is as follows: "sec" means second(s), "min"means minute(s), "h" means hour(s), "d" means day(s), "μL" means microliter, "mL" means milliliters, "L" means liters, "mm" means millimeters, "nm" means nanometers, "mM" means millimolar, "M" means molar, "mmol" means millimole(s), "μmole" mean micromole", "g" means gram, "μg" means microgram and "ng" means nanogram, "U" means units, and "mU" means milliunits. Strains, vectors and culture conditions: Tyrosine auxotrophic Escherichia coli strain AT2471 and wild type Escherichia coli W3110 were originally obtained from Coli Genetic Stock Center (CGSC #4510), Yale University, New Haven, CT.). Epicurian coli XL 1 -Red strain was purchased from Stratagene. Escherichia coli BL21(DE3) cells were used for enzyme over-expression (Shuster, B. and Retey, J., FEBS Lett. 349:252-254 (1994)). pBR322 and pET-24d vectors were purchased from New England Biolab (Bevely, MA) and Novagen (Madison, WI), respectively. pKK223-3 was purchased from Amersham Pharmacia. Growth Media for Rhodosporidium toruloides: Complex Medium: Rhodosporidium toruloides (ATCC number 10788) was cultured in a medium containing malt extract (1.0%), yeast extract (0.10%) and L-phenylalanine (0.10%) in deionized water. Difco certified Bacto-malt and Bacto-yeast extract were used. A solution of malt and yeast extract was autoclaved without phenylalanine. An aliquot (50 mL) of a filter-sterilized 2% solution of phenylalanine was added to the 1.0 L autoclaved malt and yeast extract solution. (Abell et al., "Phenylalanine Ammonia-lyase from Yeast Rhodotorula glutinis", Methods Enzymol. 142:242-248 (1987)). Minimal Medium: The medium contained 50 mM potassium phosphate buffer (pH 6.2), MgSO 4 (100 mg/L), biotin (10 mg/L) and L-phenylalanine (2.5 g/L) in deionized water. A solution of phosphate buffer was autoclaved without the other ingredients. A solution of L-phenylalanine (25 g/L), MgSO (1.0 g/L) and biotin (0.1 g/L) in 1.0 1 of 50 mM potassium phosphate buffer (pH 6.2) was filter sterilized and 100 mL added to 900 mL of the autoclaved phosphate buffer. Final concentrations of the ingredients were: KH2PO 4 (5.55 g/L); K 2 HPO 4 (1.61 g/L) MgSO 4 (100 mg/L); biotin (10 mg/L) and L-phenylalanine (2.5 g/L) (Marusich, W. C, Jensen, R. A. and Zamir, L. O. "Induction of L-Phenylalanine Ammonia-Lyase During Utilization of Phenylalanine as a Carbon or Nitrogen Source in Rhodosporidium toruloides", J. Bacteriol. 146:1013-1019 (1981)). Enzyme activity assay: The PAL or TAL activity of the purified enzymes were measured using a spectrophotometer according to Abell et al., "Phenylalanine Ammonia-lyase from Yeast Rhodotorula glutinis," Methods Enzymol. 142:242-248 (1987). The spectrophotometric assay for PAL determination was initiated by the addition of the enzyme to a solution containing 1.0 mM L-phenylalanine and 50 mM Tris-HCl (pH 8.5). The reaction was then followed by monitoring the absorbance of the product, cinnamic acid, at 290 nm using a molar extinction coefficient of 9000 cm" 1 . The assay was run over a 5 min period using an amount of enzyme that produced absorbance changes in the range of 0.0075 to 0.018/min. One unit of activity indicated deamination of 1.0 μmol of phenylalanine to cinnamic acid per minute. The TAL activity was similarly measured using tyrosine in the reaction solution. The absorbance of the /rørα-hydroxy cinnamic acid produced was followed at 315 nm and the activity was determined using an extinction coefficient of 10,000 cm -1 for PHCA. One unit of activity indicated deamination of 1.0 μmol of tyrosine to >αr -hydroxy cinnamic acid per minute. SDS Gel Electrophoresis: The 8-25% native PhastGels were run with 4.0 μg of protein per lane and stained with Coomassie blue. Pharmacia High Molecular Weight (HMW) markers and grade I PAL from Sigma were used as standards. Sample Preparation for HPLC Analysis: An HPLC assay was developed for measuring the levels of cinnamic acid and PHCA formed by the whole cells. In a typical assay, following centrifugation of a culture grown in the medium of choice, 20-1000 μL of the supernatant was acidified with phosphoric acid, filtered through a 0.2 or 0.45 micron filter and analyzed by the HPLC to determine the concentration of PHCA and cinnamic acid in the growth medium. Alternatively, following centrifugation, the cells were resuspended in 100 mM Tris-HCl (pH 8.5) containing 1.0 mM tyrosine or 1.0 mM phenylalanine and incubated at room temperature for 1.0-16 h. A filtered aliquot (20-1000 μL) of this suspension was then analyzed. The HPLC Method: A Hewlett Packard 1090M HPLC system with an auto sampler and a diode array UV/vis detector was used with a reverse-phase Zorbax SB-C8 column (4.6 mm x 250 mm) supplied by MAC-MOD Analytical Inc. Flow rate of 1.0 mL per min, at column temperature of 40 °C was carried out. The UV detector was set to monitor the eluant at 250, 230, 270, 290 and 310 nm wavelengths. Solvents/Gradients: Time (min) Solvent A Solvent B Methanol 0.2% TFA 0.0 10% 90% 0.1 10% 90% 9.0 35% 65% 9.1 50% 50% 14.0 50% 50% 18.0 0% 0% 21.0 0% 0% Retention time (RT) of related metabolites using the HPLC system described above are summarized below. Compounds (1.0 mM) RT (min) 1. tyrosine 6.7 2. phenylalanine 9.4 3. 4-hydroxybenzoic acid (PHBA) 11.6 4. 3, 4-dihydroxy cinnamate (caffeic acid) 12.5 5. 3-(4-hydroxyphenyl)propionate 13.3 6. 4-hydroxyphenylpyruvate 13.6 7. 4-hydroxyacetaphenone 14.0 8. 4-hydroxycinnamic acid (PHCA) 14.2 9. 2-hydroxycinnamic acid (OHCA) 15.3 10. benzoic acid 15.5 11. coumarin 16.0 12. cinnamyl alcohol 17.3 13. pheny lpyruvate 18.1 14. cinnamic acid 18.3 MONO O buffer: The buffer used for these analyses was a 50 mM potassium phosphate, pH 7.0, as the starting buffer followed by a 400 mM potassium phosphate buffer, pH 7.2 as eluent for the Mono-Q column. EXAMPLE 1 Microorganisms for Conversion of Cinnamic Acid to PHCA Example 1 describes screening of various microorganisms for the presence of cinnamate hydroxy lases and investigation of their ability to convert cinnamic acid to PHCA. In order to discover microorganisms with cinnamate hydroxylase activity, over 150 different strains of bacteria and fungi were screened for their ability to convert cinnamic acid to PHCA. A two-stage fermentation protocol was used. Microorganisms were first grown in the medium for three days and then a 20% inoculum was used to start the second stage cultures. Following 24 h growth in stage two, cinnamic acid was added, samples were taken at intervals and analyzed by HPLC for the presence of PHCA. Growth Media: ATCC medium # 196 - yeast/malt medium This medium contained (in grams per liter): malt extract, 6.0; maltose, 1.8; dextrose, 6.0; and yeast extract, 1.2. The pH was adjusted to 7.0. ATCC medium # 5 - sporulation broth This medium contained (in grams per liter): yeast extract, 1.0; beef extract, 1.0; tryptone, 2.0; and glucose, 10.0. Soybean flour/glycerol medium (SBG-): This medium contained (in grams per liter): glycerol, 20; yeast extract, 5.0; soybean flour, 5.0; sodium chloride, 5.0; potassium phosphate dibasic, 5.0. The pH was adjusted to 7.0. Potato-dextrose/veast medium (PDY): This medium which contained (in grams per liter): potato dextrose broth, 24.0; yeast extract, 5.0; was used for growth of fungal strains. Of the 100-150 microorganisms tested, three separate strains of Streptomyces griseus (ATCC 13273, ATCC 13968, TU6), the bacterium Rhodococcus erythropolis (ATCC 4277), and the fungal strains, Aspergillus petrakii (ATCC 12337), Aspergillus niger (ATCC 10549) and Arthrobotrys robusta (ATCC 11856) demonstrated the ability to convert ciimamic acid to PHCA. The results indicated that Streptomycetes, in general, and Streptomyces griseus, in particular, appeared to be most active in this hydroxylation. Further studies were therefore performed using the following strains of Streptomyces griseus (ATCC 13273, ATCC 13968, TU6). The ability of the Streptomyces griseus strains to />αrø-hydroxylate cinnamic acid to PHCA while growing in three complex media (SBG, sporulation broth and yeast/malt media) was examined. The two stage fermentation protocol with SBG, sporulation broth and malt/yeast media was used. Samples were taken at various time intervals and analyzed by HPLC for the presence of PHCA. Data is shown below in Table 1. TABLE 1 Effect of Different Media on the Ability of Various Strains of Streptomyces sriseus to Convert Cinnamic Acid to PHCA Strain 13273: PHCA Production (μM) malt/veast SBG sporulation broth 4 h 0.93 116.81 2.75 18 h 0 360.75 14.31 24 h 5.36 407.27 12.14 42 h 0 350.08 7.26 60 h 0 363.94 9.79 1/11071 1/USUU/_115- Strain TU6: PHCA Production (μM) malt/yeast SBG sporulation broth 4 h 0 2.54 0.62 18 h 0 20.76 0.64 24 h 1.23 22.23 0.54 42 h 0.93 30.46 0.95 60 h 1.24 50.82 1.84 Strain 13968: PHCA Production (μM) malt/yeast SBG sporulation broth 4 h 0 2.92 41.82 18h 0 6.02 267.38 24h 0 20.55 282.29 42 h 0 127.25 177.44 60 h 0 172.78 160.71 As is seen by the data, among Streptomyces griseus strains tested, ATCC 13273 followed by ATCC 13968 and TU6 were the most active