De Novo Biosynthesis of Vanillin in Fission Yeast (Schizosaccharomyces pombe) and Baker's Yeast (Saccharomyces cerevisiae)

Vanillin is one of the world''s most important flavor compounds, with a global market of 180 million dollars. Natural vanillin is derived from the cured seed pods of the vanilla orchid (Vanilla planifolia), but most of the world''s vanillin is synthesized from petrochemicals or wood pulp lignins. We have established a true de novo biosynthetic pathway for vanillin production from glucose in Schizosaccharomyces pombe, also known as fission yeast or African beer yeast, as well as in baker''s yeast, Saccharomyces cerevisiae. Productivities were 65 and 45 mg/liter, after introduction of three and four heterologous genes, respectively. The engineered pathways involve incorporation of 3-dehydroshikimate dehydratase from the dung mold Podospora pauciseta, an aromatic carboxylic acid reductase (ACAR) from a bacterium of the Nocardia genus, and an O-methyltransferase from Homo sapiens. In S. cerevisiae, the ACAR enzyme required activation by phosphopantetheinylation, and this was achieved by coexpression of a Corynebacterium glutamicum phosphopantetheinyl transferase. Prevention of reduction of vanillin to vanillyl alcohol was achieved by knockout of the host alcohol dehydrogenase ADH6. In S. pombe, the biosynthesis was further improved by introduction of an Arabidopsis thaliana family 1 UDP-glycosyltransferase, converting vanillin into vanillin β-d-glucoside, which is not toxic to the yeast cells and thus may be accumulated in larger amounts. These de novo pathways represent the first examples of one-cell microbial generation of these valuable compounds from glucose. S. pombe yeast has not previously been metabolically engineered to produce any valuable, industrially scalable, white biotech commodity.In 2007, the global market for flavor and fragrance compounds was an impressive $20 billion, with an annual growth of 11 to 12%. The isolation and naming of vanillin (3-methoxy-4-hydroxybenzaldehyde) as the main component of vanilla flavor in 1859 (8), and the ensuing chemical synthesis in 1874 (41), in many ways marked the true birth of this industry, and this compound remains the global leader in aroma compounds. The original source of vanillin is the seed pod of the vanilla orchid (Vanilla planifolia), which was grown by the Aztecs in Mexico and brought to Europe by the Spaniards in 1520. Production of natural vanillin from the vanilla pod is a laborious and slow process, which requires hand pollination of the flowers and a 1- to 6-month curing process of the harvested green vanilla pods (37). Production of 1 kg of vanillin requires approximately 500 kg of vanilla pods, corresponding to the pollination of approximately 40,000 flowers. Today, only about 0.25% (40 tons out of 16,000) of vanillin sold annually originates from vanilla pods, while most of the remainder is synthesized chemically from lignin or fossil hydrocarbons, in particular guaiacol. Synthetically produced vanillin is sold for approximately $15 per kg, compared to prices of $1,200 to $4,000 per kg for natural vanillin (46).An attractive alternative is bioconversion or de novo biosynthesis of vanillin; for example, vanillin produced by microbial conversion of the plant constituent ferulic acid is marketed at $700 per kilogram under the trade name Rhovanil Natural (produced by Rhodia Organics). Ferulic acid and eugenol are the most attractive plant secondary metabolites amenable for bioconversion into vanillin, since they can be produced at relatively low costs: around $5 per kilogram (37). For the bioconversion of eugenol or ferulic acid into vanillin, several microbial species have been tested, including gram-negative bacteria of the Pseudomonas genus, actinomycetes of the genera Amycolatopsis and Streptomyces, and the basidiomycete fungus Pycnoporus cinnabarinus (19, 23, 25, 27, 31, 34, 35, 36, 45, 48). In experiments where the vanillin produced was absorbed on resins, Streptomyces cultures afforded very high vanillin yields (up to 19.2 g/liter) and conversion rates as high as 55% were obtained (15). Genes for the responsible enzymes from some of these organisms were isolated and expressed in Escherichia coli, and up to 2.9 g/liter of vanillin were obtained by conversion of eugenol or ferulic acid (1, 3, 32, 49).Compared to bioconversion, de novo biosynthesis of vanillin from a primary metabolite like glucose is much more attractive, since glucose costs less than $0.30/kilogram (42). One route for microbial production of vanillin from glucose was devised by Frost and coworker Li (6, 20), combining de novo biosynthesis of vanillic acid in E. coli with enzymatic in vitro conversion of vanillic acid to vanillin. 3-Dehydroshikimic acid is an intermediate in the shikimate pathway for biosynthesis of aromatic amino acids, and the recombinant E. coli was engineered to dehydrate this compound to form protocatechuic acid (3,4-dihydroxybenzoic acid) and methylate this to form vanillic acid. The vanillic acid was subsequently converted into vanillin in vitro using carboxylic acid reductase isolated from Neurospora crassa. The main products of the in vivo step were protocatechuic acid, vanillic acid, and isovanillic acid in an approximate ratio of 9:4:1, indicating a bottleneck at the methylation reaction and nonspecificity of the OMT (O-methyltransferase) enzyme for the meta-hydroxyl group of protocatechuic acid. Serious drawbacks of this scheme are the lack of an in vivo step for the enzymatic reduction of vanillic acid, demanding the addition of isolated carboxylic acid reductase and costly cofactors such as ATP, NADPH, and Mg²⁺, and the generation of isovanillin as a contaminating side product.In this study, we have genetically engineered single-recombination microorganisms to synthesize vanillin from glucose, according to the metabolic route depicted in Fig. ​Fig.1.1. To avoid the synthesis of isovanillin as an undesired side product, a large array of OMTs was screened for the desired high substrate specificity, and an appropriate enzyme was identified. A synthetic version of an aromatic carboxylic acid reductase (ACAR) gene, optimized for yeast codon usage, was introduced to achieve the reduction step. The vanillin pathway was introduced into both Saccharomyces cerevisiae and Schizosaccharomyces pombe yeast, and significant levels of vanillin production were obtained in both organisms. Vanillin β-d-glucoside is the form in which vanillin accumulates and is stored in the fresh pod of the vanilla orchid (Vanilla planifolia). During the “curing” process of the pod, β-glucosidases are liberated and facilitate a partial conversion of the vanillin β-d-glucoside into vanillin. Upon consumption or application, the conversion of vanillin β-d-glucoside into free vanillin by enzymes in the saliva or in the skin microflora can provide for a slow-release effect that prolongs and augments the sensory event, as is the case for other flavor glycosides investigated, such as menthol glucoside (14, 16). In addition to the increased value of vanillin β-d-glucoside as an aroma or flavor compound, production of the glucoside in yeast may offer several advantages. Vanillin β-d-glucoside is more water soluble than vanillin, but most importantly, compounds such as vanillin in high concentrations are toxic to many living cells (4). It has been shown that glucosides of toxic compounds are less toxic to yeasts (24). We found this to be the case with vanillin and S. cerevisiae yeast as well. Thus, to facilitate storage and accumulation of higher vanillin yields, we introduced a step for vanillin glucosylation in S. pombe.Open in a separate windowFIG. 1.Biosynthetic scheme for de novo biosynthesis of vanillin in Schizosaccharomyces pombe and outline of the different vanillin catabolites and metabolic side products observed in different yeast strains and constructs. Gray arrows, primary metabolic reactions in yeast; black arrows, enzyme reactions introduced by metabolic engineering; diagonally striped arrows, undesired inherent yeast metabolic reactions.     

