Biotransformation of betulin to betulone by growing and resting cells of the actinobacterium Rhodococcus rhodochrous IEGM 66

The ability of Rhodococcus actinobacteria to transform betulin to betulone was proved and reported for the first time. Betulone, the product of regioselective oxidation of a 3β-hydroxyl group of betulin, is a useful intermediate in the synthesis of novel biologically active compounds. Of 56 strains of Rhodococcus tested, Rhodococcus rhodochrous IEGM 66 was selected because it had the highest betulin-transforming ability. It was shown that R. rhodochrous IEGM 66 growing cells transformed 0.5 g/L betulin to betulone with 45% conversion rate within 240 h. A substantial reduction in the time of betulin (0.5 g/L) biotransformation was achieved by using resting cells, which catalyzed the production of 75% betulone after 96 h. At higher initial betulin concentrations (1.0–3.0 g/L), resting cells catalyzed 40–60% betulone production within 24 h.     

Simultaneous production of single cell protein and killer toxin by Wickerhamomyces anomalus HN1-2 isolated from mangrove ecosystem

The yeast Wickerhamomyces anomalus (the previous name was Pichia anomala) HN1-2 isolated from the mangrove ecosystem was found to be able to produce high level of both killer toxin and single cell protein. When the killer yeast cells were grown by batch cultivation in 5-l fermentor, crude protein in the cells, cell mass, reducing sugar, and diameter of the inhibition zone reached 56.0 g per 100 g of cell dry weight, 7.3 g per liter, 9.5 g per liter, and 19.0 mm, respectively within 12 h and this yeast synthesized a large amount of the essential amino acids, such as lysine (7.8%), methionine (1.8%), and leucine (9.0%). The crude killer toxin produced by the killer yeast isolate HN1-2 could kill the cells of Lodderomyces elongisporus, Candida albicans, Metschnikowia bicuspidata, Pichia guilliermondii, Saccharomyces cerevisiae, Yarrowia lipolytica, and Kluyveromyces aestuarii, which were widely distributed in natural marine environments. The results also showed that the undesirable yeast could be avoided during cell growth of the killer yeast.     

Development and characterization of a new Bombyx mori cell line for protein expression

A Bombyx mori continuous cell line, designated DZNU-Bm-17, was established from larval ovaries. The cells were initially grown in MGM-448 insect cell culture medium supplemented with 10% fetal bovine serum and 3% heat inactivated B. mori hemolymph at 25 ± 1 °C and later adapted gradually to TNM-FH medium. Partially adhered refractive cells were the predominant cell type in the culture. The cells took about 1055 days to complete 100 passages in TNM-FH medium. The population doubling time of the cell line was about 30–34 h at 25 ± 1 °C. The cell population was largely diploid, but a few triploids and tetraploids were also observed. DNA profiles using simple sequence repeat loci established the differences between the DZNU-Bm-1, Bm-5, DZNU-Bm-12, DZNU-Bm-17, and BmN cell lines. The cell line was susceptible to budded virus of B. mori nucleopolyhedrovirus (BmNPV), and 85–92% of the cells harbored BmNPV with an average of 15 occlusion bodies/infected cell. The cells expressed the luciferase and green fluorescent proteins using the BmNPV bacmid vector. We suggest the usefulness of the DZNU-Bm-17 cell line for BmNPV-based baculoviral expression studies.     

Factors affecting the biotransformation of trimethylammonium compounds into l-carnitine by Escherichia coli

The biotransformation of d-carnitine and crotonobetaine into l-carnitine with wild and transformed E. coli strains under batch and continuous operation was optimised. In batch, the best conditions for the transformed strain were 30% oxygen saturation, a temperature of 41 °C and a minimal medium, whereas anaerobic cultures in either complex or minimal media at 37 °C and pH 7.5 were optimal for the wild strain. Studies on the expression of the enzymes involved in trimethylammonium metabolism showed that l-carnitine dehydratase activity was always higher than that of d-carnitine racemase. Experiments with the transformed strain in continuous cell-recycle reactors showed that, despite the higher productivity that could be achieved (0.65–1.2 g/L h), plasmid-bearing cells were segregated even when a selective medium was used. This fact was also confirmed by studying the evolution of the d-carnitine racemase level. Immobilization of the transformed strain in κ-carrageenan gels allowed continuous operation for l-carnitine production with no plasmid loss. In continuous processes with cell-retention systems, the wild strain showed higher productivity and stability than the transformed strain. Moreover, crotonobetaine was a better substrate for both strains used. Recycling with hollow-fiber cartridges provided the highest biomass level even though the l-carnitine dehydratase/biomass ratio was lower. However, membrane composition and cut-off had less influence on reactor performance as similar levels of productivity were attained. In spite of this, continuous processes attained a l-carnitine production as high as 11.5 g/L h as a result of the high enzyme induction and biomass levels.     