in producing PHCA when grown in the SBG medium. With ATCC 13968 strain of Streptomyces griseus growth in both SBG and sporulation broth resulted in the ability to convert cinnamic acid to PHCA. Cells (ATCC 13968) grown on sporulation medium showed the highest ability to produce PHCA after 24 h of growth while those grown on SGB medium reached their maximum PHCA producing activity after 60 h. EXAMPLE 2 Screening of Microorganisms Containing Optimal TAL/PAL Activity Ratio Example 2 describes the screening of various microorganisms for their PAL and TAL activities. This information was required to allow for selection of the most suitable microbe for further cloning, expression, purification and kinetic analysis of the PAL and PAL/TAL enzyme. Medium for growth and induction of PAL in Streptomyces: A two stage fermentation protocol was used for Streptomyces. Stage I medium contained, glucose (2%); soybean flour (1%); yeast extract (0.5%); meat extract (0.3%); calcium carbonate (0.3%); used 4% inoculum for stage II. Stage II medium contained, glucose (2%); yeast extract (2%); sodium chloride (0.5%); calcium carbonate (0.3%). The medium was distributed at 100 mL portions into 500 mL flasks. Cells transferred to this medium were incubated for 24 h at 25 °C on a shaker. Preparation of cells of Rhodosporidium toruloides following growth in the Complex Medium: In order to determine the growth yield and PAL/TAL specific activity Rhodosporidium toruloides cells were grown in 50 mL (in 250 mL capacity DeLong flasks) of complex medium. The yield (wet weight of cells) was 8.11 grams. The second transfer was made into 200 mL (in 10 x one liter DeLong flasks) using 0.8 g (wet weight) from the initial harvest. The yield was 16.0 grams after 3 washes with 100 mM phosphate buffer (pH 7.1 ). Preparation of cell extracts: The cell pellet was resuspended with 0.5 mL/g cells, 50 mM Tris-HCl buffer (pH 8.5) and disrupted by a single passage through the French Pressure Cell at 20,000 psi. The disrupted cells were then centrifuged for 30 min at 14,200 x g to remove the unbroken cell mass. Samples of the extract were used for protein concentration assay and the PAL/TAL activity determination. Protein determination was performed by the BCA (bicinchoninic acid) method from Pierce Co. Gels: Precast 7.5% acrylamide gels from BioRad (Cambridge, MA) were used. Cell extracts or samples of enzyme solutions were loaded on the gel along with molecular weight standards were from Pharmacia (Upsula, Sweden). The High Molecular Weight (HMW) lyophilized proteins were solubilized in 100 μL of 50 mM Tris-HCl pH 8.5 and bromophenol blue was added. The running buffer from BioRad was prepared from a 1 Ox solution and the gels were run at 150 volts. The running dye was electrophoresed off the gel, the gels were run for an additional 1 h. One end of the gels containing the molecular weight marker and the sample lanes was cut off and stained with Coomassie blue for approximately 45 min. Two sections of the gel were cut out and the gel material cut up and placed into 1.0-2.0 mL of 50 mM Tris-HCl buffer pH 8.5 at 4 °C. PAL activity was then measured at two different time intervals. The gel slices contained a maximum of 173 mU of PAL activity, determined as described above. PAL/TAL Activity: The PAL/TAL activity was determined as described above. Using this procedure, specific activities of 0.0241 ± 0.0005 U/mg and 0.0143 ± 0.0005 U/mg were observed for PAL and TAL, respectively (Table 2). Based on these results, the ratio of PAL/TAL was calculated to be 1.68 ± 0.07. A PAL/TAL ratio of 2.12 was observed for the purified enzyme. A literature value of 1.7 has been reported for these enzymes (Hanson and Havir In The Biochemistry of Plants; Academic: New York, 1981; Vol. 7, pp 577-625). The complete data is shown in Table 2. TABLE 2 PAL and TAL Activity Observed in Cell Free Extracts of Various Microorganisms ATCC # Name Medium Specific Activity Ratio of PAL (U/mg) TAL (U/mg) PAL/TAL 15873 Streptomyces griseus SBG 0.0 ND ND Streptomyces griseus SBG +Phe 0.0004 ND ND Streptomyces griseus Strep. + Phe 0.0003 ND ND 13495 Streptomyces verticillat 1 0.0025 ND ND 11386 Sporidiobolus pararoseus 2 0.0158 0.0024 6.51 20804 Rhodotorula graminis 3 0.0436 0.0102 4.27 2080 Saccharomycopsis fibulige 4 0.0070 0.0016 4.27 10788 Rhodotorula glutinis 3 0.0241 0.0143 1.68 ND: not determined 1. Grown in medium in Can. J. Biochem. 48:613-622 ( 1970) at 25 °C. 2. Grown in 0.7% Difco malt extract, 0.1% Difco yeast extract and 0.1% phenylalanine at 30 °C. 3. Grown in 1% malt extract, 0.1% yeast extract and 0.1% phenylalanine medium at 30 °C. 4. Grown in 1% peptone, 1% yeast extract, 0.5% phenylalanine, 0.1% KH2PO4, 0.3% KHPO4 and 0.05% MgS0 4 -7H 2 0 at 25 °C. As outlined in Table 2, Rhodosporidium toruloides also known as Rhodotorula glutinis (ATCC 10788,) possesses the highest TAL activity and was therefore selected for further studies. EXAMPLE 3 Cloning and Expression of Rhodosporidium toruloides PAL in E. coli Example 3 describes the cloning and expression of phenylalanine ammonia lyase (PAL) from Rhodosporidium toruloides in E. coli in order to produce sufficient quantities of PAL for purification. RNA Purification: The Rhodosporidium toruloides RNA was purified from exponential phase cells grown in the complex medium containing phenylalanine. The total RNA was isolated and the mRNA was purified using Qiagen total RNA and mRNA isolation kits, respectively, according to the manufacturers instructions. Reverse Transcription: The Rhodosporidium toruloides mRNA (3 μL, 75 ng) was reversed transcribed according to Perkin Elmer (Norwich CT.) GeneAmp kit instructions without diethylpyrocarbonate (DEPC) treated water. The PCR primers used (0.75 μ M) were the random hexamers supplied with the kit, the upstream primer (SEQ ID NO:l) 5*-ATAGTAGAATTCATGGCACCCTCGCTCGACTCGA-3* containing a EcoRl restriction site, and a downstream PCR primer (SEQ ID NO:2) 5'-GAGAGACTGCAGAGAGGCAGCCAAGAACG-3' containing a Pstl restriction site. These were synthesized from the Rhodosporidium toruloides PAL gene. A positive control using the kit pAW109 RNA and the DM151 and DM152 primers was also performed. PCR was carried out for 30 cycles with a 95 °C melting temperature for 1.0 min, a 55 °C annealing temperature for 1.0 min and a 72 °C elongation temperature for 2.0 min. Five sec were added per cycle to the elongation step and a final elongation step of 10 min was used. An aliquot (5.0 μL) was taken from the PCR reaction mix and loaded onto a 1% agarose gel to verify the PCR reaction product. Digestion of PCR fragments was achieved by using lOx multibuffer (2.0 μL), bovine serum albumin (BSA, 10 mg/mL, 1.0 μL), EcoRI and Pstl (0.5 μL each), PCR product (4.0 μL) and distilled deionized water (12.5 μL). The entire reaction was loaded onto a 1% agarose gel and the desired size of the DNA fragments were purified. Ligation: The ligation mixture (total vol. 50 μL) for constructs contained: ligation buffer (lOx, 5.0 μL), 3.0 U/μL T4 DNA ligase (1.0 μL), BSA (10 mg/mL, 2.5 μL), 19 ng/μL PCR product using primers with EcoRI and Pstl restriction sites (25 μL), 33 ng/μL pKK223-3 previously cut with EcoRI and Pstl (2.0 μL) and distilled deionized water (14.5 μL). The ligation mixture (total vol. 50 μL) for the control vector contained, ligation buffer (lOx, 5.0 μL), 3.0 U/μL T4 DNA ligase (1.0 μL), BSA (10 mg/mL, 2.5 μL), 33 ng/μL pKK223-3 previously cut with EcoRI and Pstl (2.0 μL), and distilled deionized water (39.5 μL). The reaction mixtures were incubated overnight at 16 °C. Transformation: Competent DHlOb E. coli cells (Gibco) were thawed on ice for approximately 20 min. Then, 2.0 μL of the ligation mix were added to 50 μL of the cells and incubated on ice for 30 min. The cells were heat shocked for 20 sec at 37 °C and then chilled on ice again. Then, 0.95 mL of LB broth was added to the cells and incubated for 1.0 h at 37 °C on a shaker. The cells were then centrifuged, resuspended in approximately 50 μL of the LB broth and streaked on LB plates containing 100 mg/L ampicillin and incubated overnight at 37 °C. Clones: The Rhodosporidium toruloides PAL gene was over-expressed in E. coli. The PCR product, which was prepared in this example, was first cloned into a standard cloning vector and then cloned into pKK223-3 over-expression vector under the tac promoter in DHlOb E. coli. A total of six clones were tested for both whole cell and cell free PAL activity. Cell Growth: Cells were initially grown overnight, at 37 °C on 50 mL LB media with 100 mg/L ampicillin in baffled 250 mL flask. Before harvesting the non-induced 10 cells, a 5.0 mL aliquot was transferred into the fresh medium and grown to about 0.9 (OD^oo)- IPTG was then added to a final concentration of 0.2 mg/mL to induce the enzyme and the cells were further grown for 3.0 h. OD6 0 Q measurements are shown in Table 3. TABLE 3 15 Growth and PHCA Production mAU's Time Cinn. PHCA [Cinn.] [PHCA] Cinn. PHCA Medium Glucose (hr) OD^nn 270 nm 310 nm (μM) (μM) (μM/OD f inn) LB 0 24 ND 10689.27 5000.41 839.42 629.50 