What is claimed is:
1 . A process for producing a purified omega-3 desaturase, comprising:
(a) constructing a pPinkα-HC vector containing cDNA molecule having the nucleotide sequence shown as SEQ ID NO:1; (b) transforming a suitable host cell with said vector of Step (a), wherein said host cell is a yeast cell; (c) culturing said host cell under conditions which allow the expression of said omega-3 desaturase by said host cell; and (d) isolating said omega-3 desaturase from the culture media of Step (c); wherein said purified omega-3 desaturase is produced.
2 . The process of claim 1 , said yeast cell is Pichia pastoris.
3 . The process of claim 2 , said Pichia pastoris is selected from a group of hosts consisting of PichiaPink strain 1, PichiaPink strain 2, PichiaPink strain 3, and PichiaPink strain 4.
4 . The process of claim 3 , said omega-3 desaturase has the amino acid sequence shown as SEQ ID NO:2.
5 . A method of synthesizing polyunsaturated fatty acid, wherein an omega-3 desaturase is utilized to convert an unsaturated fatty acid into an omega-3 polyunsaturated fatty acid.
6 . The method of claim 5 , said omega-3 desaturase is produced by the process of claim 1 .
7 . The method of claim 5 , said synthesizing polyunsaturated fatty acid includes converting fatty acid C18:1 Δ9 into C18:2 Δ9,15 , C18:2 Δ9,12 into C18:3 Δ9,12,15 , C20:4 Δ5,8,11,14 into C20:5 Δ5,8,11,14,17 .
8 . The method of claim 5 , said omega-3 polyunsaturated fatty acid is able to be utilized as food supplementation to prevent human disorders, wherein said human disorders consisting of cancer, cardiovascular disease, inflammation, developmental disorders, psychiatric disorders, and cognitive aging.
 This application claims priority to U.S. patent application Ser. No. 13/646,667 filed 6 Oct. 2012 which claimed priority to Chinese Patent Application Ser. No. 201210309215.2 filed 29 Aug. 2012.
FIELD OF INVENTION
 The present invention relates to the field of microbial manufacturing of polyunsaturated fatty acids (PUFAs), specifically to the fatty acid desaturases in the synthesis process of polyunsaturated fatty acids.
BACKGROUND OF THE INVENTION
 Lipids are first synthesized as saturated fatty acids and double bonds are introduced post-synthetically by oxygen-dependent enzymes known as fatty acid desaturases, in a process that is initiated by abstraction of hydrogen from a methylene group. Fatty acid desaturases are divided into soluble and integral membrane classes, which may have been evolved independently (Shanklin J, Somerville C., “Stearoyl-acyl-carrier-protein desaturase from higher plants is structurally unrelated to the animal and fungal homologs”, Proc Natl Acad Sci USA 1991; 88:2510-4). The acyl-ACP desaturases are soluble enzymes found in the plastids of higher plants, whereas the more widespread class of integral membrane acyl-CoA desaturases is found in endomembrane systems in prokaryotes and eukaryotes (Shanklin J, Cahoon E B., “Desaturation and Related Modifications of Fatty Acids1”, Annu Rev Plant Physiol Plant Mol Biol 1998; 49:611-41). Fatty acid desaturases in each class are closely related homologs based on their amino acid sequences, and yet perform highly regio- and stereo-selective reactions on long-chain fatty acids composed of essentially equivalent methylene chains that lack distinguishing landmarks close to the site of desaturation. As pointed out by Nobel Laureate Dr. Konrad Bloch, this region- and stereo-specific removal of hydrogen “would seem to approach the limits of the discriminatory power of enzymes” (Bloch K., “Enzymatic synthesis of monounsaturated fatty acids”, Accounts of Chemical Research 1969; 2:193-202).
