Synthesis of Polymer Precursor 12-Oxododecenoic Acid Utilizing Recombinant Papaya Hydroperoxide Lyase in an Enzyme Cascade

Hydroperoxide lyases (HPLs) catalyze the splitting of 13S-hydroperoxyoctadecadienoic acid (13S-HPODE) into the green note flavor hexanal and 12-oxo-9(Z)-dodecenoic acid, which is not yet used industrially. Here, HPL from Carica papaya (HPLCP) was cloned and functionally expressed in Escherichia coli to investigate synthesis of 12-oxo-9(Z)-dodecenoic acid in detail. To improve the low catalytic activity of full-length HPLCP, the hydrophobic, non-conserved N-terminal sequence was deleted. This enhanced enzyme activity from initial 10 to 40 U/l. With optimization of solubilization buffer, expression media enzyme activity was increased to 2700 U/l. The tetrameric enzyme was produced in a 1.5 l fermenter and enriched by affinity chromatography. The enzyme preparation possesses a slightly acidic pH optimum and a catalytic efficiency (kcat/KM) of 2.73 × 106 s−1·M−1 towards 13S-HPODE. Interestingly, HPLCP-N could be applied for the synthesis of 12-oxo-9(Z)-dodecenoic acid, and 1 mM of 13S-HPODE was transformed in just 10 s with a yield of 90%. At protein concentrations of 10 mg/ml, the slow formation of the 10(E)-isomer traumatin was observed, pointing to a non-enzymatic isomerization process. Bearing this in mind, a one-pot enzyme cascade starting from safflower oil was developed with consecutive addition of Pseudomonas fluorescens lipase, Glycine max lipoxygenase (LOX-1), and HPLCP-N. A yield of 43% was obtained upon fast extraction of the reaction mixtures after 1 min of HPLCP-N reaction. This work provides first insights into an enzyme cascade synthesis of 12-oxo-9(Z)-dodecenoic acid, which may serve as a bifunctional precursor for bio-based polymer synthesis. Supplementary Information The online version contains supplementary material available at 10.1007/s12010-022-04095-0.


Introduction
optimized HPL from guava was expressed with improved stability [31]. Little attention was paid so far to the co-product 12-oxododecenoic acid, which is naturally isomerized to traumatin, an important phytohormone for wound healing [32].
Here we present the cloning, expression, and characterization of papaya HPL as well as evaluation of its 12-oxododecenoic acid synthesis starting from 13S-hydroperoxyoctadecadienoic acid (13S-HPODE). The objective of the work was the synthesis of a bifunctional C12-intermediate suitable for polymer application without using tropical lauric acid-rich oils. For this, we developed an enzyme cascade with N-terminally truncated papaya HPL, soybean LOX-1, and P. fluorescens lipase for multi-step transformation starting from safflower oil (Fig. 1).

Bioinformatic Analyses
Carica papaya HPL sequence (accession number: XP_021890218.1) was identified through BLAST analysis with the "National Center for Biotechnology Information" (NCBI) website by searching for putative HPL sequences of the already analyzed guava HPL (accession number: AAK15070.1). A multiple sequence alignment of protein sequences was performed with ClustalW [33] using the BLOSUM62 matrix. A phylogenetic tree was created with ClustalX [34] and NJPlot [35] with the neighbor-joining algorithm. The bootstrap value was set to 1000.