LB 0.2% 24 ND 12000.60 3540.89 942.40 445.76 M9 0.2% 24 0.2377 418.84 336.98 32.89 42.42 138.37 178.47 M9 2% 24 0.2079 411.03 370.11 32.28 46.59 155.26 224.11 LB 0 72 2.1010 12698.07 7942.28 997.17 999.85 474.62 475.89 LB 0.2% 72 4.2740 14038.05 8416.65 1102.40 1059.57 257.93 247.91 Cinn. 12734.13 PHCA 7943.46 Whole Cell PAL Activity: Aliquots of non-induced (1.0 mL) and induced (0.2 mL) cells were taken before harvest. The cells were pelleted and resuspended in 1.0 mL of 50 mM Tris 20 buffer pH 8.5. Phenylalanine was then added (1.0 mM, final concentration) and the mixtures were incubated on the shaker at 37 °C for 1.0 h. The mixtures were then acidified with 50 μL of phosphoric acid and the cells were pelleted. The solute was then filtered and analyzed by HPLC as described above. The culture media from the induced cells was similarly treated and analyzed by HPLC. 25 Cinnamic acid and PHCA standards (1.0 mM) were also analyzed and used to calculate the concentration of the compounds in the samples (e.g., (177.66 mAU sample)/(12734.13 mAU/mM standard)* (1000 μM/mM) = 13.95 μM cinnamic acid). Results are shown in Table 3. Cell Free PAL Activity: Cells were harvested by centrifugation. To the harvested cell pellet, 1.0 mL of 50 mM Tris buffer (pH 8.5) was added and the cells were disrupted by a single passage through the French Pressure Cell at approximately 18,000 psi. The extract was centrifuged for 10-15 min in an Ependorf Microfuge at 4 °C. The supernatant (1.0 mL) was removed and used for PAL activity and Bradford protein assays (Bradford, M., Anal. Biochem., 72, 248, 1976). The highest specific activities observed, were 0.244 (PAL) and 0.0650 (TAL) U/mg protein. SDS Gel Electrophoresis: The purified PAL protein was run on a 8-25% native PhastGel as described in General Methods. The molecular weight of the purified PAL was estimated to be 287 kD based on these analyses. During the above experiments, it was discovered that both PHCA and cinnamic acid appeared during growth of the cells in the LB medium and also during the whole cell assays. Detection of PHCA in transformed E. coli cultures was an unexpected discovery since E. coli does not contain the enzymatic machinery for conversion of cinnamic acid to PHCA. Presence of PHCA in these cultures therefore indicated that the wild type yeast PAL enzyme expressed in E. coli, in addition to its PAL activity, contained the TAL activity and directly converts tyrosine to PHCA. EXAMPLE 4 PHCA Production from Glucose by Recombinant E. coli Over-Expressing the Rhodosvoridium toruloides Wild Type PAL This Example describes analysis of the E. coli strain over-expressing the wild type PAL for its ability to produce PHCA during growth in either glucose or the LB medium. As described above, there are two pathways to synthesize PHCA. In one pathway, PHCA can be synthesized through conversion of phenylalanine by PAL to trαjw-cinnamic acid which is in turn hydroxy lated at the para position by the cytochrome P-450 enzyme system. In the other pathway, tyrosine is converted to PHCA in a single step reaction by TAL and no cytochrome P-450 is required. Since no cytochrome P-450 enzyme is present in E. coli, any PHCA formed in these cells should be through the TAL route. To confirm this hypothesis, the following experiments were carried out: E. coli cells containing PCA12Km (described in Example 8) were incubated overnight with 1.0 mM cinnamic acid, and the PHCA production was monitored by HPLC. Cell Growth: The cells were grown overnight, in LB broth, LB + 0.2% glucose with 100 mg/L ampicillin at 30 °C or in the M9 medium (see below) + 0.2% glucose or the M9 medium + 2% glucose with 100 mg/L ampicillin for 24 h at 30 °C. The cells grown in the M9 medium + glucose grew significantly more slowly than the cells in the LB medium. Assay of PHCA: An aliquot (1.0 mL) of each cell culture was acidified with 50 μL of phosphoric acid and pelleted and the supernatant was filtered and analyzed by HPLC as described in the General Methods. Samples were taken after 24 or 72 h. A PHCA standard (1.0 mM) was also analyzed and used to determine the concentration of the compound in the samples. Samples were also taken to measure the cell density at 600 nm in order to relate growth to PHCA production (see Table 3, Example 2). As can be seen from the data in Table 3, the E. coli cells containing the wild type PAL produced PHCA when grown in either the LB (with and without glucose) or M9 (see below) with glucose medium. The addition of glucose to the LB medium increased the total amount of PHCA formed and the cell density of the culture, but decreased the PHCA production per cell density. M9 medium: The M9 minimal medium for culturing bacteria contains (in gram per liter): Na 2 HPO 4 , 6.0; KH 2 PO 4 , 3.0; NH 4 C1, 1.0; NaCl, 0.5; and glucose, 4. (Maniatis, Appendix A.3). EXAMPLE 5 Purification of the Recombinant Wild Type Rhodosporidium toruloides PAL from E. coli The wild type recombinant R. toruloides ^ PAL from transformed E. coli was purified using heat treatment, ammonium sulfate precipitation, anion exchange column, and hydrophobic interaction chromatography and gel filtration. Cell Growth: The cells were grown in a 10-L fermenter at 28 °C on 2x YT medium with 100 mg/L ampicillin. Preparation of Cell Free Extracts: The cells were harvested and kept as a frozen pellet until required for use. The pellet (76 g wet weight) was washed with 50 mM Tris-HCl pH 8.5 and resuspended with the same buffer to a density of 2.0 g wet weight of cells per 1.0 mL of buffer. A small amount of DNase was added and the cells were passed twice through a French Pressure Cell at approximately 18,000 psi. The protease inhibitor, PMSF, was then added to the extract to a final concentration of 0.5 mM. The cell debris was removed by centrifugation at 13,000 x g for 30 min followed by another centrifugation at 105,000 x g for 1.0 h. Heat Treatment of Extract: The extracts were heated to a temperature of 60 °C for 10 min and then placed on ice. The denatured proteins were pelleted by centrifugation at 25,000 x g for 30 min. Ammonium Sulfate Precipitation: Ammonium sulfate precipitation was achieved by addition of saturated solutions of ammomum sulfate at 4 °C. The solution was stirred on ice for 15-30 min. The precipitated protein was pelleted by centrifugation at 25,000 x g for 15 min and the pellet dissolved in a minimal amount of Tris buffer. During the 35% ammonium sulfate cut, the pH of the solution was measured and adjusted back to 8.5. The volume of the extract was measured after each precipitation. The extracts were ammonium sulfate precipitated separately, but the 50% ammonium sulfate cuts from both runs were pooled, concentrated and desalted with Centricon-50 ultrafiltration tubes (Milipore, Bedford, MA). Anion Exchange Chromatographv: Anion exchange chromatography was carried out on a 20 mm x 165 mm, 50 μm HQ column (Perseptive Biosystems, Farmingham, MA) at a flow of 30 mL/min. The starting buffer (buffer A) was 5 mM Tris-HCl pH 8.5 and the eluting buffer (buffer B) was 0.5 M NaCl in 5.0 mM Tris-HCl pH 8.5. The column was equilibrated for two column volumes (CV) and washed for two CV with buffer A after sample injection. A gradient was run from 100% of buffer A to 50% of buffer A and buffer B over 10 CV. A second gradient was then run from 50% of buffer A and buffer B to 100% of buffer B over two CV. The column was washed with two CV of buffer B and then re-equilibrated with buffer A for two CV. Protein was monitored at 280 nm and 10 ml fractions were collected on ice during the first gradient. The sample size was up to 5.0 ml and contained up to 340 mg of protein or approximately 12% of the column's capacity of 2850 mg. Fractions from the different runs were pooled and concentrated as indicated above. Hvdrophobic Interaction Chromatographv: Hydrophobic interaction chromatography was carried out on a 20 mm x 167 mm, 50 μm PE column (Perseptive Biosystems, Farmingham, MA) at a flow rate of 30 mL/min. The starting buffer (buffer A) was 1.0 M (NH ) 2 SO in 5.0 mM Tris-HCl pH 8.5 and the eluting buffer (buffer B) was 5.0 mM Tris-HCl pH 8.5. The column was equilibrated for two CV and washed for two CV with buffer A after sample injection. A gradient was then run from 100% of buffer A to 100% of buffer B over 10 CV. The column was cleaned with 2 CV of buffer B and then re-equilibrated with buffer A for two CV. Protein was monitored at 280 nm and 10 mL fractions were collected and kept on ice during the gradient. Samples, up to 5.0 mL and containing up to 50 mg of protein or 12% of the column's capacity of 420 mg, were adjusted to 1.0 M (NH ) 2 SO by the addition of a saturated ammonium sulfate solution. Fractions from different runs were pooled, desalted and concentrated as indicated above. Gel Filtration Chromatography (GF : Gel filtration was carried out on a 10 mm x 305 mm, Superdex 200 HR column at a flow rate of 0.5 mL/min. Using a 50 mM Tris-HCl buffer (pH 8.5) containing 0.2 M NaCl, a column was run for one CV and protein elution monitored at 280 