 The membrane class of desaturases consists of enzymes with c5, c6, c9, c12 or ω3 regio-selectivity. Mammalian cells possess c5, c6 and c9, but lack c12 and ω3 desaturases (Berquin I M, Edwards I J, Kridel S J, Chen Y Q, “Polyunsaturated fatty acid metabolism in prostate cancer”, Cancer Metastasis Rev 2011; 30:295-309, and Chen Y Q, Edwards I J, Kridel S J, Thornburg T, Berquin I M., “Dietary fat-gene interactions in cancer”, Cancer Metastasis Rev 2007; 26:535-51). Mortierella alpina belongs to the subphylum of Mucoromycotina (Hibbett D S, Binder M, Bischoff J F, et al., “A higher-level phylogenetic classification of the Fungi”, Mycol Res 2007; 111:509-47). It can produce lipids up to 50% of its dry weight. We have recently characterized M. alpina genome (Wang L, Chen W, Feng Y, et al., “Genome Characterization of the Oleaginous Fungus Mortierella alpine”, PLoS One 2011; 6:e28319) which encodes one c5, two c6, three c9, one c12 and one ω3 desaturase. Therefore, M. alpina has all known regio-selective groups of membrane desaturases.
 We have expressed M. alpina c9, c12 and ω3 desaturases (FADS9-I, FADS12 and FADS15) in the methylotrophic yeast Pichia pastoris , purified the recombinant proteins and determined their enzymatic activities.
DETAILED DESCRIPTION OF THE INVENTION
 The applicant has identified a novel ω3 desaturase and a Δ9 desaturase, successfully expressed, purified and characterized their enzymatic activities More specifically, the applicant designed primers of nucleotide aiming to three desaturases coding for Δ9-I Des, Δ12 Des and ω3 Des on the basis of whole-genome sequencing of M. alpina , the sequences of specific primers are listed in Table 1 . M. alpina RNA was extracted and reverse transcribed to obtain cDNA. The amplified three sequences by PCR with three pairs of primer of FF1 and FR1, FF2 and FR2, FF3 and FR3 to PCR were inserted into pET19b (PP) and sequenced, and then subcloned into pPinkα-HC, an expression vector in Pichia pastoris . Expression vectors were linearized and transformed into PichiaPink strain 2. The recombinant strains thus obtained express the above-mentioned three desaturases. The enzyme activity analysis showed that the purified recombinant desaturases were functional
 The present invention provides genes coding for M. alpina ω3 desaturase (FADS15) and Δ9 desaturase (FADS9-I), whose nucleic acid sequences are shown as SEQ ID NO:1 and SEQ ID NO:3, respectively.
 The present invention also provides expression vectors respectively containing SEQ ID NO:1 and SEQ ID NO:3 which can respectively express M. alpina ω3 desaturase (FADS15) and Δ49 desaturase (FADS9-I). Preferably, the said expression vector is Pichia pastoris expression vector.
 The present invention also provides a recombinant microorganism which can respectively express ω3 desaturase (FADS15) and M. alpina Δ9 desaturase (FADS9-I). Preferably, the said recombinant microorganism is recombinant Pichia pastoris PichiaPink strain 2, which contains Pichia pastoris expression vector carrying SEQ ID NO:1 or SEQ ID NO:3.
 The present invention successfully expresses and purifies the novel membrane ω3 desaturase (FADS15) and Δ9 desaturase (FADS9-I), which play a key role in the polyunsaturated fatty acid biosynthetic pathway, and whose amino acid sequences are shown as SEQ ID NO:2 and SEQ ID NO:4. Furthermore, the present invention verifies the enzyme activity of the above two kinds of membrane desaturases. The present invention apply the above-mentioned novel membrane desaturases ω3 desaturase (FADS15) in the polyunsaturated fatty acid biosynthesis, converting fatty acid C18:1 Δ9 into C18:2 Δ9,15 , C18:2 Δ9,12 into C18:3 Δ9,12,15 , C20:4 Δ5,8,11,14 into C20:5 Δ5,8,11,14,17 . Omega-3 polyunsaturated fatty acids can be utilized as food supplementation to prevent human disorders, wherein said human disorders consisting of cancer, cardiovascular disease, inflammation, developmental disorders, psychiatric disorders, and cognitive aging.