Cloning and Expression of HPL
All strains, vectors, and oligonucleotides are listed in Table 1. Oligonucleotides were synthesized by Eurofins genomics (Germany). The hpl CP gene was codon-optimized for expression in E. coli and synthesized with a C-terminal hexahistidine tag through gene synthesis by BioCat GmbH (Germany). The gene was cloned into the expression vector pET-28a( +) (Fig. S1). The non-conserved, hydrophobic N-terminus was identified with  [36] was transformed with the fulllength as well as the truncated hpl vectors. Cells expressing HPL were cultivated in 500-ml shaking flasks in 50-ml lysogeny broth (LB), terrific broth (TB), or ZYM5052 (compositions of cultivation media are listed in Table S1) with 50 µg/ml kanamycin. Optionally, 2.5 mM δ-aminolevulinic acid and 0.1 mM ammonium ferric citrate were added. The shaking flasks were inoculated with 2% (v/v) bacteria from an overnight culture. Cells were cultivated at 37 °C and 200 rpm until OD 600 of 0.6 (for cultivation in LB) or 1 (for cultivation in TB and ZYM5052) was reached. Protein expression in LB and TB broth was induced by addition of 1 mM isopropyl β-d-1-thiogalactopyranoside (IPTG), and temperature was decreased to 25 °C. Cells were cultivated for 24 h. Then, cells were harvested by centrifugation at 4500 × g for 15 min and frozen at − 20 °C until further use. Cell pellets were suspended in 10 ml buffer (50 mM potassium phosphate buffer pH 6 with 1 M NaCl and 0.2% Triton X-100 if not noted otherwise) and disrupted by ultrasound sonication for 105 s in seven intervals of 15 s. The soluble fraction (SF) was obtained from the crude extract (CE) by centrifugation for 45 min with 21,000 × g at 4 °C.

Fermentation and Purification of Papaya HPL CP-N
HPL CP-N was expressed in a 3-l BioFlo Fermenter 115 (Eppendorf, Germany) for 24 h at 25 °C with 1.5 l auto-inductive ZYM5052 broth containing 50 µg/ml kanamycin and 2.5 mM δ-aminolevulinic acid. Cultivation was inoculated with 2% (v/v) bacteria from an overnight culture. The stirrer was set to 400-800 rpm, and air was injected with 2.25 l/m (1.5 vvm) with minimum dissolved oxygen (DO) level of 30%. Cell harvesting was done as described in the "Analysis of 12-Oxododeceneoic Acid Formation" section, and the cell pellet was dissolved in binding buffer (50 mM potassium phosphate buffer pH 6 with 1 M NaCl, 40 mM imidazole, and 0.2% Triton X-100). The soluble fraction was prepared by cell disruption and centrifugation as described in the "Analysis of 12-Oxododeceneoic Acid Formation" section, and the His6-tagged HPL CP-N was purified with nickel affinity chromatography using a HisTrap™ HP 5 ml column (Cytiva, USA). The soluble fraction was loaded onto the column, and then non-specific bound proteins were removed by washing with 50 mM potassium phosphate buffer pH 6 with 1 M NaCl containing 0.1% Triton X-100 and 40-100 mM imidazole. Finally, HPL CP-N was eluted with 500 mM imidazole and stored at 4 °C until further use.
HPL CP-N purification was monitored by SDS-PAGE (sodium dodecyl sulfate polyacrylamide gel electrophoresis) with Coomassie Brilliant Blue R250 staining, and the HPL CP-N band was verified by Western blotting. Proteins were transferred onto a PVDF (polyvinylidene difluoride) membrane and incubated with the monoclonal AP-conjugated Anti-His (C-term) antibody (Invitrogen, Thermo Fisher Scientific, USA, AB_2556555) in a 1:2000 dilution. Histidine-tagged proteins were visualized with alkaline phosphatase (New England Biolabs GmbH, Germany).

Preparation of Fatty Acid Hydroperoxides
Linoleic acid was prepared from safflower oil by alkaline hydrolysis and enrichment by urea crystallization as described before [11]. Linoleic acid was then diluted in 2.5 l of cold 50 mM sodium borate buffer (pH 9.5) to a final concentration of 1 mM. The peroxidation reaction was started by addition of 15 mg LOX-1 and performed for 1 h under stirring and a constant flow of 400 ml/min pure oxygen at 4 °C. The solution was acidified to pH 3.5 with HCl before adding an equivalent volume of ethyl acetate. The organic phase was separated and washed with water before evaporating residual solvent under vacuum. Final HPODE content and regioisomeric ratio were determined photometrically at 234 nm and by HPLC analysis as described before [11].