An informative set of SSLP markers and genomic profiles in the rat MHC,the <Emphasis Type="Italic">RT1</Emphasis> complex

Almost 10,000 single nucleotide polymorphisms (SNPs) had been identified in the RT1 complex, the major histocompatibility complex of the rat, but less than ∼0.5% have been characterized. In the context of the incomplete characterization of most SNPs, simple sequence length polymorphism (SSLP) marker development is still valuable for understanding the involvement of genes in the RT1 in controlling disease susceptibility, since SSLPs are user-friendly and cost-effective genetic markers in rat genome analysis. In this study, we developed a set of 67 SSLP markers, including 57 novel markers, to cover the entire RT1 complex and then created genetic profiles across 67 rat strains. These markers are located almost every 50 kb in the RT1 complex and show comparable polymorphism; the average number of alleles was 8.04 ± 3.44 and the average polymorphic rate was 71 ± 23%. Interestingly, markers failing to amplify polymerase chain reaction products were highly observed in all strains except for BN/SsNHsd, which suggests the existence of highly variable genomic sequences or genomic rearrangements in the RT1 region across rat strains. Based on the phylogenic tree and individual genotyping data, we identified 28 SSLP marker haplotypes in the RT1 region that roughly consisted of three genomic regions. These findings provided new insight into the genomic organization of the RT1 complex and we recognized the need of additional RT1 genome sequences in different strains. Owing to the accuracy and ease of determination, PCR-based SSLP genotyping could replace serological typing in genetic analyses and characterization of rat major histocompatibility. Electronic supplementary material  The online version of this article (doi:) contains supplementary material, which is available to authorized users. An erratum to this article can be found at     