Primers′ sequence table and its restriction
enzyme cutting site:
FF1(SEQ ID: 5)
atat CATATG ATGGCCCCCCCTC
FF2(SEQ ID: 6)
atat ATTAAT ATGGCACCTCCCA
FF3(SEQ ID: 7)
atat CATATG ATGGCAACTCCTC
FR1(SEQ ID: 8)
atat GGATCC TAATGCTTGTAG
FR2(SEQ ID: 9)
atat GGATCC TTACTTCTTGA
FR3(SEQ ID: 10)
atat AGATCT TTATTCGGCCT
SF1(SEQ ID: 11)
SR1(SEQ ID: 12)
atat GAATTC AT ATTTAAAT T
(Eco RI, Swa I)
SR2(SEQ ID: 13)
atatat GGTACC TTACTTCT
SR3(SEQ ID: 14)
atatat GGTACC TTATTCGGCC
DESCRIPTION OF THE ATTACHED DRAWINGS
 FIG. 1 : Diagram of the cloning strategy for desaturase expression vectors. FADS coding sequences were PCR amplified using primers listed in Table 1. PCR fragment were digested with indicated restriction enzymes, column purified and inserted into the pET-19b(PP) vector linearized with corresponding restriction enzymes. The FADS coding sequence plus His tag and Precision protease recognition sequence were PCR amplified and inserted into the pPinkalpha-HC vector. TRP2: TRP2 gene, AmpR: ampicillin resistance gene, pUC ori: oriental promoter of pUC, PAOX1: 5′AOX1 promoter region, α-factor: α-mating factor secretion signal, CYC1 TT: CCY1 transcription termination region, PADE2 HC: high-copy ADE2 promoter region, ADE2: ADE2 open reading frame.
 FIG. 2 : the sequencing results of the clone sequence of ω3 desaturase (FADS15), in which FADS15 nucleotide sequence from M. alpina ATCC#32222 shows 93.1% identity with AB182163 from M. alpina 1s-4.
 FIG. 3 : the sequencing results of the clone sequence of 412 desaturase (FADS12), in which FADS12 nucleotide sequence from M. alpina ATCC#32222 shows 99.9% identity with AF110509 from M. alpina 1s-4.
 FIG. 4 : the sequencing results of the clone sequence of Δ9 desaturase (FADS9-I), in which FADS9-I nucleotide sequence from M. alpina ATCC#32222 shows 98.4% identity with AF085500 from M. alpina 1s-4.
 FIG. 5A : Growth curve of the recombinant P. pastoris measured by cell density, wet weight and total protein concentration.
 FIG. 5B : Kinetics of recombinant protein induction. Desaturase expression was determined by Western blotting using anti-His tag antibody. The normalized level of highest expression was set at one arbitrary unit. Three independent experiments were performed and bars represent standard deviations.
 FIG. 5C : Quantification of the recombinant desaturase proteins by Coomassie blue staining after SDS-PAGE. Known concentrations of BSA were used as quantification standard.
 FIG. 5D : InVision™ His-tag In-Gel Stain of recombinant FADS proteins. The arrow head indicates the addition of methanol for induction of recombinant protein expression. The triangles indicate the expressed recombinant proteins. M: protein marker, Cont: negative control which was PichiaPink™ harboring pPinkα-HC, 15: FADS15, 12: FADS12, 9-I: FADS9-I.
 FIG. 6A : Fractionation of recombinant desaturases. InVision™ His-tag In-Gel Staining after SDS-PAGE analysis of FADS9-I membrane (top panel) and supernatant fraction (bottom panel), using different speeds of centrifugation. The triangles indicate the recombinant FADS9-I.
 FIG. 6B : Coomassie blue Staining and InVision™ His-tag In-Gel Staining of recombinant desaturases after fractionation. T: total protein after grinded by glass beads, D: debris after centrifugation at 500 g for 10 min, M: membrane fraction after centrifugation at 10,000 g for 10 min, S: supernatant after the centrifugation. The triangles indicate the recombinant desaturase proteins.
 FIG. 7A : Solubilization of recombinant desaturases. Membrane fractions were suspended in 1% concentrations of various detergents and incubated at 4° C. for 2 hr. Proteins were visualized by InVision™ His-tag In-Gel Staining (upper panel) and Western blot (lower panel). T20: Tween-20, T80: Tween-80, N40: NP-40, DDM: n-Dodecyl-β-D-maltoside, F12: Fos-Choline 12, F16: Fos-Choline 16,S: supernatant, P: pellet.