Characterization of Papaya HPL CP-N
Enzymatic activity was determined photometrically with a UV-3100PC spectrophotometer from VWR (Germany). If not noted otherwise, 10 µl HPL CP-N in an appropriate dilution was mixed with 990 µl 50 mM potassium phosphate buffer pH 6 with 1 M NaCl and 40 µM 13S-HPODE. The decrease of absorption was measured for 300 s at 22 °C at 234 nm, correlating to the decline of the conjugated double bond system of 13S-HPODE. The activity was measured in units. One unit is defined by the amount of enzyme that catalyzes 1 µmol substrate per minute. Volumetric activity was calculated using an extinction coefficient of 23,000 M −1 ·cm −1 . Specific activity was calculated after determination of protein concentration according to the method of Bradford with Coomassie Brilliant Blue G250 staining against a bovine serum albumin calibration curve. All measurements were performed in triplicate, and the average value and the standard deviation were calculated with Microsoft Excel.
For determination of the pH profile of purified HPL CP-N , pH values from 6 to 9 were tested. The kinetic parameters K m and v max of HPL CP-N were analyzed with substrate concentrations ranging from 5 to 100 µM 13S-HPODE and 13S-HPOTE. The volumetric activity was measured in triplicate with Microsoft Excel, and the kinetic parameters with standard errors were calculated through nonlinear regression with the program GraphPad Prism 6.05.
The molecular weight of purified HPL CP-N was determined with size exclusion chromatography using a Superdex™ 200 Increase 10/300 column (Cytiva, USA). The column was equilibrated with 50 mM potassium phosphate buffer pH 7 with 0.5 M NaCl pH 7 and 0.1% Triton X-100. The column was calibrated with the gel filtration markers kit ranging from 29,000 to 700,000 Da (Sigma-Aldrich, USA), and the distribution coefficient K AV was calculated as where V e is elution volume, V 0 void volume, and V c volume of the column.
HPL CP-N was loaded onto the column, and the molecular weight was calculated from the calibration curve of K AV versus the logarithm of the protein molecular weight (y = − 0.3582x + 1.04). The oligomerization state of HPL CP-N was analyzed by comparing the calculated mass to the predicted monomer mass.

Synthesis of 12-Oxododecenoic with HPL CP-N
Reaction mixtures of 500 µl were prepared with 5 U HPL CP-N and 1 mM 13S-HPODE in 50 mM potassium phosphate buffer pH 6 with 1 M NaCl and 0.2% Triton X-100. Reaction mixtures were incubated for different time intervals up to 120 min. Reactions were terminated by adding 500 µl of 4 mg/ml sodium borohydride in 20 mM NaOH directly into the reaction vessels. Addition of alkaline sodium borohydride catalyzes the hydrogenation of 13S-HPODE, 12-oxododecenoic acid, and hexanal to the corresponding hydroxides. After 1 h of borohydride hydrogenation, the reaction mixtures were acidified to pH 2 with HCl and extracted with methyl tert-butyl ether (MTBE). All reactions were performed in triplicate. The solvent extracts were used for further GC analysis.

One-Pot Reactions with LOX-HPL and Lipase-LOX-HPL
One-pot reactions with LOX-1 from G. max and purified HPL CP-N were done with varying concentrations of linoleic acid dissolved in 50 mM potassium phosphate buffer pH 7.5 containing 0.5 M NaCl and 0.05% Triton X-100. 40 Units of LOX-1 were added to the linoleic acid containing buffer to a final volume of 400 µl to start the hydroperoxidation reaction. Four hundred microliters of buffer containing purified HPL CP-N (20 U/ml) was either added simultaneously or after a pre-incubation of LOX-1 and then reacted for additional 15 min in the presence of both enzymes (consecutive reaction mode). All reactions were done at 22 °C in open cups with vortexing in intervals. The reactions were terminated by addition of an equal volume of alkaline sodium borohydride, and products were extracted as described in the previous section.
One-pot reactions with lipase from P. fluorescens, LOX-1 from G. max, and purified HPL CP-N were done essentially as described above for the two-enzyme system with simultaneous and consecutive enzyme addition. Safflower oil corresponding to an initial concentration of 2 mM linoleic acid equivalent in a volume of 300 µl was dissolved in buffer and hydrolyzed with lipase (17.6 U/ml). Three hundred microliters of LOX-1 (100 U/ml) was added over 3 h in 12 portions of 25 µl, and after 3 h of reaction, 300 µl of HPL CP-N (20 U/ml) was added. Upon addition of LOX and HPL, the reaction mixture was diluted to a final linoleic acid equivalent concentration of 0.67 mM in a volume of 900 µl. The reactions were terminated by addition of an equal volume of alkaline sodium borohydride, and products were extracted as described in the "Synthesis of 12-Oxododecenoic with HPL CP-N " section.
Product quantification was done with a GC-2100 equipped with flame ionization detector (FID) (Shimadzu, Japan) using a MTX-Biodiesel TG column (length: 14 m, film thickness: 0.16 µm, inner diameter: 0.53 mm) from Restek GmbH (Germany) and helium as carrier gas. Samples of 1 µl were injected with a split ratio of 10, and a temperature gradient starting from 40 °C was used: 40 to 175 °C with 12 °C min −1 , 175 to 210 °C with 5 °C min −1 , 210 to 330 °C with 25 °C min −1 , and hold at 330 °C for 2 min. For product quantification, calibration curves were generated with the hydrogenated and silylated reference substances linoleic acid, 13S-HPODE, 12-hydroxydodecanoic acid, and hexanal.