nm. Fractions (0.5 mL) were collected and kept on ice. The volume of the sample applied to the column was 100 μL and contained up to 10 mg of protein. The fractions from the center of the peaks were pooled and concentrated as described above. Data describing the purification and increase in specific activity are shown in Table 4. TABLE 4 Purification of PAL from E. coli Total PAL Total Specific Vol. Protein Protein Activity Activity Activity Yield Purif. Step (mL (mg/mL) (mg) (U/mL) (Units) (U/mg) (%) (Fold) ) Crude 70 77.4 5415 13.62 953.6 0.176 100% 1.00 Extract 43 52.0 2237 14.95 642.8 0.287 67% 1.63 Heat Treatment 22.2 55.6 1235 54.7 1213.6 0.982 127% 5.58 Am. Sulf. PPT 15.0 12.7 190.2 55.63 834.4 4.387 88% 24.92 Anion Exchange 5.8 15.1 88 113.75 659.7 7.530 69% 42.76 HIC 4.4 8.9 39 54.77 241.0 6.143 25% 34.89 Gel Filtration 1.6 6.6 11 31.47 50.3 4.774 5% 27.11 GF Ends EXAMPLE 6 Carbon Source Selection This example describes the effect of various carbon sources on the ability of the recombinant Saccharomyces cerevisiae strain (PTA 408) containing the Rhodosporidium toruloides PAL gene (SEQ ID NO:7) plus the plant P-450 and the P-450 reductase (SEQ ID NO: 11 and SEQ ID NO: 13 respectively) to convert phenylalanine to PHCA. Two colonies (#1 and #2) from the Saccharomyces cerevisiae containing the yeast PAL and the plant cytochrome P-450 and the cytochrome P-450 reductase were chosen and grown on three different media containing either raffinose, galactose or glucose. The media were identified as Raf SCM or Gal/SCM or Glu SCM. The formulation of various media used in these experiments is indicated below: Glu/SCM (Ade/His/Ura) contained: Bacto-yeast nitrogen base (6.7 g/L); glucose, (20.0 g/L); and SCM, (2.0 g/L). Raf/SCM(Ade/His/Ura) contained: Bacto-yeast nitrogen base, (6.7 g/L); raffinose, (20.0 g/L); and SCM, (2.0 g/L). Raf Gal SCM (Ade/His/Ura)/Tyr/Phe contained: Bacto-yeast nitrogen base, (6.7 g/L); raffinose, (10.0 g/L); galactose, (10.0 g/L); SCM, (2.0 g/L); tyrosine, (0.5 g/L); and phenyalanine, (10.0 g/L). SCM (Ade/His/Ura) agar plate for yeast contained: Bacto-yeast nitrogen base, (3.35 g/L); dextrose, (10.0 g/L); agar, (10.0 g/L); SCM, (1.0 g/L); and ddH 2 O, (500 mL). Glycerol stocks (300 μL) of each of the colonies were used to inoculate the Glu/SCM, Gal/SCM and Raf/SCM media. Duplicate cultures were prepared with each strain and each medium and cultures were grown for 24 and 48 h. The cell density was measured as described above and the cells were then centrifuged, washed once with 0.85% saline phosphate buffer, resuspended in the SCM medium (5.0 mL) and the ODgoo was measured again. The cells were then added to the corresponding flasks which contained either 25.0 mL of the Raf SCM or the Gal/SCM medium to the final OD^QO of 0.5. Galactose (5% final concentration) was added to each flask and left on the shaker for about 16 h to allow for induction. Following induction, phenylalanine (1.0 mM final concentration) was added to each flask and samples (1.0 mL) were taken from each flask at 2, 4, 6, 24 and 48 h and analyzed by HPLC for the presence of PHCA (see Table 5). TABLE 5 Strain #1 PHCA Production (μM) after Addition of 1.0 mM Phenylalanine Carbon Source 2 h 4 h 6 h 24 h 48 h raffinose 116.28 125.43 165.34 270.15 99.85 galactose 95.54 164.71 183.51 231.25 97.56 glucose 57.42 128.04 170.18 269.62 91.71 Strain #2 PHCA Production (μM) after Addition of 1.0 mM Phenylalanine Carbon Source 2 h 4 h 6 h 24 h 48 h raffinose 145.95 188.06 218.45 293.54 116.7 galactose 150.85 171.07 196.26 230.95 103.09 glucose 75.71 179.52 161.1 238.77 78.65 As is seen by the data in Table 5, both strains tested appeared to behave similarly when grown in different media. The highest level of production of PHCA was observed between 6-24 h and around 30% of the phenylalanine was converted to PHCA. Following the initial appearance and accumulation, a decrease in the concentration of the PHCA was observed (48 h). EXAMPLE 7 Production of PHCA by Recombinant Saccharomyces cerevisiae Strain Containing the Rhodosporidium toruloides PAL, the Plant Cytochrome P-450 and the Cytochrome P-450 Reductase This example describes induction by galactose for production of PHCA by a recombinant Saccharomyces cerevisiae strain that contains the wild type PAL plus the plant cytochrome P-450 and the cytochrome P-450 reductase genes. Since PAL, the cytochrome P-450 and the cytochrome P-450 reductase that had been incorporated into the Saccharomyces cerevisiae strain, were under the control of the galactose promoter, experiments were performed in order to examine the effect of the length of induction by galactose on the level of PHCA formed. Saccharomyces cerevisiae strain #2, which had produced the highest level of PHCA, was chosen and induced by galactose. In order to examine if the recombinant Saccharomyces cerevisiae could directly convert glucose to PHCA, one set of cells, after one h induction with galactose, received glucose but no phenylalanine was added. Another set of cells was grown on raffinose. Samples were taken from all flasks at intervals and prepared for HPLC analysis as described above. A sample of the glycerol suspension of Saccharomyces cerevisiae was streaked on an SCM-glucose plate and incubated at 30 °C. Four colonies were picked from the plate, inoculated into 4.0 mL of Glu/SCM medium left on the shaker (30 °C, 250 rpm) overnight. One mL of the cell suspension was taken and the ODgoo measured. After 24 h of growth, when the OD 60Q was around 1.4 to 1.6, cells (1.0 mL) were transferred to 25 mL of Glu/SCM medium or 50 mL of Raf SCM medium. Following overnight growth (30 °C, 250 rpm) samples (1.0 mL) were taken from each flask and the OD 6Q O measured. ODeoo 1. # 1 in RafVSCM medium 0.3775 2. # 1 in Glu/SCM medium 1.5119 3. # 2 in Raf/SCM medium 0.4730 4. # 2 in Glu SCM medium 1.4923 As can be seen from the OD data, higher cell mass was obtained after growth on glucose compared to raffinose. In order to examine if the recombinant Saccharomyces cerevisiae could directly convert glucose to PHCA without additional phenylalanine an experiment was set up in which following growth on glucose or raffinose, cells were induced by galactose prior to glucose addition. Samples were taken at intervals and prepared for HPLC analysis as described above. Data is shown in Table 6. TABLE 6 Effect of Growth on Glucose Versus Raffinose on PHCA Production by Saccharomyces cerevisiae Containing PAL + P-450 + P-450 Reductase (induced by galactose) Recombinant Saccharomyces cerevisiae grown on glucose: PHCA production (μM) Incubation Time Induction 1.0 h Induction 3.0 h Induction 6.0 h 2.0 h 0.33 1.37 4.58 4.0 h 0.57 2.62 N/A 6.0 h 0.48 3.33 N/A 24 h 0.98 7.63 14.59 48 h 2.14 6.64 14.25 Recombinant Saccharomyces cerevisiae grown on raffinose PHCA production (μM) Incubation Time Induction 1.0 h Induction . ' 3.0 h Induction 6.0 h 2.0 h 7.11 30.72 62.73 4.0 h 9.33 45.49 N/A 6.0 h 12.55 55.88 N/A 24 h 28.49 112.37 202.77 48 h 38.63 110.85 193.63 As shown in the data in Table 6, while growth in the medium containing glucose produced higher cell mass, the amount of PHCA formed was much higher following growth in the presence of raffinose (approximately 200 μM PHCA within 24 h following growth in raffinose versus approximately 14.5 μM following growth in glucose). This underlines the inhibitory effect of glucose on the galactose inducible promoter. In another experiment, the effect of addition of phenylalanine to the growth medium containing either glucose or raffinose was determined. Samples (10 mL) from each flask were transferred into a 125 mL capacity flask containing 25 mL of medium and cells were induced by galactose (2% final concentration). The induction was allowed for 1.0, 3.0, 6.0 h and overnight. After the specified induction time, phenylalanine (1.0 mM) was added to each flask and formation of PHCA was measured. Results are summarized in Table 7 below. TABLE 7 Effect of Addition of Phenylalanine on PHCA Production by Saccharomyces cerevisiae Containing PAL + P-450 + P-450 Reductase During Growth on Glucose Versus Raffinose (induced by galactose) PHCA Production (μ ) after Addition of 1.0 mM Phenylalanine Induction Carbon Time Source 2.0 h 4.0 h 6.0 h 24 h 48 h 54 h 1.0 h raffinose 9.33 45.05 57.69 475.62 531.25 554.46 glucose 1.65 7.01 5.99 172.04 233.97 230.24 3.0 h raffinose 37.66 72.44 155.16 459.99 536.54 545.29 glucose 4.14 4.86 18.55 212.02 318.62 342.95 6.0 h raffinose 142.02 N/A N/A 454.71 539.33 537.62 glucose 25.21 N/A N/A 235.42 369.9 372.24 overnight raffinose 11.56 208.11 260.46 497.97 424.28 408.32 glucose 9.87 10.13 36.74 354.15 424.89 398.81 As depicted in Table 7 and as expected, addition of phenylalanine to both cultures resulted in production of higher levels of PHCA compared to those produced in the absence of additional phenylalanine. Generally cells grown on raffinose produced higher amounts of PHCA from phenylalanine compared to those grown on glucose. The average level of PHCA produced from phenylalanine by cells growing on raffinose was around 500 μM and the