 FIG. 7B : Membrane fractions of recombinant FADS9-I were suspended in 1% Fos-Choline 16 and incubated at 4° C. for various time (0, 0.5, 1.5, 3, 12 hr). Aliquots were analyzed by InVision™ His-tag In-Gel Staining. S: supernatant, P: pellet.
 FIG. 7C : One-step purification using His Mag Sepharose Ni beads under the high yield (upper panel) and high stringency conditions (lower panel). Proteins were analyzed by SDS-PAGE and Coomassie blue staining. M: protein marker, S: supernatant, F: flow through, E: eluate.
Mortierella alpina Culture
 Mortierella alpina (#32222, American Type Culture Collection, Manassas, Va., USA) was inoculated on Potato Dextrose Agar (PDA) plates (BD Difco™ Potato Dextrose Agar cat#213400) and incubated for 20-30 days at 25° C. 5 mL broth (20 g/L Glucose, 5 g/L Bacto yeast extract BD Biosciences cat#212750, 1 g/L KH 2 PO 4 , 0.25 g/L MgSO 4 , 10 g/L KNO 3 ) were added to three plates. Spores were gently scraped off the surface with a sterile loop, and then filtrated through a 40 micron cell strainer. Spores were concentrated by centrifuging at 12,000×g for 15 min, suspended in a small volume of broth, enumerated using a hemocytometer, and kept at −80° C. in 30% glycerol at a density of approximately 10 7 spores/mL. Alternatively, 3 mL of unconcentrated spore suspension were directly added into 45 mL broth without KNO 3 in a 250-mL flask covered with 8 layers of cheese cloth, and shaken at 200 rpm, 25° C. for 5 days. Cultures were blended using a Braun hand blender for 5 sec/pulse, 8 pulses, then 0.3 g wet mycelia were inoculated into 45 mL broth without KNO 3 in a 250-ml flask and shaken at 200 rpm, 25° C. for 24 h. The above step was repeated once, by which time the whole fungal culture was in proliferative phase and ready for experiments. Mycelia were collected by filtration and weighed. Samples were snap-frozen in liquid nitrogen, pulverized and kept at −80° C. for RNA extraction.
Expression Vector Construction
 M. alpina RNA extraction was performed using Trizol Reagent (Invitrogen, CA) according to the manufacturer's instructions. Total RNA was reverse transcribed with SuperScript® III First-Strand Synthesis SuperMix (Invitrogen) following the manufacturer's instructions. Using both C- and N-terminal sequences as primers (Table 1), desaturase coding sequences were PCR amplified as follows: denaturation at 95° C. for 30 sec, annealing at 55° C. for 45 sec and extension at 72° C. for 1 min for 25 cycles. The amplified products were cloned into a modified pET19 vector (Novagen) derivative containing a PreScission protease cleavage site (GE Healthcare) between the multiple cloning site and N-terminal His tag (Jonsson T J, Johnson L C, Lowther W T (2009) Protein engineering of the quaternary sulfuredoxin.peroxiredoxin enzyme.substrate complex reveals the molecular basis for cysteine sulfinic acid phosphorylation. J Biol Chem 284: 33305-33310.) to construct pET19b-FADS15, pET19b-FADS12 and pET19b-FADS94). The desaturase genes, including the His-Tag and PreScission protease cleavage site, were then PCR amplified using primers SF1 and SR1-SR3 (Table 1). The PCR conditions used were the same as the first step for cDNAs. The PCR fragments were then purified and inserted into pPinkα-HC to generate the expression vectors pPinkα-HC-FADS15, pPinkα-HC-FADS12 and pPinkα-HC-FADS9-I. The presence of the inserts in the plasmids was confirmed by restriction digestion analysis and sequencing. The strategy used for constructing desaturase expression vectors is shown in FIG. 1 . Sequencing results from the amplified fragment of these desaturases are in FIG. 2-4 . The FADS12 and FADS9-I genes from M. alpina ATCC#32222 are 99.9% and 98.4% identical, respectively, to the corresponding genes from M. alpina 1s-4. The FADS12 and FADS9-I proteins from M. alpina ATCC#32222 are 100% and 99.6% identical, respectively, to these proteins from M. alpina 1s-4. The high similarity of FADS12 and FADS9-I genes between two strains indicates that these genes are highly conserved in M. alpina . Interestingly, the FADS15 gene is much less conserved at both DNA (93.1% identity) and protein (97.9%) levels.