Cloning of Papaya HPL and Optimization of Expression
For the development of a one-pot enzyme cascade with lipase, LOX, and HPL, high amounts of enzymes are needed. While lipases and lipoxygenases can be obtained easily in large quantities, HPLs are not commercially available due to their low stability and poor solubility in aqueous solutions. Purification of HPLs from plant materials is complicated and cost-intensive. Therefore, cloning and expression of HPL in microbial hosts are a suitable method for HPL synthesis [14,37].
On basis of the known sequence of industrially used guava HPL [23] (accession number AAK15070.1), we identified a related protein sequence from C. papaya (HPL CP ) by BLAST analysis. The putative HPL (accession number XP_021890218.1, Fig. S1) has an identity of 66.88% compared to the guava sequence. A phylogenetic tree was drawn with known HPLs from the CYP74B and CYP74C subfamily using ClustalX and NJplot (Fig. S3). Based on the phylogenetic relations, HPL CP can be assigned to the CYP74B subfamily that comprises 13 specific HPLs. The respective gene was synthesized by Bio-Cat GmbH (Germany) and cloned into the pET-28a( +) expression vector (Fig. S1). The enzyme was expressed in E. coli BL21(DE3) in LB medium. After harvest, the cell pellet was dissolved in 50 mM Tris buffer pH 7 with 0.05 M NaCl and 0.2% Triton X-100 and disrupted through sonication. Only a slight protein band was visible on SDS-PAGE (Fig. 2a), and activity of the full-length protein was low with 10 units per liter cultivation medium (Fig. 2b). Therefore, we tried to enhance activity of HPL CP by N-terminal truncation. The non-conserved N-terminal sequence of HPL CP was identified in a multiple sequence alignment with several known HPL sequences with ClustalW (Fig. S2) and removed through PCR-based subcloning (Fig. S1). After expression of HPL CP-N in E. coli BL21(DE3), a fourfold increase of activity was obtained in comparison to the full-length enzyme (Fig. 2b). A protein band was visible on SDS-PAGE at 53 kDa in the crude extract (CE) indicating an improved expression of the truncated enzyme (Fig. 2a). However, no protein band was visible in the soluble fraction (SF). Thus, it seems that most of the HPL protein was not present in a solubilized form. Therefore, the solubilization buffer was optimized starting from the initially used 50 mM Tris buffer pH 7 with 0.05 M NaCl (set to 100% relative activity). The effects of different buffer components, pH values, salts, and detergents on the final enzyme activity in the CE and SF were analyzed by one factor at a time variation (OFAT, Fig. S4a-d). Highest activity in the CE was obtained at a pH of 6 ( Fig. S4a), in the presence of potassium phosphate as buffering substance (Fig. S4b) and by addition of 1 M NaCl (Fig. S4c). In all experiments, the activity of the SE was significantly lower than that of the CE. An increase in activity of the SE was obtained by adding the detergent Triton X-100 (Fig. S4d). Combination of the best conditions (50 mM potassium phosphate buffer pH 6 with 1 M NaCl and 0.2% Triton X-100) increased the activity in the CE and SF more than eight-fold in comparison to the initial 50 mM Tris buffer pH 7 with 50 mM NaCl (Fig. S4e). Next, different cultivation media (Table S1) were analyzed for higher HPL CP-N expression. A significant increase in HPL expression was obtained by using the auto-inductive ZYM5052 medium with δ-aminolevulinic acid (Fig. 2c).
Summarizing, His6-tagged papaya HPL was successfully cloned into pET-28a( +) expression vector and expressed in E. coli BL21(DE3) as full-length and N-terminally truncated form. Though comparatively high HPL activity was reported for papaya fruit extracts [23], the enzyme has not been expressed recombinantly before. The expression level of full-length HPL CP was low on SDS-PAGE, while it increased in the expression of the truncated HPL CP-N . The reason for this in unclear, and we suggest that the deletion of the hydrophobic N-terminus must play a role due to the fact that the expression increased upon truncation. The activity of papaya HPL in the soluble fraction could be increased from initial 10 U/l with the full-length enzyme to 2700 U/l in shake flask cultures with the truncated HPL under optimized expression and solubilization conditions. As described for alfalfa or guava HPL [25,31], solubility of full-length HPL proteins seems to be a common problem resulting in low or no HPL activity. For papaya full-length HPL, we could only measure low activity as well, and since no corresponding protein band was visible on SDS-PAGE, it can be concluded that HPL expression of the full-length HPL CP was rather low. Expression of the truncated HPL resulted in higher activity and a visible protein band on SDS-PAGE. Therefore, we suggest that the hydrophobic N-terminus negatively influences the expression level of HPL CP . Addition of δ-aminolevulinic acid as heme precursor leads to an increase of soluble HPL expression in accordance to results obtained for beet, bell pepper, and olive HPL [38][39][40]. Additionally, buffer optimization had a significant effect on increasing the activity of HPL CP-N in the crude extract (CE) as well as in the soluble fraction (SF). A major factor was the addition of detergent Triton X-100, which solubilized HPL CP-N and increased activity in the SF. In accordance to our results, solubility and activity increase in the presence of detergents was reported for barley and barrel medic HPLs [41,42]. Although a more than 100-fold activity increase was obtained by optimization of cultivation and solubilization buffer, Bradford staining did not exhibit a HPL CP-N protein band in the SF (Fig. 2d). Thus, further optimization of expression and solubilization may improve volumetric HPL activity.