highest level of PHCA was formed at around 24 h. In most cases, the level of PHCA reached a maximum at or around 24 h and remained without significant changes until the end of the experiment (approximately 54 h). Duration of induction (i.e., 1.0, 3.0, 6.0 h and overnight) did not seem to make a significant difference in the level of PHCA production. The level of PHCA formed in cultures growing on glucose was around 300 μM. While the total amount of PHCA formed by glucose-grown cells was less than that produced by cells grown on raffinose, the pattern of production of PHCA was similar. In summary, the recombinant Saccharomyces cerevisiae cells containing the Rhodosporidium toruloides wild type PAL plus the plant cytochrome P-450 and the cytochrome P-450 reductase had the ability to convert glucose directly, in the absence of additional phenylalanine, to PHCA (approximately 25% conversion). When phenylalanine was added around 50% was converted to PHCA. EXAMPLE 8 Development of a Selection System for Identification of the Mutant PAL (PAL/TAL) Enzyme This example describes a method for selection of the mutant PAL enzyme with improved TAL activity. There are currently no engineered enzymes that can efficiently catalyze the conversion of tyrosine directly to PHCA with no intermediate step. In this reaction, the enzyme converts tyrosine to PHCA and ammonia while in the reverse reaction the same enzyme converts PHCA and ammonia to tyrosine. In order to detect mutant PAL enzymes able to convert tyrosine to PHCA, the following screen was developed. Constructing the expression vector (PCA12Km): A weak expression vector was made by modifying the commercially available pBR322 vector. Briefly, pBR322 was digested with Pst I and subjected to 20 cycles of PCR with two primers, pBRl (SEQ ID NO:3) 5'-GAGAGACTCGAGCCCGGGAGATCTCAGACCAAGTTTACTCATATA-3' and pBR2 (SEQ ID NO:4) 5'-GAGAGACTCGAGCTGCAGTCTAGAACTCTTTTTTCAATATTATTG-3'. The PCR reaction product was extracted with phenol chloroform, EtOH precipitated and digested with Xho I. The Xho I digested product was then gel isolated, ligated and transformed into E. coli selecting for tetracycline resistance. This vector is therefore a pBR322 lacking the ampicillin resistance gene but containing the beta-lactamase promoter and the following restriction sites: Xba I, Pst I, Xho I, Sma I, Bgl II. The tetracycline-resistance gene in pBR322 was replaced by the kanamycin-resistance gene. Tetracycline resistant gene was cut out of pCA12 (Figure 1) at EcoR V (185) and Nru 1 (972) sites, the ends were polished by using pfu polymerase (PCR polishing kit, Stratagene) and ligated with the blunt-ended 9 kb kanamycin resistant gene fragment (V ieira and Messing, Gene 19:259-268 (1982)). Final construction was selected on the LB/km plates after transformation of the ligation in to the XL 1 -Blue vector (Figure 1). Subcloning the Rhodosporidium toruloides PAL gene into PCA12Km: The gene sequence of yeast (Rhodosporidium toruloides) PAL has been determined and published (Anson et al., Gene 58:189-199 (1987)). Based on the published sequence, the gene was subcloned into a pBR322-based vector. The entire PAL gene was then removed from the plasmid by Xbal-Pstl digestion, and the gene was ligated into the _Ω>αI -Pstl-digested PCA12Km. The new construct containing the PAL gene was designated PCA18Km. Expression of the PAL enzyme in the tyrosine-auxotrophic E. coli: The PCA12Km and PCA18Km were transformed into the tyrosine- auxotrophic E. coli strain AT2471 and the TAL and PAL activities were measured using the whole cell assay. Formation of small quantities of PHCA or cinnamic acid were detected following incubation of these cells with tyrosine or phenylalanine (Table 8). TABLE 8 PHCA and Cinnamic Acid Formation from Tyrosine and Phenylalanine. Respectively* PHCA (μM) cinnamic acid (μM) Cells containing PCA12Km 0 0 Cells containing PCA18Km 10.8 38 *The cells were incubated with 1.0 mM tyrosine or phenylalanine for 1.0 h, and the PHCA or cinnamic acid formation was detected by HPLC (see general methods). As seen in Table 8, the yeast PAL enzyme was weakly expressed in the tyrosine-auxotrophic E. coli strain AT2471 containing the PCA18Km vector. Determination of selection condition (Development of a selection system): The tyrosine-auxotrophic E. coli strain AT2471 containing pCA18Km showed the same tyrosine-auxotrophic property as the original strain. The cells did not grow on the minimal plate, but grew well when 0.004 mM tyrosine was added to the plate. In order to find the sviitable condition for selection, cell growth was tested on a minimal plate containing various concentrations of tyrosine or PHCA (see Table 9). TABLE 9 Tyrosine-Auxotrophic E. coli Cell Growth Under Various Concentrations of Tyrosine or PHCA Tyrosine* PHCA** 0.0001-0.0002 mM - +++ 0.0003-0.0005 mM 0.001-0.004 mM ++ 1.0-2.0 mM 4.0-6.0 mM 10 mM No PHCA was added in the growth medium for testing the tyrosine-auxotrophic property. ** 0.004 mM tyrosine was added in the growth medium for testing the toxicity of PHCA. -: no growth; +: very poor growth; ++: poor growth; +++: good growth. The results shown in Table 9 indicate that high concentrations of PHCA are toxic to the cells. The 2.0 mM PHCA concentration was chosen for the selection experiment. The information about the cell growth at different tyrosine concentrations is important for the selection. For example, when the tyrosine made from PHCA by the cell is not enough to support cell growth, small amounts of tyrosine (0.0001-0.0002 mM) can be added to the plate. This will allow identification of strains expressing the enzyme with slightly improved TAL activity. In other words, the selection stringency can be modulated by changing the concentration of PHCA and tyrosine in the selection plate. EXAMPLE 9 Engineering the Mutant PAL Enzyme with Improved TAL Activity Error-Prone PCR: The following primers were used for amplifying the entire PAL gene from PCA18Km construct: Primer A (SEQ ID NO:5): 5'-TAGCTCTAGAATGGCACCCTCG-3 * Primer B (SEQ ID NO:6): 5'-AACTGCAGCTAAGCGAGCATC-3*. The primer A (forward primer) contained a.Xba I restriction enzyme site just before the ATG codon, and primer B (reverse primer) had a Pst I site just after the stop codon. To increase the rate of the PCR error, plain Taq polymerase and more reaction cycles (35 cycles) were used. In addition, the ratio of dATP, dTTP, dGTP and dCTP was changed. Four different reactions were performed. In each reaction, the concentration of one of the dNTP's was 0.1 mM, and the other three dNTP were adjusted to 0.4 mM. The PCR products from four reactions were mixed together following completion of the reaction. After digestion of the error- prone PCR products with Xba I and Pst I, fragments were ligated into the _ΫbαI-P_tI-digested PCA12Km. In vivo mutagenesis using E. coliXLl-Ked strain: The PCAlδKm was transformed into the XL 1 -Red strain, and the cells were grown overnight in the LB medium plus kanamycin. To increase the mutation rate, the cells were diluted with fresh growth medium, and grown further. After 2-4 cell generation cycles, the plasmids were purified, and used for selection. Selection: After mutagenesis, the pool of mutated PCAlδKm containing the randomly mutated PAL gene were transformed into the tyrosine-auxotrophic E. coli strain by electroporation. The transformation efficiency was 1.5 x 10 8 cfu/μg DNA. The cells were then incubated in the LB medium with antibiotics for more than 5.0 h. After washing with the minimal medium, the cells were streaked on plates containing the minimal medium supplemented with 0.0002 mM tyrosine and 2.0 mM PHCA. After 3.0-5.0 days of incubation at 30 °C, 1.0-10 colonies appeared on each plate. The colonies that had appeared on the selection plates were analyzed for their PAL/TAL activity using the whole cell assay described in the general methods. One of the mutants, designated ΕP18Km-6, showed an enhanced TAL activity ratio than the wild type cell. Genetic analysis for the EP18Km-6 mutant was carried out. The plasmid DNA was purified from the mutant cells, and then re-transformed into E. coli. The new transformant showed the same enhanced TAL ratio as the original mutant, indicating that all mutations that involved improvement of TAL activity were on the plasmid. To better characterize the mutants, the following analyses were carried out. EXAMPLE 10 Characterization of the Mutant PAL Enzyme Sequence analysis of the mutant gene: The entire gene of EP18Km-6 was sequenced on an ABI 377 automated sequencer (Applied Biosystems, Foster City, CA), and the data managed using DNAstar program (DNASTAR Inc., Madison, WI). Analysis of the resulting PAL mutants followed by comparison with the wild type gene (SEQ ID NO:7), indicated that the mutant gene (SEQ ID NO:9) contained the following four single base substitution mutations (point mutations): CTG (Leu215) to CTC, GAA (Glu264) to GAG, GCT (Ala286) to GCA and ATC (Ile540) to ACC. The first three mutations were at the third base, generating silent mutations which did not result in