 Desaturase expression vectors and pPinkα-HC (negative control vector) were linearized with restriction enzyme Spe I and transformed into P. pastoris strains (PichiaPink strain 1, 2, 3 and 4) using the MicroPulser Electroporator (Bio-Rad Laboratories, Hercules, Calif.) according to the User Manual of PichiaPink Expression System (Invitrogen). P. pastoris were incubated with YPDS media (YPD with 1 M sorbitol) in the Gene Pulser Cuvettes at 28° C. for 2 hr without shaking, spread onto PAD (Pichia Adenine Dropout) agar selection plates, and then incubated at 28° C. for 4 days until distinct colonies were formed. Eight white colonies for each transformation were picked and plasmid integration in the yeast genome was confirmed by PCR.
 Isolated clones were individually inoculated into 10 mL of BMGY medium (Buffered Glycerol-complex Medium, 1% yeast extract; 2% peptone; 100 mM potassium phosphate, pH 6.0; 1.34% YNB-Yeast Nitrogen Base; 0.0004% biotin; 1% glycerol) in 50 mL conical tubes. The cells were grown for 48 hr at 28° C. with vigorous shaking at 250 rpm. Then, the cultures were centrifuged at 1,500 g for 5 mM at room temperature, the cell pellets were resuspended in 2 mL of BMMY medium (Buffered Methanol-complex Medium, 1% yeast extract; 2% peptone; 100 mM potassium phosphate, pH 6.0; 1.34% YNB; 0.0004% biotin; 0.5% methanol) and cultured at 28° C. with shaking at 250 rpm to induce the expression. After continuous cultivation for 72 hr with daily addition of 0.5% methanol, cells were harvested by centrifuging for 10 mM at 1500 g. Supernatant was transferred to a separate tube and both the supernatant and cell pellet were stored at −80° C. until ready for assay. Supernatants and cell pellets were analyzed for protein expression by SDS-PAGE Coomassie blue staining and Western blot. Our data showed that PichiaPink strain 2(ade2, pep4) supported the highest level of expression for FADS15, 12 and 9-I.
Expression Condition Optimization and Protein Analysis
 Individual colonies of P. pastoris -FADS15, FADS12 and FADS9-I were inoculated into 10 mL of BMGY medium in 50 mL conical tubes and cultured for 48 hr at 28° C. at shaking speed of 250 rpm. Then, 2.5 mL of culture were inoculated into 50 mL of BMGY medium in 250-mL volume shaker flasks and grown at 28° C. for 24 hr at 250 rpm. The cells were collected by centrifugation at 1500 g for 10 mM, and resuspended in 10 mL induction medium (BMMY medium with 0.5% methanol) in a 100-mL shaker flask. The induction of protein expression was performed for 96 hr at 28° C. with 250 rpm agitation and daily addition of 0.5% methanol. Samples were collected at 0, 6, 24, 48, 72 and 96 hr for measuring cell density at OD 600 , wet cell weight and total protein concentration, and for Western blot analysis of desaturase expression levels.
 The cell pellets and supernatants were collected by centrifuging 100 μL cell culture at 1500 g for 10 mM Cell pellets were resuspended in 100 μL lysis buffer (20 mM Tris. Cl pH7.9, 1 mM EDTA, 5% Glycerol) with an equal volume of 0.5 mm Glass Beads (Biospec products, Inc.), and vortexed for 10 mM at 4° C. Cell lysates were mixed with 4×SDS sample buffer and heated for 5 mM at 95° C. About 5 μl sample was loaded onto Mini-Protein Precast Gels (4-15%, Bio-Rad Laboratories, Cat #456-1086), and ran for 40 mM at 150 V. Then, the SDS-PAGE gels were used for Coomassie blue stain, Invision His-Tag in-gel stain (Invitrogen) or Western blot.