Purification and Biochemical Characterization of HPL CP-N
HPL CP-N was expressed under optimized conditions in 1.5 l scale to obtain sufficient amount of enzyme for downstream processing and characterization. In a typical process more than 7000 units, HPL CP-N was obtained after cell harvest, cell disruption, and solubilization in buffer. After centrifugation, a specific activity of 1.27 U/mg was obtained in the soluble fraction ( Table 2). Purification of the His6-tagged HPL CP-N was done with nickel affinity chromatography, and the purification process was analyzed by SDS-PAGE (Fig. 2d). A protein band was detected after affinity chromatography indicating significant HPL enrichment. Western blot was performed with an Anti-His antibody, confirming the identity of the His-tagged HPL CP-N protein (Fig. S5). The specific activity of HPL CP-N was increased more than 15-fold in the eluate fraction of the affinity chromatography (Table 2). According to gel filtration analysis, HPL CP-N has a calculated molecular weight of 225.9 kDa (Fig. S6). Based on the monomer molecular weight of 53 kDa from the truncated and His-tagged sequence, it can be presumed that HPL CP-N appears as a tetramer, which correlates with previous analyses of guava and sunflower HPL [23,43]. A pH analysis in the range Table 2 Fermentation and purification of HPL CP-N . BL21(DE3)/ pET-28a::Hishpl CP-N was cultivated in a 3 l bioreactor with a volume of 1.5 l ZYM5052 + δ-aminolevulinic acid, and cells were harvested after 24 h of cultivation of 6-9 revealed that the enzyme shows highest activity under slightly acidic conditions but retains approximately 40% of its maximum activity at pH 9 (Fig. S7). The kinetic parameters of the affinity chromatography enriched HPL CP-N were measured at pH 6 and calculated with GraphPad Prism 6.05 (Table 3, Fig. S8). HPL CP-N has a K m value of 140 µM for linoleic acid hydroperoxide (13S-HPODE) and 150 µM for linolenic acid hydroperoxide (13S-HPOTE) suggesting a relative similar substrate affinity. However, HPL CP-N exhibits a 1.55 fold higher catalytic efficiency (k cat /K m ) with 13S-HPOTE as substrate in comparison to 13S-HPODE, which indicates a weak preference of HPL CP-N towards 13S-HPOTE. In contrast, the truncated form of olive HPL showed a 22.5 fold increase of turnover with 13S-HPOTE compared to 13S-HPODE and a 5.5 fold higher catalytic efficiency (2.36 × 10 6 versus 0.43 × 10 6 s −1 ·M −1 ) [40]. Similarly, HPLs from Medicago truncatula and Solanum tuberosum showed a clear preference for 13S-HPOTE [42,44]. The comparably high catalytic activity of HPL CP-N with the substrate 13S-HPODE is beneficial for the cascade with lipase and LOX starting from safflower oil rich in linoleic acid.