Use of Citrobacter koseri whole cells for the production of arabinonucleosides: A larger scale approach

Purine arabinosides are well known antiviral and antineoplastic drugs. Since their chemical synthesis is complex, time-consuming, and polluting, enzymatic synthesis provides an advantageous alternative. In this work, we describe the microbial whole cell synthesis of purine arabinosides through nucleoside phosphorylase-catalyzed transglycosylation starting from their pyrimidine precursors. By screening of our microbial collection, Citrobacter koseri (CECT 856) was selected as the best biocatalyst for the proposed biotransformation. In order to enlarge the scale of the transformations to 150 mL for future industrial applications, the biocatalyst immobilization by entrapment techniques and its behavior in different reactor configurations, considering both batch and continuous processes, were analyzed. C. koseri immobilized in agarose could be used up to 68 times and the storage stability was at least 9 months. By this approach, fludarabine (58% yield in 14 h), vidarabine (71% yield in 26 h) and 2,6-diaminopurine arabinoside (77% yield in 24 h), were prepared.     

Nicotinic acid bio-production by Microbacterium imperiale CBS 489-74: Effect of 3-cyanopyridine and temperature on amidase activity

3-Cyanopyridine (3-cnp) modulates via inactivation and/or inhibition, the amidase activity of the resting cells of Microbacterium imperiale CBS 489-74 which contained an in situ nitrile hydratase-amidase (NHase/AMase) cascade system suitable for catalyzing the bio-production of nicotinic acid form 3-cnp. The combined effect of 3-cnp concentration and temperature is investigated on the sole AMase activity by selectively inactivating the NHase activity. The study was performed in continuous stirred membrane reactors (CSMRs) fed with 100 mM nicotinamide solutions containing 25–200 mM 3-cnp at various temperatures. At 25–40 °C, the inactivation constant is negligible, even at high 3-cnp concentration, and the decrease in AMase activity is reversible. At 50 °C, a synergistic effect of temperature and 3-cnp inactivates AMase irreversibly, thus preventing a high yield being reached.     

Estudios de la viabilidad y la vitalidad frente al congelado de la levadura probiótica Saccharomyces boulardii: efecto del preacondicionamiento fisiológico

The aim of this study was to evaluate the vitality and viability of the probiotic yeast Saccharomyces boulardii after freezing/thawing and the physiological preconditioning effect on these properties. The results indicate that the specific growth rate (0.3/h^?1) and biomass (2-3 × 10⁸ cells/ml) of S. boulardii obtained in flasks shaken at 28 °C and at 37 °C were similar. Batch cultures of the yeast in bioreactors using glucose or sugar-cane molasses as carbon sources, reached yields of 0.28 g biomass/g sugar consumed, after 10 h incubation at 28 °C; the same results were obtained in fed batch fermentations. On the other hand, in batch cultures, the vitality of cells recovered during the exponential growth phase was greater than the vitality of cells from the stationary phase of growth. Vitality of cells from fed-batch fermentations was similar to that of stationary growing cells from batch fermentations. Survival to freezing at –20 °C and subsequent thawing of cells from batch cultures was 0.31% for cells in exponential phase of growth and 11.5% for cells in stationary phase. Pre-treatment of this yeast in media with water activity (a_w) 0.98 increased the survival to freezing of S. boulardii cells stored at –20 °C for 2 months by 10 fold. Exposure of the yeast to media of reduced a_w and/or freezing/thawing process negatively affected cell vitality. It was concluded that stress conditions studied herein decrease vitality of S. boulardii. Besides, the yeast strain studied presented good tolerance to bile salts even at low pH values.     