any amino acid change. The fourth mutation was a second base change (ATC to ACC). This mutation changed the isoleucine-540, which is in the conserved region of the enzyme, to a threonine. Various PAL enzymes from different sources have either isoleucine or leucine at this critical position. Over-expression and purification of EP18Km-6 mutant enzyme: In order to obtain sufficient quantities of the pure enzyme for enzymatic kinetics analysis, the enzyme was expressed in the over-expression vector, pET-24-d. The pET-24-d vector was digested with EcoRI, and the digestion product was filled-in using the Klenow enzyme (Promega, Madison, WI) according to the manufacturer's instructions. The linearized vector was then digested with Nhel and the mutant PAL gene was obtained by cutting the EP18Km-6 with_¥bαl and Smal. Since the Nhel and Xbal are compatible sites, the mutant gene was subcloned into the pET24-d vector by ligation in order to prepare the pETAL construct (Figure 2). Although the pET-24-d vector carries an N-terminal T7 Tag sequence plus an optional C-terminal HisTag sequence, these Tags were not used so that the enzymes could be expressed with natural sequences at both N- and C-termini. After cloning the mutant gene into the pET-24-d vector, the construct was transformed into E. coli BL21(DE3). For over-expression, the cells were grown in the LB medium containing kanamycin to an ODgoo of 1.0 before 1.0 mM IPTG was added. After 4.0 h of induction, cells were harvested by centrifugation and the crude extracts prepared as described in the General Methods section. The SDS-PAGE analysis of the crude extracts revealed that the expressed enzyme was the dominant protein band, and the expression level was estimated to be 10-15% of total protein (Figure 3). Figure 3 shows the SDS-PAGE of purified mutant PAL enzyme (lane A) and the cell crude extracts (lane B) which has been used as the starting materials for purification. Lane C is the standard marker of molecular weight (94, 67, 43, 30, 20 and 14 kDa from top to bottom). For purification of PAL, the cell pellet was suspended in 10 mM potassium phosphate buffer, pH 6.6, containing protease inhibitors PMSF, amino caproic acid and benzamidine (1.0 mM, each). The cells were broken by sonication (Branson model 185, 70% power setting, 4 min in ice bath), followed by centrifugation (30,000 x g, 30 min). The clear supernatant was applied to a Mono-Q HPLC column (flow rate of 1.0 mL/min). The column was started using a 50 mM potassium phosphate buffer, pH 7.0, followed by a 400 mM potassium phosphate buffer, pH 7.2 as the elution buffer. The enzyme was eluted at a concentration of approximately 90 mM potassium phosphate. The active fractions were pooled and concentrated using Centricon YM100 (Milipore, Bedford, MA). The enzyme was >98% pure as judged by the SDS-PAGE electrophoresis (Figure 3). Biochemical characterization of mutant PAL enzyme: A detailed enzyme kinetics analysis using the yeast wild type and the purified mutant PAL enzyme and tyrosine or phenylalanine as substrate, was carried out. The PAL and TAL activities were measured spectrophotometrically as described in the General Methods and the K M and V max were determined from its Lineweaver-Burke plot. The kc at was calculated from V max assuming the presence of four active sites in the active tetramer. The determined __M and k^ of the enzymes are shown in Table 10. TABLE 10 ^M and k cat of wild type and mutant PAL Enzyme K M (mM) k C at ( sec_1 ) WT (Phe)* 0.250 2.09 WT (Tyr)** 0.111 0.46 Mutant (Phe)* 0.333 2.45 Mutant (Tyr)** 0.05 0.63 ♦ Phenylalanine was used as substrate. **Tyrosine was used as substrate. The catalytic efficiency, defined as k cat / M , was calculated for both the wild type and mutant enzyme. The ratio of the TAL catalytic efficiency versus the PAL of the wild type enzyme was 0.5 while that of the mutant enzymes had increased to 1.7 (see Table 11). The results showed that unlike the wild type PAL enzyme which preferred to use phenylalanine, the mutant enzyme preferred to use tyrosine as substrate thereby clearly demonstrating that the substrate specificity of the yeast PAL enzyme had changed after mutagenesis and selection. TABLE 11 Catalytic Efficiency* and TAL/PAL Ratio Comparison Between Wild Type and Mutant PAL Enzyme FALQ^^K f), M^sec' 1 * TAL(k cat /Λ M ), M^sec' 1 ** TAL/PAL ratio Wild type 8.36 x l0 3 4.14 x l0 3 0.5 Mutant 7.36 x lO 3 12.61 x 10 3 1.7 ""Phenylalanine was used as substrate **Tyrosine was used as substrate 1 catalytic efficiency is defined as k^t/ ^ EXAMPLE 11 Bioproduction of PHCA from Glucose in E coli through the TAL Route Production of PHCA from glucose in E. coli using the mutant PAL: The plasmid with the mutant PAL gene, with improved TAL activity (EP18Km-6), was transformed into the wild type E. coli W3110. The cells were then grown in the minimal medium using glucose as the sole carbon source. After overnight growth, 20 μL of the growth medium was filtered, and analyzed by HPLC for detection of PHCA. No PHCA accumulation was found in the wild type (control) E. coli cells. However, when the mutant PAL gene was expressed in E. coli, 0.138 mM PHCA was detected in the overnight growth of the cells in a minimal medium containing glucose as the sole carbon source (see Table 12). TABLE 12 PHCA Production from Glucose in E. coli cells With and Without Mutant PAL/TAL Enzyme Expressed PHCA (μM) Cinnamic acid (μM) Wild type E. coli 0 0 E. coli with mutant PAL expressed 135 90 The E. coli cells lack cinnamate hvdroxylase activity: An overnight incubation of the E. coli cells, containing the PCA12Km vector, with 1.0 mM cinnamic acid did not result in PHCA production underscoring the lack of ability of the E. coli cells to convert cinnamic acid to PHCA. EXAMPLE 12 Incorporation of the Modified PAL into the Yeast Expression Vector The following yeast strains and the pGPD316 expression vector were used. Strain ZXY34-1 A contained the genotype: Mata, ade2-l, canl-100, his3-l 1, -15, leu2-3, -112, trupl-1, ura3-l, aro 3:: ΔURA3, aro4:: ΔHIS3 and was designated an aro3, aro4 double knockout. Strain ZXY0304A contained the genotype: Mata, ade2-l, canl-100, his3-l l, -15, leu2-3, -112, trupl-1, ura3-l, aro 3:: Δura3, aro4:: ΔHIS3 was an aro3, aro4 double knockout. Using standard sub-cloning methods well known in the art, the modified PAL was incorporated into the above vectors. The modified PAL cDNA (2.0 kb) was cut by Xbal and Smal restriction enzymes and the cut fragment obtained ligated into the expression vector pGPD316 which had been cut by Spel and Smal restriction enzymes. The new construct from pGPD316 plus insert from pEp 18 was designated pGSWl 8 (Figure 4). The new construct were verified by restriction enzyme digestion followed by agarose gel electrophoresis. EXAMPLE 13 The Ability of ARO4GSW to Convert Glucose to PHCA in the Absence of Aromatic Amino Acids Strain ZXY0304A contained the genotype: Mata, ade2-l, canl-100, his3-l l, -15, leu2-3, -112, trupl-1, ura3-l, aro 3:: Δura3, aro4:: ΔHIS3, designated as an aro3, aro4 double knockout was used. The ZXY0304A strain was transformed by pGSWl 8 containing the modified PAL with the standard lithium acetate method. The transformants, ARO4GSW, were selected using the SCM medium (without leucine and uracil). ARO4GSW (100 μL glycerol stock) was used to inoculate the regular SCM medium containing 2% glucose. The organisms were grown at 30 °C for 5.0 h, cells were centrifuged, resuspended in the SCM medium containing 2% glucose but without aromatic amino acids and allowed to grow overnight. The cells were then centrifuged and resuspended in the following media to a final cell density of 1.0 (ODgoo n* 1 )'- a ) regular SCM medium containing about 400 μm of phenylalanine and tyrosine and b) SCM medium without aromatic amino acids. The cells were left on the shaker (250 rpm, 0 °C) and samples (1.0 mL) were taken for HPLC analysis at 2.0, 4.0, 6.0 and 16 h. The results are shown in Table 13. TABLE 13 Effect of Aromatic Amino Acids on PHCA Production of AR04GSW Yeast Strain PHCA production (uM> 2.0 h 4.0 h 6.0 h 16 h no aromatic AA* 1.157 2.187 2.866 5.813 aromatic AA 3.806 6.316 10.313 15.147 *AA = amino acid As shown in Table 13, the recombinant yeast strain ARO4GSW produced PHCA from glucose in the absence of any additional aromatic amino acids in the growth medium. The data also demonstrate that addition of aromatic amino acids to the growth medium results in almost a 2.5 fold increase in the level of PHCA produced compared to growth in the absence of aromatic amino acids. These results underscore the ability of the recombinant Saccharomyces cerevisiae containing the mutated PAL, in the absence of the cytochrome P-450 and the cytochrome P-450 reductase, to convert glucose to PHCA. EXAMPLE 14 Effect of Phenylalanine and Tyrosine on PHCA Production by ARO4GSW Containing the Modified PAL During Aromatic Amino Acid Starvation This Example investigates the effects of phenylalanine and tyrosine on PHCA production by the recombinant yeast strain ARO4GSW containing the modified