Analysis of 12-Oxododeceneoic Acid Formation
HPL-catalyzed synthesis of green note aldehydes often neglected the by-product 12-oxo-9(Z)dodecenoic acid, though the compound may serve as polymer precursor. Reaction mixtures containing 1 mM 13S-HPODE were incubated up to 120 min with the soluble fraction of E. coli expressing HPL CP-N . Product formation was analyzed after sodium borohydride reduction and extraction. GC-MS peak assignment and GC quantification revealed rapid disappearance of 13S-HPODE and formation of a new peak at 11.9 min (Fig. 3). After 120 min, the peak at 11.9 min decreased significantly, and a new peak appeared at 12.2 min. The major signals were m/z 73 and 103 for the peak at 11.9 min and m/z 73 and 129 for the peak at 12.2 min (Fig. 3). This characteristic pattern of the silylated compounds points to the release of 12-oxo-9(Z)-dodecenoic acid and the consecutive isomerization to 12-oxo-10(E)-dodecenoic acid (traumatin). Comparative analysis with reference substances verified the fragmentation patterns (Fig. S10), which were also found by Noordermeer et al. [45].
In time-course experiments, it became apparent that the concentration of 12-oxo-9(Z)dodecenoic acid reached its maximum after 10 s and started to decrease rapidly ( Fig. 4a and  b). Up to 0.1 mM of the isomerization product 12-oxo-10(E)-dodecenoic acid (traumatin) was detected after 120 min (Fig. 4b). Incubation on ice slowed down the decrease of 12-oxo-9(Z)dodecenoic acid, but could not prevent consecutive reactions. The second reaction product hexanal proved to be significantly more stable, though a slight concentration decrease was monitored (Fig. 4c).
The isomerization product traumatin was described before for guava HPL [18]. Grechkin and Hamberg proposed the enol to be formed upon cleavage of the hemiacetal intermediate leading to either 9(Z)-or 10(E)-oxododecenoic acid tautomers [18]. Surprisingly, formation of traumatin was only detected in traces with purified HPL CP-N , and stability of 12-oxo-9(Z)dodecenoic acid was significantly higher (Fig. 4b). In our opinion, the differences in traumatin formation indicate secondary isomerization processes not specifically related to HPL (Fig. 5). Keto-enol tautomerism followed by double-bond shifting leads to traumatin formation. The formation of Schiff bases and isomerization of the double bond system via an imine-enamine tautomerism may be responsible for additional release of traumatin. In the presence of proteinrich crude extracts, an overall loss of reaction products was monitored suggesting Schiff base formation with, e.g., proteinogenic lysine residues. Thus, utilization of purified enzyme and rapid extraction seem to be necessary to quantitatively isolate 12-oxo-9(Z)-dodecenoic acid. Similarly in alfalfa HPL preparations, purified from its seeds, 12-oxo-10(E)-dodecenoic acid was found in the crude fraction, while 12-oxo-9(Z)-dodecenoic acid was the main product upon HPL purification [45]. Noordermeer et al. proposed a 3Z:2E-enal isomerase as isomerization factor, whereas our experiments with recombinant HPL strongly point to non-enzymatic isomerization. Nevertheless, a 3Z:2E-enal isomerase acting on hexenal was recently found in plants and cloned from cucumber [46,47].