Carbonic anhydrase inhibitors: transepithelial transport of thioureido sulfonamide inhibitors of the cancer-associated isozyme IX is dependent on efflux transporters

Sulfonamides and their derivatives inhibit the catalytic activity of carbonic anhydrases (CA, EC 4.2.1.1). Isozyme IX (CA IX) is a transmembrane isoform with the active site oriented toward the extracellular space. CA IX was recently shown to be a drug target, and it is highly overexpressed in hypoxic tumors with limited distribution in normal tissues. The present report deals with the drug design, synthesis, and biological investigation of a group of thioureido sulfonamides, which have been obtained by reaction of isothiocyanate-substituted aromatic sulfonamides with amines. These compounds have potent inhibitory properties against CA IX with K(I) values in the range of 10-37 nM and P(app)values > 0.34 x 10(-6) cm/s for the absorptive transepithelial transport in Caco-2 cells. In Caco-2 cells, one of these compounds (A6) was shown to be a substrate for efflux transporters such as P-glycoprotein (P-gp). P-gp activity is not likely to be rate-limiting for intestinal absorption, but might be useful when targeting hypoxic tumors expressing both P-gp and CA IX.     

Improved vanillin production in baker's yeast through <Emphasis Type="Italic">in silico</Emphasis> design

Background  

Vanillin is one of the most widely used flavouring agents, originally obtained from cured seed pods of the vanilla orchid Vanilla planifolia. Currently vanillin is mostly produced via chemical synthesis. A de novo synthetic pathway for heterologous vanillin production from glucose has recently been implemented in baker's yeast, Saccharamyces cerevisiae. In this study we aimed at engineering this vanillin cell factory towards improved productivity and thereby at developing an attractive alternative to chemical synthesis.     

CFD-aided design of a dynamic filter for mammalian cell separation

In the present work, a rotating disk filter was designed for mammalian cell separation with the aim of avoiding both cell damage and membrane fouling. Different geometric and operational variables of the rotating disk filter were studied using computational fluid dynamics (CFD) by varying rotor radius, rotor angle, membrane-rotor distance, and angular velocity. The combinations of these variables followed a statistical design, so that an analysis of the CFD results provided correlations describing the average shear stress on the membrane surface and the maximum shear stress in the whole module as a function of the variables studied. Based on these correlations, and on the shear resistance levels of Chinese hamster ovary (CHO) and baby hamster kidney (BHK) cell lines, which were investigated using a cone-and-plate viscosimeter, it was possible to determine the geometry and angular velocity that would minimize both cell damage and membrane fouling. After construction, the filter was tested in filtration experiments at increasing permeate fluxes. Cell viability remained >90% for the duration of the experiments (2.5 h), and no indication of fouling was observed. It was shown that the designed dynamic filter is able to effectively avoid both cell damage and membrane fouling, and thus can be used for mammalian cell harvesting and perfusion.     

Chemical synthesis of methyl 6'-alpha-maltosyl-alpha-maltotrioside and its use for investigation of the action of starch synthase II

The branched pentasaccharide methyl 6'-alpha-maltosyl-alpha-maltotrioside was chemically synthesised and investigated as a primer for particulate starch synthase II (SSII) using starch granules prepared from the low-amylose pea mutant lam as the enzyme source. For chemical synthesis, the trichloroacetimidate activation method was used to synthesise methyl O-(2,3,4,6-tetra-O-benzyl-alpha-D-glucopyranosyl)-(1-->4)-O-(2,3,6-tri-O-benzyl-alpha-D-glucopyranosyl)-(1-->6)-O-[(2,3,4,6-tetra-O-benzyl-alpha-D-glucopyranosyl-(1-->4)]-O-(2,3-di-O-benzyl-alpha-D-glucopyranosyl)-(1-->4)-2,3,6-tri-O-benzyl-alpha-D-glucopyranoside, which was then debenzylated to provide the desired branched pentasaccharide methyl 6'-alpha-maltosyl-alpha-maltotrioside as documented by 1H and 13C NMR spectroscopy. Using a large excess of the maltoside, the pentasaccharide was tested as a substrate for starch synthase II (SSII). Both of the non-reducing ends of methyl 6'-alpha-maltosyl-alpha-maltotrioside were extended equally resulting in two hexasaccharide products in nearly equal amounts. Thus, SSII catalyses an equimolar and non-processive elongation reaction of this substrate. Accordingly, the presence of the alpha-1,6 linkages does not dictate a specific structure of the pentasaccharide in which only one of the two non-reducing ends are available for extension.     