PAL during aromatic amino acid starvation. A sample (100 μL) of glycerol stock of ARO4GSW was inoculated into the regular SCM medium containing 2% glucose. The cells were left on the shaker at 30 °C for 5.0 h before they were harvested. The pellet was resuspended in the SCM medium containing 2% glucose but without aromatic amino acids and grown overnight at 30 °C on a shaker. The cultures were then centrifuged and resuspended in the following media with final cell density of 1.0 ODgoo nm : J a) regular SCM medium, b) SCM medium containing no aromatic amino acids, 2% glucose and 1.0 mM phenylalanine and c) SCM medium containing no aromatic amino acid, 2% glucose and 1.0 mM tyrosine. These cultures were returned to the shaker (250 rpm, 30 °C) and samples (1.0 mL) were taken for HPLC analysis after 2.0, 4.0, 6.0 and 16 h. Results are shown in Table 14. TABLE 14 Effect of Aromatic Amino Acids on PHCA Production of AR04GSW Yeast Strain PHCA production (uM) 2.0 h 4.0 h 6.0 h o/n no aromatic aa 0 0.609 0.806 1.327 Phe 0 0.872 1.147 1.735 Tyr 1.141 1.563 2.433 4.272 As is seen by the data in Table 14, when cells were starved for aromatic amino acids, no significant PHCA was produced. Addition of phenylalanine did not have any significant effect on the level of PHCA produced. However, addition of tyrosine, resulted in significant increase in the level of PHCA. The results therefore confirm that the novel recombinant strain containing the modified PAL gene developed in this invention preferred tyrosine as the substrate for PHCA production. EXAMPLE 15 Transformation and Expression of Mutant PAL/TAL in Maize and production of PHCA A chimeric gene comprising the mutant PAL/TAL gene (SEQ ID NO:8) in sense orientation can be constructed by polymerase chain reaction (PCR) of the gene using appropriate oligonucleotide primers. Cloning sites (Ncol or Smal) can be incorporated into the oligonucleotides to provide proper orientation of the DNA fragment when inserted into the digested vector pML103 as described below. Amplification is then performed in a 100 μL volume in a standard PCR mix consisting of 0.4 mM of each oligonucleotide and 0.3 pM of target DNA in 10 mM Tris-HCl, pH 8.3, 50 mM KC1, 1.5 mM MgCl 2 , 200 mM dGTP, 200 mM dATP, 200 mM dTTP, 200 mM dCTP and 0.025 unit DNA polymerase. Reactions are carried out in a Perkin-Elmer Cetus Thermocycler™ for 30 cycles comprising 1 min at 95 °C, 2 min at 55 °C and 3 min at 72 °C, with a final 7 min extension at 72 °C after the last cycle. The amplified DNA is then digested with restriction enzymes Ncol and Smal and fractionated on a 0.7% low melting point agarose gel in 40 mM Tris-acetate, pH 8.5, 1 mM EDTA. The appropriate band can be excised from the gel, melted at 68 °C and combined with a 4.9 kb Ncol-Smal fragment of the plasmid pML103. Plasmid pML103 has been deposited under the terms of the Budapest Treaty with the ATCC and bears accession number ATCC 97366. The DNA segment from pML103 contains a 1.05 kb Sall-Ncol promoter fragment of the maize 27 kD zein gene and a 0.96 kb Smal-Sall fragment from the 3' end of the maize 10 kD zein gene in the vector pGem9Zf(+) (Promega Corp., 7113 Benhart Dr., Raleigh, NC). Vector and insert DNA can be ligated at 15 °C overnight, essentially as described (Maniatis). The ligated DNA may then be used to transform E. coli XL 1 -Blue (Epicurian Coli XL-1; Stratagene). Bacterial transformants can be screened by restriction enzyme digestion of plasmid DNA and limited nucleotide sequence analysis using the dideoxy chain termination method (DNA Sequencing Kit, U.S. Biochemical). The resulting plasmid construct would comprise a chimeric gene encoding, in the 5' to 3' direction, the maize 27 kD zein promoter, a DNA fragment encoding the mutant PAL/TAL enzyme, and the 10 kD zein 3' region. The chimeric gene so constructed can then be introduced into corn cells by the following procedure. Immature corn embryos can be dissected from developing caryopses derived from crosses of the inbred corn lines H99 and LH132 (Indiana Agric. Exp. Station, IN, USA). The embryos are isolated 10 to 11 days after pollination when they are 1.0 to 1.5 mm long. The embryos are then placed with the axis-side facing down and in contact with agarose-solidified N6 medium (Chu et al., Sci. Sin. Peking 18:659-668 (1975)). The embryos are kept in the dark at 27 °C. Friable embryogenic callus consisting of undifferentiated masses of cells with somatic proembryoids and embryoids borne on suspensor structures proliferates from the scutellum of these immature embryos. The embryogenic callus isolated from the primary explant can be cultured on N6 medium and sub-cultured on this medium every 2 to 3 weeks. The plasmid, p35S/Ac (obtained from Dr. Peter Eckes, Hoechst Ag, v Frankfurt, Germany), may be used in transformation experiments in order to provide for a selectable marker. This plasmid contains the Pat gene (see European Patent Publication 0 242 236) which encodes phosphinothricin acetyl transferase (PAT). The enzyme PAT confers resistance to herbicidal glutamine synthetase inhibitors such as phosphinothricin. The pat gene in p35S/ Ac is under the control of the 35S promoter from Cauliflower Mosaic Virus (Odell et al., Nature 313:810-812 (1985)) and the 3M region of the nopaline synthase gene from the T-DNA of the Ti plasmid of Agrobacterium tumefaciens. The particle bombardment method (Klein et al., Nature 327:70-73 (1987)) may be used to transfer genes to the callus culture cells. According to this method, gold particles (1 μm in diameter) are coated with DNA using the following technique. Ten μg of plasmid DNAs are added to 50 μL of a suspension of gold particles (60 mg per mL). Calcium chloride (50 μL of a 2.5 M solution) and spermidine free base (20 μL of a 1.0 M solution) are added to the particles. The suspension is vortexed during the addition of these solutions. After 10 min, the tubes are briefly centrifuged (5 sec at 15,000 rpm) and the supernatant removed. The particles are resuspended in 200 μL of absolute ethanol, centrifuged again and the supernatant removed. The ethanol rinse is performed again and the particles resuspended in a final volume of 30 μL of ethanol. An aliquot (5 μL) of the DNA-coated gold particles can be placed in the center of a flying disc (Bio-Rad Labs, 861 Ridgeview Dr, Medina, OH). The particles are then accelerated into the corn tissue with a PDS-1000/He (Bio-Rad Labs, 861 Ridgeview Dr., Medina, OH), using a helium pressure of 1000 psi, a gap distance of 0.5 cm and a flying distance of 1.0 cm. For bombardment, the embryogenic tissue is placed on filter paper over agarose-solidified N6 medium. The tissue is arranged as a thin lawn and covers a circular area of about 5 cm in diameter. The petri dish containing the tissue can be placed in the chamber of the PDS-1000/He approximately 8 cm from the stopping screen. The air in the chamber is then evacuated to a vacuum of 28 inches of Hg. The macrocarrier is accelerated with a helium shock wave using a rupture membrane that bursts when the He pressure in the shock tube reaches 1000 psi. Seven days after bombardment the tissue can be transferred to N6 medium that contains gluphosinate (2 mg per liter) and lacks casein or proline. The tissue continues to grow slowly on this medium. After an additional 2 weeks, the tissue can be transferred to fresh N6 medium containing gluphosinate. After 6 weeks, areas of about 1 cm in diameter of actively growing callus can be identified on some of the plates containing the glufosinate-supplemented medium. These calli may continue to grow when sub-cultured on the selective medium. Plants can be regenerated from the transgenic callus by first transferring clusters of tissue to N6 medium supplemented with 0.2 mg per liter of 2,4-D. After two weeks, the tissue can be transferred to regeneration medium (Fromm et al., Bio/Technology 8:833-839 (1990)). Levels of PHCA production is expected to range from about 0.1% to about 10% dry weight of the plant tissue. EXAMPLE 16 Selection For An Improved TAL Enzyme Using L-Tyrosine As A Sole Carbon Source The mutagenized TAL gene (SEQ ID NO: 8) is introduced into an Acinetobacter chromosome by natural transformation, essentially as described by Kok et al., (Appl. Environ. Microbiol. 65:1675-1680 (1999)), incorporated herein by reference. The TAL gene is inserted in the host in a vector under the control a constitutive promoter and in the presence of an antibiotic resistance marker gene. Transformants are cultured on an M9 salt media (Example 4) containing 15 g agar, 6 g Na 2 HPO 4 , 3 g KH 2 PO 4 , 0.5 g NaCl, 1 g NH 4 C1, 0.5 g L-tyrosine, 2 ml 1 M MgSO 4 , 0.1 ml 1 M CaCl 2 in 1 L distilled water (pH 7.4). Transformants are isolated on the basis of antibiotic resistance. Transformants containing an evolved TAL gene that improves the conversion of L-tyrosine to PHCA show better growth on minimal media containing L-tyrosine and form larger colonies. These larger colonies are recovered for additional rounds of evolution until the desired level of TAL activity is achieved.