Enhanced ethanol production by continuous fermentation in a two-tank system with cell recycling

An experimental method for producing ethanol continuously was designed and tested with a cell-recycling two-tank system, which was composed of two fermentors, each of which was individually equipped with a settler for recycling flocculent yeast. This system was effective for the continuous fermentation of ethanol from sucrose at high cell-recycling (r = 0.8–0.9) and dilution (up to 0.48 h^?1) rates. The system has several advantages; the high cell concentration in the fermentors and relief of substrate and product inhibition. Thus, the enhanced productivity using this continuous fermentation with the two-tank cell-recycling system was significantly higher compared with that of the batch fermentation. The results indicate that increased recycling ratios caused an increase in biomass concentration and subsequently, product concentration in the tank. The ethanol productivity increased with the dilution rate, but higher dilution rates could render increasing amounts of sugar unconverted. Continuous fermentation with the sugar feed concentration of 160 g/l at r = 0.9 and dilution rate of 0.2 h^?1 achieved the highest productivity with less than 2% of the unconverted sugar in the product steam. Under the same cell recycling ratios a productivity range of 6.9–7.5 g/l h^?1 could be achieved with feeding concentrations of 80–200 g/l, while batch fermentation at these sugar concentrations led to productivities of 3.85–4.48 g/l h^?1.     

Comparison of batch,fed-batch and continuous well-mixed reactors for enzymatic hydrolysis of orange peel wastes

An alternative potential feedstock for bioethanol in the automotive sector is citrus peel waste (CPW), which can be processed through enzymatic hydrolysis and fermentation. The present work considers mathematical modeling of orange peel wastes (OPW) hydrolysis with the use of free enzymes and compares the performance of batch, fed-batch and continuous well-mixed reactors after introducing appropriate rate equations in dynamic mass balances. MATLAB^® was used for model implementation.Following the Michaelis–Menten approach, the authors used their own kinetic parameters for the pectin hydrolysis rate equation. The parameters were generated in an apposite experimental program for OPW hydrolysis to galacturonic acid with consideration of product inhibition; the corresponding values were obtained after Lineweaver–Burk linearization and are: r_max = 0.28 g/(L min), K_m = 19.80 g/L and K_IGA = 6.96 g/L, respectively. Vice-versa, the authors adopted the Kadam's group kinetic schemes and parameters for cellulose hydrolysis to cellobiose and glucose. The mathematical model of a well-mixed batch reactor was perfectly validated against the experimental results of OPW hydrolysis to galacturonic acid. In the case of a continuous well-mixed reactor, high dilution rates determine low conversion of OPW. The increased complication of fed-batch operation does not add advantages when compared to batch processing.     

Surfactant-mediated permeabilization of Pseudomonas putida KT2440 and use of the immobilized permeabilized cells in biotransformation

Surfactants were used to permeabilize cells of Pseudomonas putida KT2440 so as to maximize retention of the arginine deiminase (ADI) activity within the treated cells. The surfactants cetyltrimethylammoniumbromide (CTAB), sodium dodecyl sulfate (SDS) and Triton X100 were tested separately. Statistical models were developed for the effects on the ADI activity of the following factors: the concentration of the surfactant, the length of the treatment period and the concentration of the cells. For all surfactants, the concentration of cells was the most significant factor in influencing permeabilization. All permeabilization treatments used mild conditions (pH 7, 37 °C). The permeabilized cells were immobilized in alginate beads for the biotransformation of arginine to citrulline. The optimal conditions for immobilization and biotransformation were as follows: 2% (w/v, g/100 mL) sodium alginate, 100 g/L of treated cells, 40 mM arginine, pH 6.0, a temperature of 35 °C and an agitation speed of 150 rpm. The immobilized biocatalyst retained nearly 90% of its initial activity after nine cycles of repeated use in batch operations. In contrast, the freely suspended cells were barely active after the second use cycle.     

Solvent free biocatalytic synthesis of isoniazid from isonicotinamide using whole cell of Bacillus smithii strain IITR6b2