One-Pot Enzyme Cascade of HPL CP-N Coupled with LOX-1 and Lipase
The development of enzyme cascades possesses significant advantages over successive reactions including a shift of equilibria without the need for isolation of intermediates [48,49]. In our previous work, we developed a cascade reaction for 13S-HPODE synthesis from safflower oil utilizing lipase from P. fluorescens, LOX-1 from soybeans, and catalase for in situ oxygen generation [11]. Now we wanted to couple lipase and LOX-1 reaction with HPL CP-N to prove the concept of a one-pot synthesis of 12-oxo-9(Z)-dodecenoic acid and hexanal from safflower oil. In contrast, the industrial process for volatile aldehyde production uses plant extracts in separate reactors for each reaction step [13]. First, LOX-1 reaction was combined with the HPL CP-N reaction in a one-pot experimental set-up. The pH optimum of LOX-1 is pH 9, whereas HPL CP-N is most active at pH 6, yet both enzymes exhibited sufficient activity at pH 7.5 (Fig. S7), and 13-regioselectivity of LOX-1 is still around 90% at pH 7.5 [11]. Linoleic acid with starting concentrations between 1 and 5 mM was pre-incubated with LOX-1 for 1 to 5 h, and then HPL CP-N was added for 15 min. Reaction mixtures were extracted and analyzed on GC. Small-scale reactions were conducted without active oxygen supply, which caused O 2 depletion at higher linoleic acid concentrations leading to a decrease of 13S-HPODE yield (Fig. 6a). Transformation of the 13S-HPODE to 12-oxo-9(Z)-dodecenoic acid with HPL CP-N yielded up to 80% transformation for the lowest linoleic acid concentration applied (Fig. 6b). At higher initial linoleic acid concentrations, HPL CP-N transformation was lower pointing to an incipient substrate inhibition, which was also described for other HPLs [14]. The comparison of simultaneous LOX-1 and HPL CP-N reaction for 3 h with consecutive addition of HPL CP-N after 3 h revealed that product recovery rates were low in simultaneous reaction mode (Fig. 7a). This observation was expected from our product incubation studies described in the previous section. In contrast, a good overall yield of 62% 12-oxo-9(Z)-dodecenoic acid was achieved by consecutive enzyme addition starting from 1 mM linoleic acid and HPL CP-N for 15 min.
Additionally, the combination of P. fluorescens lipase with LOX-1 and HPL CP-N was tested with simultaneous and consecutive addition of the enzymes (Fig. 7b). As control reactions, the transformation of safflower oil with lipase alone and with lipase and LOX was analyzed to monitor oil hydrolysis and hydroperoxidation. Again, simultaneous addition of all enzymes resulted in extremely low product recovery of less than 5%. Lipase-catalyzed hydrolysis of safflower oil equivalent to 2 mM linoleic acid yielded 66% hydrolysis, and around 2/3 of the liberated fatty acids were peroxidized by LOX-1. In contrast to the LOX-HPL two-enzyme system, significantly lower yields of 12-oxo-9(Z)-dodecenoic acid were obtained upon 15 min of HPL CP-N reaction. This observation indicates a rapid product transformation caused by addition of the lipase preparation. HPL CP-N reactions below 1 min proved to be sufficient for quantitative 13S-HPODE transformation (Fig. 4). Thus, the reaction of the three-enzyme system was terminated by rapid extraction 1 min after addition of HPL CP-N . With this methodology, a final yield of 43% 12-oxo-9(Z)-dodecenoic acid was obtained from safflower oil in the one-pot enzyme cascade (Fig. 7b).

Conclusions
Hydroperoxide lyase from papaya was cloned, functionally expressed as N-terminally truncated enzyme, purified and characterized biochemically. HPL CP-N was successfully applied for the synthesis of 12-oxo-9(Z)-dodecenoic acid from 13S-HPODE, and a one-pot enzyme cascade in combination with lipase and LOX-1 starting from safflower oil was established. Instability of the reactive product needs proper control of reaction conditions, and further research is needed to optimize process conditions for larger scale synthesis of 12-oxo-9(Z)dodecenoic acid.

Availability of Data
Data are available on request.