 For Western blot analysis, protein gels were transferred onto a nitrocellulose transfer membrane (Schleicher & Schuell GmbH, Germany) by electroblotting (100 V, 2 hr) using Mini Trans-Blot electrophoretic transfer cell (Bio-Rad Laboratories). The membrane was blocked with 3% BSA in TBST (150 mM NaCl, 10 mM Tris-Cl pH 7.5, 0.05% Tween20), and probed with mouse Penta•His antibody (Invitrogen) followed by HRP-conjugated goat anti-mouse IgG (GE Healthcare). Blots were then incubated with enhanced chemiluminescence reagent (ECL, GE healthcare) and analyzed using Fluorchem E (Cell Biosciences, Inc.).
 The total protein concentration was determined with Pierce BCA protein assay kit (Thermo Scientific). The quantification of target protein on Coomassie blue stained gel was performed using known concentrations of BSA as standard, and analyzed with the AlphaView SA software (Cell Biosciences, Inc.).
 To determine potential toxicity of recombinant proteins, we first examined cell growth density, weight and total protein synthesis of the PichiaPink pPinkα-HC-FADS clones. The recombinant PichiaPink pPinkα-HC-FADS cells had growth characteristics similar to the control ( FIG. 5A ). A time course experiment showed that desaturase expression was detectable after 24 hr induction with 0.5% methanol and remained high for at least 72 hr post-induction ( FIG. 5B ). There were no significant differences in protein expression when cells were induced at different temperatures (16° C., 22° C., 28° C.) or with a different concentration of methanol (0.5%, 1%). Therefore, we used an optimized procedure as described in the Materials and Methods for the expression of recombinant desaturase. Under this condition, expression levels of recombinant desaturase proteins reached approximately 130 mg/L of culture for FADS15, 110 mg/L for FADS12 and 350 mg/L for FADS9-I ( FIG. 5C ).
 All purification procedures were performed at 4° C. Cells harvested from 800 μL of culture were suspended in 800 μL of lysis buffer. After addition of 0.5 mm glass beads to the cell suspension, P. pastoris cells were disrupted by vortexing at 4° C. for 10 min Cell lysis efficiency was usually more than 95% evaluated using a light microscope. Intact cells and cell debris were removed from the membrane suspension by low speed centrifugation (500 g, 10 min at 4° C.). Then various centrifugation speeds and time (1,000 g for 10 min; 10,000 g for 10 min; 10,000 g for 20 min; 20,000 g for 10 min; 20,000 g for 20 min) were used to determine the best centrifugation conditions for collecting the membrane fraction.
 Fractions containing recombinant desaturases were solubilized in buffer, containing 20 mM Tris.Cl, pH 7.9, 500 mM NaCl, 10% glycerol, 0.1 mM EDTA, and different concentrations (0.5%, 1%, 2%) of various detergents (Tween 20, Tween 80, Nonidet P-40, DDM, Fos-Choline 12, Fos-Choline 16) at 4° C. for different times (0.5, 1, 1.5, 2 hr and overnight). The insoluble materials were removed by centrifugation at 25,000 g for 30 min at 4° C.
 Optimized culture and protein solubilization conditions were used for the subsequent purification process. His Mag Sepharose™ Ni affinity beads (GE Healthcare) were washed with binding buffer (20 mM Tris.Cl, pH 7.9, 500 mM NaCl, 10% glycerol, 0.1 mM EDTA, 0.5% Fos-Choline 16, 5 or 20 mM imidazole) and added to the solubilized fractions after detergent incubation. The bead-protein sample mixtures were incubated for 45 min at 4° C. with end-over-end mixing. After washing three times with binding buffer containing 5 mM or 20 mM imidazole, desaturase enzymes were eluted with elution buffer (20 mM Tris.Cl, pH 7.9, 500 mM NaCl, 10% glycerol, 0.1 mM EDTA, 0.5% Fos-Choline 16, 500 mM imidazole). The purified FADS15, FADS12 and FADS9-I proteins were stored at −80° C. in aliquots. The quantity and quality of these purified enzymes were analyzed by SDS-PAGE and desaturase activity assay.