A biocatalytic route for the synthesis of isoniazid, an important first-line antitubercular drug, in aqueous system is presented. The reported bioprocess is a greener method, does not involve any hazardous reagent and takes place under mild reaction conditions. Whole cell amidase of Bacillus smithii strain IITR6b2 having acyltransferase activity was utilized for its ability to transfer acyl group of isonicotinamide to hydrazine–2HCl in aqueous medium. B. smithii strain IITR6b2 possessed 3 folds higher acyltransferase activity as compared to amide hydrolase activity and this ratio was further improved to 4.5 by optimizing concentration of co-substrate hydrazine–2HCl. Various key parameters were optimized and under the optimum reaction conditions of pH (7, phosphate buffer 100 mM), temperature (30 °C), substrate/co-substrate concentration (100/1000 mM) and resting cells concentration (2.0 mg_dcw/ml), 90.4% conversion of isonicotinamide to isoniazid was achieved in 60 min. Under these conditions, a fed batch process for production of isoniazid was developed and resulted in the accumulation of 439 mM of isoniazid with 87.8% molar conversion yield and productivity of 6.0 g/h/g_dcw. These results demonstrated that enzymatic synthesis of isoniazid using whole cells of B. smithii strain IITR6b2 might present an efficient alternative route to the chemical synthesis procedures without the involvement of organic solvent.     

Bioaugmentation of microbial communities in laboratory and pilot scale sequencing batch biofilm reactors using the TOL plasmid

The aim of this study was to investigate the effectiveness of bioaugmentation and transfer of plasmid pWWO (TOL plasmid) to mixed microbial populations in pilot and laboratory scale sequencing batch biofilm reactors (SBBRs) treating synthetic wastewater containing benzyl alcohol (BA) as a model xenobiotic. The plasmid donor was a Pseudomonas putida strain chromosomally tagged with the gene for the red fluorescent protein carrying a green fluorescent protein labeled TOL plasmid, which confers degradation capacity for several compounds including toluene and BA. In the pilot scale SBBR donor cells were disappeared 84 h after inoculation while transconjugants were not detected at all. In contrast, both donor and transconjugant cells were detected in the laboratory scale reactor where the ratio of transconjugants to donors fluctuated between 1.9 × 10^?1 and 8.9 × 10^?1 during an experimental period of 32 days. BA degradation rate was enhanced after donor inoculation from 0.98 mg BA/min prior to inoculation to 1.9 mg BA/min on the seventeenth day of operation. Survival of a bioaugmented strain, conjugative plasmid transfer and enhanced BA degradation was demonstrated in the laboratory scale SBBR but not in the pilot scale SBBR.     

Efficient production of glycyrrhetic acid 3-O-mono-β-d-glucuronide by whole-cell biocatalysis in an ionic liquid/buffer biphasic system

Hydrolysis of glycyrrhizin (GL) to glycyrrhetic acid 3-O-mono-β-d-glucuronide (GAMG) by whole-cell biocatalysts in a system containing non-conventional solvents was performed. Three whole-cell biocatalysts were used, including wild-type Penicillium purpurogenum Li-3 (w-PGUS) and recombinant strains Escherichia coli BL21 and Pichia pastoris GS115. The biotransformation of GL to GAMG by w-PGUS in a 1-butyl-3-methylimidazolium hexafluorophosphate ([Bmim]PF₆)/buffer biphasic system was the main focus of this study because w-PGUS showed a higher GAMG yield and a higher relative activity in this system than the other two whole-cell biocatalysts. Using the optimized reaction conditions determined as a pH 5.2 buffer, a 6.0 mM substrate concentration, a reaction temperature of 30 °C, and a 60 g/L (1.23 U/g) cell concentration, a GAMG yield of 87.63% was achieved after 60 h. After eight reaction cycles, [Bmim]PF₆ retained a high recovery percentage (85.48%)_[0], indicating the reusability of this IL. The biotransformation activity of w-PGUS was not significantly affected, even after two batch reaction cycles. Furthermore, the product GAMG and the byproduct glycyrrhetinic acid were spontaneously separated in the biphasic system. In conclusion, the combination of whole cells and ionic liquid is a promising approach for economical and industrial-scale production of GAMG.     

A novel disintegrin protein from Naja naja venom induces cytotoxicity and apoptosis in human cancer cell lines in vitro

Animal venoms and toxins are potential bioresources that have been known to mankind as a therapeutic tool for more than a century through folk and traditional medicine. The purified “disintegrin protein” (64 kDa) from the venom of the Indian cobra snake (Naja naja) exhibited cytotoxic effects of various types of human cancer cell lines such as breast cancer (MCF-7), lung cancer (A549) and liver cancer (HepG2). In vitro cytotoxicity, DNA fragmentation, an apoptotic assay and a cell cycle analysis were performed to evaluate the anticancer activity of disintegrin against the above cell lines. The IC₅₀ value of disintegrin was determined to be 2.5 ± 0.5 μg/mL, 3.5 ± 0.5 μg/mL, and 3 ± 0.5 μg/mL for the MCF-7, A549 and HepG2 cell lines respectively. Moreover, the increased distribution of G0/G1 and S phase led to decreased populations of cells in the G2/M phase of MCF-7, HepG2 and A549 cells.     