The in vitro substrate regiospecificity of recombinant UGT85B1, the cyanohydrin glucosyltransferase from Sorghum bicolor

The in vitro substrate specificity of UDP-glucose:p-hydroxymandelonitrile-O-glucosyltransferase from Sorghum bicolor (UGT85B1) was examined using a range of potential acceptor molecules, including cyanohydrins, terpenoids, phenolics, hexanol derivatives and plant hormones. Qualitative enzyme activity assays employing 20 different putative substrates were performed and 15 proved to be glucosylated using recombinant UGT85B1 isolated from Escherichia coli. K(m) and k(cat) values were determined for nine of these substrates including mandelonitrile, geraniol, nerol and beta-citronellol, 2-hydroxy-3-methoxybenzyl alcohol, 1-hexanol, cis-3-hexen-1-ol, 3-methyl-3-buten-1-ol and 3-methyl-2-buten-1-ol. UGT85B1 has a rather broad substrate specificity in vitro but shows regiospecificity, demanding the presence of a sterically unhindered hydroxyl group e.g. as part of a cyanohydrin function, as a primary alcohol or as a phenolic hydroxyl group and being influenced by the stereochemistry and/or interactive chemistry of the substituents on the hydroxyl-bearing carbon atom.     

The influence of domestic piglets' (<Emphasis Type="Italic">Sus scrofa</Emphasis>) age and test experience on the preference for the replayed maternal nursing vocalisation in a modified open-field test

The nursing vocalisation of lactating sows is an important part of the complex nursing and suckling behaviour of domestic pigs (Sus scrofa). It helps to lead the young through the several phases of a nursing episode. A total of 135 suckling piglets were investigated regarding their reactions to different vocalisations and sounds successively replayed in combined choice/open-field experiments. Two piglet samples were used to determine the impact of age (sample 1: weeks 1 and 5, n=93) and previous test experience of naive older piglets (sample 2: week 5, n=42) on their behavioural responses. In the 1st week after birth, the nursing vocalisation of sows released an initial generalised approach and contact response in the young, indicating high motivation to gain nutritional or social support. Close to the sound source, the piglets then strongly preferred the nursing vocalisation produced by their own mothers compared to that produced by another, unrelated and unfamiliar sow, or an artificial sound composed of similar frequencies as the nurse grunting, or a control without sound. However, at the end of the suckling period (5-week-old piglets) no clear differences in the reactions to the sounds could be identified. Moreover, the lack of a clear response at week 5 seems largely independent of any earlier test experience of the piglets. As well in the 1st as in the 5th week the piglets showed a decrease in open-field activity when sow grunting was present, indicating that the replay of the nursing vocalisation might have some calming effect. Communicated by K. Kotrschal     

PHOTOSYNTHESIS AND PHOTOSYNTHESIS-COUPLED RESPIRATION IN NATURAL BIOFILMS QUANTIFIED WITH OXYGEN MICROSENSORS1

Photosynthesis and respiration were analyzed in natural biofilms by use of O₂ microsensors. Depth profiles of gross photosynthesis were obtained from the rate of decrease in O₂ concentration during the first few seconds following extinction of light, and net photosynthesis of the photic zone was calculated from O₂ concentration gradients measured at steady state. Respiration within the photic zone was calculated as the difference between gross and net photosynthesis. Two types of biofilms were investigated: one dominated by diatoms, and one dominated by cyanobacteria. High O₂/CO₂ ratios caused increased respiration especially within the diatom biofilm, which could indicate that photorespiration was a dominant O₂-consuming process. The rate of respiration was constant within both biofilms during the first 4.6 s following extinction of light, even when respiration was stimulated by high O₂/CO₂ ratio. The assumption of a constant rate of respiration during the dark period is an essential one for the determination of gross photosynthetic activity by use of O₂ microsensors. We here present the first evidence to substantiate this assumption. The results strongly suggest that gross photosynthesis as measured by use of O₂ microsensors may include carbon equivalents that are subsequently lost through photorespiration. Computer modeling of photosynthesis profiles measured after 1.1, 1.6, and 2.6 s of dark incubation illustrated how the actual photosynthesis profile could have appeared if it had been possible to do the determination at time 0. Diffusion of O₂ during the up to 4.6-s long dark incubations did not affect gross photosynthetic rate when integrated over all depths, but the apparent vertical distribution of the photosynthetic activity was strongly affected.