 In order to solubilize and purify the recombinant desaturases from cell membrane for in vitro enzymatic activity, we first tested conditions to enrich the cell membrane containing recombinant FADS15, FADS12 and FADS9-I. Different centrifugation speeds and times were examined for the separation of the membrane fractions containing target proteins. Efficient recovery of each recombinant desaturase produced in P. pastoris was achieved by centrifuging the cell homogenates at 500 g for 10 min to remove cell debris, then at 10,000 g for 10 min to collect membrane fractions ( FIG. 6 ).
 Solubilization of membrane proteins requires the presence of detergents. Therefore, we tested the conditions for solubilization of the recombinant FADS15, FADS12 and FADS9-I from enriched cell membrane fractions using a panel of detergents: Tween-20, Tween-80, NP-40, n-Dodecyl-β-D-maltoside (DDM), Fos-Choline 12 or Fos-Choline 16. After treatment with 1% (w/v) of Fos-Choline 12 or Fos-Choline 16, FADS9-I and FADS12 were totally solubilized, and approximately 50% and 80% of FADS15 was solubilized with Fos-Choline 12 and Fos-Choline 16, respectively ( FIG. 7A ). Tween-20, Tween-80, NP-40 and DDM had little effect on extracting these desaturase enzymes from the membrane. In addition, we noticed that FADS9-I protein degradation occurred during protein solubilization. This phenomenon was visible for proteins solubilized by both Fos-Choline 12 and 16. Thus, we investigated detergent incubation time during solubilization to optimize for the least protein degradation. Our results showed that the solubilization of FADS9-I protein reached its maximum level after incubation with detergent for 1.5 hr. Degradation of desaturase protein increased after more than 3 hr of incubation ( FIG. 7B ). To maximize the ratio of intact vs. degraded proteins, we used 1.5 hr as our standard detergent incubation time for protein solubilization. We also compared the effect of detergent concentrations on protein solubilization efficiency and found that 0.5%, 1% or 2% of Fos-Choline 16 had similar effects. Taken together, our results indicate that all three recombinant desaturase enzymes can be solubilized efficiently from the cell membrane with 0.5% Fos-Choline 16 for 1.5 hr at 4° C.
 Solubilized FADS15, FADS12 and FADS9-I were affinity-purified on His Mag Sepharose Ni beads (GE healthcare) with aims of high purity or high yield. High purity (>95%) was achieved after one step purification using the His Mag Sepharose Ni beads with high stringency wash before elution ( FIG. 7C ). High yield (2-fold higher than that in the high purity process) was achieved with low stringency wash. Yield and quantity of each desaturase enzyme are summarized in Table 2. Our estimated yields of desaturases with purity >95% are approximately 22.5 mg/L for FADS15, 12 mg/L for FADS12 and 188 mg/L for FADS9-I.