Cell adaptations of Rhodococcus rhodochrous IEGM 66 to betulin biotransformation

The findings of a comprehensive study on R. rhodochrous IEGM 66 and triterpenoid betulin interactions during its biotransformation were reported. In the presence of betulin, rhodococci were shown to form heterogeneous cell aggregates. The enhanced size of the aggregates from 12–15 μm to 25– 35 μm was consistent with the increase in betulin concentration from 0.5 to 3.0 g/L. The confocal laser scanning microscopy indicated a high (80.0%) level of rhodococcal viability during betulin biotransformation regardless of the betulin concentration. Experiments employing the combined confocal laser scanning and atomic force microscopy system confirmed that interactions between actinobacterial cells and betulin occur by direct contact. Transforming activities of the crude cell extracts from R. rhodochrous IEGM 66 were compared, and localization of enzymes catalyzing betulin oxidation to betulone was determined. Additionally the effects of betulin on fatty acid composition of rhodococci and their morphometric and morphofunctional characteristics during biotransformation were studied. Our findings could be used to develop approaches for enhanced betulin bioavailability, thus leading to improved biotransformation efficiency.     

Immobilized cell microchannel bioreactor for evaluating fermentation characteristics of mixed substrate consumption and product formation

An immobilized cell microchannel bioreactor was designed to test continuous fermentation. The fermentation set-up included a bottom hydrophilic quartz channel to immobilize cells using 0.4 wt% polyethyleneimine and a top channel designed to continuously remove metabolically generated carbon dioxide using hydrophobic polypropylene. To evaluate fermentation characteristics of immobilized cells, ethanol fermentation was carried out using Saccharomyces cerevisiae and Pichia stipitis. The immobilized cell microchannel bioreactor was used to identify long-term activity of immobilized S. cerevisiae cells. The continuous flow microchannel bioreactor was operated stably over a period of 1 month. The immobilized cell microchannel bioreactor was used to examine the characteristics cells that consumed mixed substrates. The concentration ratio of glucose to xylose for simultaneous utilization of hemicellulosic sugars was evaluated using the microchannel bioreactor and the results were compared with those obtained by using conventional batch fermentation with P. stipitis.     

Antitumor activity of resveratrol is independent of Cu(II) complex formation in MCF-7 cell line

Resveratrol (Rsv) is widely reported to possess anticarcinogenic properties in a plethora of cellular and animal models having limited toxicity toward normal cells. In the molecular level, Rsv can act as a suppressive agent for several impaired signaling pathways on cancer cells. However, Fukuhara and Miyata have shown a non-proteic reaction of Rsv, which can act as a prooxidant agent in the presence of copper (Cu), causing cellular oxidative stress accompanied of DNA damage. After this discovery, the complex Rsv-Cu was broadly explored as an antitumor mechanism in multiples tumor cell lines. The aim of the study is to explore the anticarcinogenic behavior of resveratrol–Cu(II) complex in MCF-7 cell line.Selectivity of Rsv binding to Cu ions was analyzed by HPLC and UV–VIS. The cells were enriched with concentrations of 10 and 50 µM CuSO₄ solution and treated with 25 µM of Rsv. Copper uptake after enrichment of cells, as its intracellular distribution in MCF-7 line, was scanned by ICP-MS and TEM-EDS. Cell death and intracellular ROS production were determined by flow cytometry.Different from the extracellular model, no relationship of synergy between Rsv–Cu(II) and reactive oxidative species (ROS) production was detected in vitro. ICP-MS revealed intracellular copper accumulation to both chosen concentrations (0.33 ± 0.09 and 1.18 ± 0.13 ppb) but there is no promotion of cell death by Rsv–Cu(II) complex. In addition, significant attenuation of ROS production was detected when cells were exposed to CuSO₄ after Rsv treatment, falling from 7.54% of ROS production when treated only with Rsv to 3.07 and 2.72% with CuSO₄.Based on these findings antitumor activity of resveratrol when in copper ions presence, is not mediated by Rsv-Cu complex formation in MCF-7 human cell line, suggesting that the antitumoral reaction is dependent of a cancer cellular model.     