Claims: CLAIMS What is claimed is: 1. A method for the production of PHCA comprising: (i) contacting a recombinant host cell with a fermentable carbon substrate, said recombinant cell lacking a cinnamate hydroxylase activity and comprising a gene encoding a tyrosine ammonia lyase activity operably linked to suitable regulatory sequences; (ii) growing said recombinant cell for a time sufficient to produce PHCA; and (iii) optionally recovering said PHCA. 2. A method according to Claim 1 wherein said fermentable carbon substrate is selected from the group consisting of monosaccharides, oligosaccharides, polysaccharides, carbon dioxide, methanol, formaldehyde, formate, and carbon-containing amines. 3. A method according to Claim 2 wherein said fermentable carbon substrate is glucose. 4. A method according to Claim 1 wherein said recombinant host cell is selected from the group consisting of bacteria, yeasts, filamentous fungi, algae and plant cells. 5. A method according to Claim 4 wherein said recombinant host cell is selected from the group consisting of Aspergillus, Arthrobotrys, Saccharomyces, Zygosaccharomyces, Pichia, Kluyveromyces, Candida, Hansenula, Debaryomyces, Mucor, Torulopsis, Methylobacter, Escherichia, Salmonella, Bacillus, Acinetobacter, Rhodococcus, Rhodobacter, Synechocystis, Streptomyces, and Pseudomonas. 6. A method according to Claim 1 wherein said recombinant host cell is selected from the group consisting of soybean, rapeseed, sunflower, cotton, corn, tobacco, alfalfa, wheat, barley, oats, sorghum, rice, broccoli, cauliflower, cabbage, parsnips, melons, carrots, celery, parsley, tomatoes, potatoes, strawberries, peanuts, grapes, grass seed crops, sugar beets, sugar cane, beans, peas, rye, flax, hardwood trees, softwood trees, and forage grasses. 7. A method according to Claim 1 wherein said tyrosine ammonia lyase has a catalytic efficiency from about 4.14 x 10 3 M^sec -1 to about l x l0 9 M" 1 sec- 1 . 8. A method according to Claim 1 wherein said gene encoding a tyrosine ammonia lyase activity encodes the polypeptide set forth in SEQ ID NO: 8 or SEQ ID NO: 10. 9. A method according to Claim 1 wherein the gene encoding a tyrosine ammoma lyase activity is derived from Rhodosporidium sp. 10. A recombinant host cell lacking a cinnamate hydroxylase activity and comprising a gene encoding a tyrosine ammonia lyase activity operably linked to suitable regulatory sequences. 11. A recombinant host cell comprising a gene encoding a tyrosine ammonia lyase activity operably linked to suitable regulatory sequences selected from the group consisting of cells having the ATCC designation PTA 407 and PTA 409. 12. A cell according to Claim 10 wherein said tyrosine ammonia lyase has a catalytic efficiency from about 4.14 x 10 3 M^sec -1 to about 1 x 10 9 M^sec -1 . 13. A tyrosine ammonia lyase gene encoding the polypeptide set forth in SEQ ID NO: 10. 14. A polypeptide as set forth in SEQ ID NO: 10 15. A method for the production of PHCA comprising: (i) contacting a recombinant yeast cell with a fermentable carbon substrate , said recombinant cell comprising: a) genes encoding a plant P-450/P-450 reductase system; and b) a gene encoding a yeast PAL activity operably linked to suitable regulatory sequences; (ii) growing said recombinant cell for a time sufficient to produce PHCA; and (iii) optionally recovering said PHCA. 16. A method according to Claim 15 wherein said fermentable carbon substrate is selected from the group consisting of monosaccharides, oligosaccharides, polysaccharides, carbon dioxide, methanol, formaldehyde, formate, and carbon-containing amines. 17. A method according to Claim 16 wherein said fermentable carbon substrate is glucose. 18. A method according to Claim 15 wherein said recombinant yeast cell is selected from the group consisting of Aspergillus, Arthrobotrys, Saccharomyces, Zygosaccharomyces, Pichia, Kluyveromyces, Candida, Hansenula, Debaryomyces, Mucor, Torulopsis, and Penicillium. 19. A method according to Claim 15 wherein the genes encoding a plant P-450/P-450 reductase system are derived from plants selected from the group consisting of Jerusilum artichoke, soybean, rapeseed, sunflower, cotton, corn, tobacco, alfalfa, wheat, barley, oats, sorghum, rice, broccoli, cauliflower, cabbage, parsnips, melons, carrots, celery, parsley, tomatoes, potatoes, strawberries, peanuts, grapes, grass seed crops, sugar beets, sugar cane, beans, peas, rye, flax, hardwood trees, softwood trees, and forage grasses. 20. A method according to Claim 19 wherein the genes encoding a plant P-450/P-450 reductase system are set forth in SEQ ID NO:ll and SEQ ID NO:13. 21. A method according to Claim 15 wherein the gene encoding a yeast PAL activity is derived from the group consisting of Rhodotorula sp., Rhodosporidium sp. and Sporobolomyces sp. 22. A method according to Claim 21 wherein the gene encoding a yeast PAL actvity encodes a polypeptide as set forth in SEQ ID NO:8. 23. A recombinant host cell having the ATCC designation, PTA 408. 24. A method for the production of PHCA comprising: (i) contacting a microbial cell selected from the group consisting of Streptomyces griseus (ATCC 13273 , ATCC 13968, TU6), Rhodococcus erythropolis (ATCC 4277), Aspergillus petrakii (ATCC 12337), Aspergillus niger (ATCC 10549) and Arthrobotrys robusta (ATCC 11856) with cinnamate; (ii) growing said microbial cell for a time sufficient to produce PHCA; and (iii) optionally recovering said PHCA. 25. A method for identifying a gene encoding a TAL activity comprising: (i) contacting a recombinant microorganism comprising a foreign gene suspected of encoding a TAL activity with PHCA for a time sufficient to metabolize PHCA; and (ii) monitoring the growth of the recombinant microorganism whereby growth of the organism indicates the presence of a gene encoding a TAL activity. 26. A method for identifying a gene encoding a TAL activity comprising: (i) fransforming a host cell which uses PHCA as a sole carbon source with a gene suspected of encoding a TAL activity to create a transformant; (ii) comparing the rate of growth of the transformant with an un-transformed host cell capable of using PHCA as a sole carbon source wherein an accelerated rate of growth by the transformant indicates the presence of a gene encoding a TAL activity.

Inventors: GATENBY ANTHONY A, QI WEI WEI, SARIASLANI SIMA, TANG XIAO-SONG, VANNELLI TODD M, GATENBY, ANTHONY, A., QI, WEI, WEI, SARIASLANI, SIMA, TANG, XIAO-SONG, VANNELLI, TODD, M.
Applicants: DU PONT, GATENBY ANTHONY A, QI WEI WEI, SARIASLANI SIMA, TANG XIAO SONG, VANNELLI TODD M, E.I. DU PONT DE NEMOURS AND COMPANY, GATENBY, ANTHONY, A., QI, WEI, WEI, SARIASLANI, SIMA, TANG, XIAO-SONG, VANNELLI, TODD, M.
Application year: 2000
Main classification: C12P7
IPC codes: C12N1, C12N5, C12N9, C12N15, C12P7, C12Q1