Purification of M. alpina desaturases
(20 mM ID)
(5 mM ID)
Desaturase Activity Assay
 Approximately 20 mg of P. pastoris cell pellets were collected and used for each lipid extraction with the method of Bligh and Dyer (Bligh E G, Dyer W J (1959) A rapid method of total lipid extraction and purification. Can J Biochem Physiol 37: 911-917). under acidified conditions with pentadecanoic acid and heneicosanoic acid added as internal standards. The solvent from the extract was removed under a stream of nitrogen. Lipids were saponified in 1 mL of freshly prepared 5% ethanolic potassium hydroxide at 60° C. for 1 hr under an argon atmosphere. After cooling, 1 mL of water was added to the samples and non-saponifiable lipids were extracted into 3 mL of hexane. The aqueous layer was acidified with 220 μL of 6 M hydrochloric acid and the fatty acids extracted into 3 mL of hexane. After removing the hexane in a stream of nitrogen, fatty acids were converted to methyl esters by first treating with 1 mL of 0.5 M methanolic sodium hydroxide at 100° C. for 5 min under argon followed by 1 mL of 14% methanolic boron trifluoride at 100° C. for 5 min under argon (Metcalfe L D, Schmitz A A, Pelka J R (1966) Rapid preparation of fatty acids esters from lipids for gas chromatographic analysis. Analytical Chemistry 38: 514-515.). After cooling, the sample was mixed with 2 mL of hexane followed by 4 mL of saturated aqueous sodium chloride. After separating the phases, aliquots of the hexane layers were diluted 24-fold with hexane and then analyzed by GC/MS. One μL was injected in the splitless mode onto a 30 m×250 μm DB-WAXETR column (Agilent Technologies, Santa Clara, Calif.) with 0.25 μm film thickness. The temperature program was as follows: 100° C. for 2 mM, ramp to 200° C. at 16° C. per mM, hold for one mM, ramp to 220° C. at 4° C. per mM, hold one mM, ramp to 260° C. at 10° C. per mM, and hold for 11 mM Helium was the carrier gas at a constant flow of 1.5 mL/min. The mass spectrometer was operated in positive-ion electron impact mode with interface temperature 260° C., source temperature 200° C., and filament emission 250 μA. Spectra were acquired from m/z 50 to 450 with a scan time of 0.433 s. Lower-boiling fatty acid methyl esters were quantified using the pentadecanoic acid internal standard, whereas higher-boiling methyl esters were quantified using the heneicosanoic acid internal standard.
 In Vivo Desaturase Activity Analysis:
 Individual colonies of P. pastoris -FADS15, FADS12 and FADS9-I were cultured as described in the Recombinant protein expression section. Protein expression was induced for 72 hr with 0.5% methanol. Cell pellets were collected by centrifugation and stored at −80° C. for fatty acid analysis.
 In Vitro Desaturase Activity Analysis:
 20 μL of the purified protein was added to 200 μL of yeast EGY49 cell homogenate, prepared by breaking cells with 0.5 mm glass beads in lysis buffer (20 mM Tris-HCl pH7.9, 1 mM EDTA, 5% Glycerol). The enzyme reactions were performed at 28° C. for 3 h with shaking (250 rpm), and the assay mixture (220 μL) were stored at −80° C. for fatty acid analysis.
 To determine the functional activity of the recombinant M. alpina desaturase in vivo, PichiaPink cells were cultured and induced to express desaturases. Fatty acid methyl esters (FAME) analysis of cell pellets showed that expression of recombinant desaturases in PichiaPink cells altered their fatty acid contents compared to the control. Table 3 shows the percentage increase of C16:1 Δ9 , C18:1 Δ9 , C18:2 Δ9,12 and C18:2 Δ9,12,15 compared to the negative control. The C16:1 Δ9 and C18:1 Δ9 were increased 40% and 20%, respectively, in PichiaPink cells expressing FADS9-I, suggesting that FAD9-I can insert the first double bond into both C16:0 and C18:0 with a preference for C16:0 as substrate. The C18:2 Δ9,12 content was 27% higher in cells expressing FADS12, suggesting that FADS12 can desaturate C18:1 Δ9 at the c12-position to produce C18:2 Δ9,12 . There was a 5% increase in C18:3 Δ9,12,15 in cells expressing FADS15, suggesting that FADS15 can desaturate C18:2 Δ9,12 at the c15-position to produce C18:3 Δ9,12,15 . These results suggest that the recombinant desaturases, FADS9-I, FADS12 and FADS15, were active in P. pastoris.
 We used yeast EGY49 cell homogenate for our in vitro assay of recombinant desaturase activity. Our results showed that purified recombinant FADS12 converted C18:1 Δ9 to C18:2 Δ9,12 in vitro, and C18:2 Δ9,12 level was increased 116% compared to the control (Table 3). Activities of purified FADS9-I and FADS15 were relatively low in vitro.
M. alpina desaturases in-vivo and in-vitro activities
C18:2 Δ9, 12
C18:3 Δ9, 12, 15
C18:2 Δ9, 12
C18:3 Δ9, 12, 15
(% a )
40 ± 6
20 ± 7
27 ± 4
5 ± 3
6 ± 8
7 ± 7
116 ± 40
8 ± 4
60 ± 7 b
13 ± 8
a Percent increase over control;
b Sum of two products