Biodesulfurisation of DBT with Pseudomonas putida CECT5279 by resting cells: Influence of cell growth time on reducing equivalent concentration and HpaC activity

Dibenzothiophene (DBT) biodesulfurisation (BDS) route using a genetically modified organism, Pseudomonas putida CECT 5279, is studied. Tests of BDS with whole cells and with homogenized cells are carried out by taking samples of the cells during growth. The influence of the growth phases in the evolution of the intermediates of the 4S DBT desulfurising route is shown.Conversions of the five key compounds of the 4S route (DBT, DBTO, DBTO₂, HBPS and HBP) are measured. DBT conversion values are maximal with cells obtained after 30 h of growth time. HBP conversion values do not coincide with DBT conversion values, the maximum HBP production is obtained with cells grown for 10 h. A greater intermediate DBTO and DBTO₂ accumulation in broth is produced with cells obtained at 5 and 10 h of growth time. Nevertheless, the accumulation in broth of HBPS, another intermediate, is considerably lower than that observed with cells obtained at 23, 30 and 45 h of growth time.Also, the concentration of the reducing equivalents (NADH and FMNH₂) and flavin-oxido-reductase activity inside the cells is measured. This showed that the concentration of the reducing equivalents and the activity of the HpaC enzyme in the P. putida cytoplasm do not limit BDS rate.The influence of 4S compound transport across cellular membrane is studied by comparison of results obtained by resting cell assays (whole cells) and with homogenized cells assays (disrupted cells). The results show that there is no accumulation of any compound inside the cells, and that the transport rate across the cellular membrane does not limit the overall biodesulfurisation rate.     

Bioprocess engineering to produce 10-hydroxystearic acid from oleic acid by recombinant Escherichia coli expressing the oleate hydratase gene of Stenotrophomonas maltophilia

Microbial hydroxylation of long chain fatty acids has been extensively investigated. However, biotransformation productivity remains below ca. 1.0 g/g cell dry weight (CDW)/h under process conditions. In the present study, a highly efficient microbial hydroxylation process to convert oleic acid into 10-hydroxystearic acid was developed. A recombinant Escherichia coli expressing ohyA, the gene encoding oleate hydratase of Stenotrophomonas maltophilia, was used as the biocatalyst. Investigation of the ohyA expression and biotransformation conditions (e.g., inducer concentration, gene expression period before initiating biotransformation, mixing condition of reaction medium) enabled 10-hydroxystearic acid to accumulate to a final concentration of approximately 46 g/L in the culture medium. The specific product formation rate and product yield reached approximately 2.0 g/g CDW/h (i.e., 110 U/g CDW) and 91%, respectively. The specific product formation rate was more than 3-fold higher than those of a bioprocess using wild type Stenotrophomonas sp. cells. Additionally, the product of the whole-cell biotransformation was recovered at a yield of 70.9% and a purity of 99.7% via solvent fraction crystallization at low temperature. These results will contribute to developing a biological process for hydroxylation of oleic acid.     

Association between hypermethylation of DNA repetitive elements in white blood cell DNA and pancreatic cancer

Pancreatic cancer is a leading cause of cancer-related deaths worldwide. Methylation of DNA may influence risk or be a marker of early disease. The aim of this study was to measure the association between methylation of three DNA repetitive elements in white blood cell (WBC) DNA and pancreatic cancer.DNA from WBCs of pancreatic cancer cases (n = 559) and healthy unrelated controls (n = 603) were tested for methylation of the LINE-1, Alu and Sat2 DNA repetitive elements using MethyLight quantitative PCR assays. Odds ratios (ORs) and 95% confidence intervals (95%CI) between both continuous measures of percent of methylated sample compared to a reference (PMR) or quintiles of PMR and pancreatic cancer, adjusted for age, sex, smoking, BMI, alcohol and higher education, were estimated.The PMR for each of the three markers was higher in cases than in controls, although only LINE-1 was significantly associated with pancreatic cancer (OR per log unit = 1.37, 95%CI = 1.16–1.63). The marker methylation score for all three markers combined was significantly associated with pancreatic cancer (p-trend = 0.0006). There were no associations between measures of PMR and either presence of metastases, or timing of blood collection in relation to diagnosis, surgery, chemotherapy or death (all p > 0.1).We observed an association between methylation of LINE-1 in WBC DNA and risk of pancreatic cancer. Further studies are needed to confirm this association.