Responses of an American eel brain endothelial-like cell line to selenium deprivation and to selenite,selenate, and selenomethionine additions in different exposure media

The effect of selenium deprivation and addition on the American eel brain endothelial cell line (eelB) was studied in three exposure media: complete growth medium (L15/FBS), serum-free medium (L15), and minimal medium (L15/ex). L15/ex contains only galactose and pyruvate and allowed the deprivation of selenium on cells to be studied. In L15/ex, without any obvious source of selenium, eelB cells survived for at least 7 d, formed capillary-like structures (CLS) on Matrigel, and migrated to heal wounds. Three selenium compounds were added to cultures: selenite, selenate, and selenomethionine (SeMet). Adding selenite or selenate to eelB cell cultures for 24 h caused dose-dependent declines in cell viability, regardless of the exposure media. Although varying with exposure media and viability end point, selenite was approximately 70-fold more cytotoxic than selenate. By contrast, 24 h exposures to either dl- or l-SeMet in the three media caused little or no cytotoxicity. However for 7 d exposures in L15/ex, dl- and l-SeMet were very cytotoxic, even at the lowest tested concentration of 31 μM. By contrast in L15 and L15/FBS, cytotoxicity was only observed with 500 and 1000 μM l-SeMet. In L15/FBS, eelB continued to migrate and form CLS in the presence of SeMet but at 500 μM, cell migration appeared stimulated. As judged from a colony-forming assay over 14 d in L15/FBS, 500 and 1000 μM dl- and l-SeMet inhibited cell proliferation. Overall, the responses of eel cells to selenium depended on the selenium form, concentration, and exposure media, with responses to SeMet being most dependent on exposure media.     

<Emphasis Type="SmallCaps">l</Emphasis>-Serine overproduction with minimization of by-product synthesis by engineered <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis>

The direct fermentative production of l-serine by Corynebacterium glutamicum from sugars is attractive. However, superfluous by-product accumulation and low l-serine productivity limit its industrial production on large scale. This study aimed to investigate metabolic and bioprocess engineering strategies towards eliminating by-products as well as increasing l-serine productivity. Deletion of alaT and avtA encoding the transaminases and introduction of an attenuated mutant of acetohydroxyacid synthase (AHAS) increased both l-serine production level (26.23 g/L) and its productivity (0.27 g/L/h). Compared to the parent strain, the by-products l-alanine and l-valine accumulation in the resulting strain were reduced by 87 % (from 9.80 to 1.23 g/L) and 60 % (from 6.54 to 2.63 g/L), respectively. The modification decreased the metabolic flow towards the branched-chain amino acids (BCAAs) and induced to shift it towards l-serine production. Meanwhile, it was found that corn steep liquor (CSL) could stimulate cell growth and increase sucrose consumption rate as well as l-serine productivity. With addition of 2 g/L CSL, the resulting strain showed a significant improvement in the sucrose consumption rate (72 %) and the l-serine productivity (67 %). In fed-batch fermentation, 42.62 g/L of l-serine accumulation was achieved with a productivity of 0.44 g/L/h and yield of 0.21 g/g sucrose, which was the highest production of l-serine from sugars to date. The results demonstrated that combined metabolic and bioprocess engineering strategies could minimize by-product accumulation and improve l-serine productivity.     

Stereoisomeric Prodrugs to Improve Corneal Absorption of Prednisolone: Synthesis and <Emphasis Type="Italic">In Vitro</Emphasis> Evaluation

A series of stereoisomeric prodrugs have been designed to examine efficacy in generating higher corneal absorption relative to prednisolone. Prodrugs have been studied and identified with LC/MS/MS and NMR analyses. Prodrugs have been characterized for aqueous solubility, buffer stability, and cytotoxicity. Cellular uptake and permeability studies have been conducted across MDCK-MDR1 cells to determine prodrug affinity towards P-glycoprotein (P-gp) and peptide transporters. Enzyme-mediated degradation of prodrugs has been determined using Statens Seruminstitut rabbit cornea (SIRC) cell homogenates. Prodrugs exhibited higher aqueous solubility relative to prednisolone. Prodrugs circumvented P-gp-mediated cellular efflux and were recognized by peptide transporters. Prodrugs (DP, DDP) produced with d-isomers (d-valine) were significantly stable against both chemical and enzymatic hydrolyses. The order of degradation rate constants observed in chemical and enzymatic hydrolyses were in the same order, i.e., l-valine-l-valine-prednisolone (LLP)?>?l-valine-d-valine-prednisolone (LDP)?>?d-valine-l-valine-prednisolone (DLP)?>?d-valine-d-valine-prednisolone (DDP). Results obtained from this study clearly suggest that stereoisomeric prodrug approach is an effective strategy to overcome P-gp-mediated efflux and improve transcorneal permeability of prednisolone following topical administration.     

Safety of long-term dietary supplementation with <Emphasis Type="SmallCaps">l</Emphasis>-arginine in rats

This study was conducted with rats to determine the safety of long-term dietary supplementation with l-arginine. Beginning at 6 weeks of age, male and female rats were fed a casein-based semi-purified diet containing 0.61 % l-arginine and received drinking water containing l-arginine-HCl (0, 1.8, or 3.6 g l-arginine/kg body-weight/day; n = 10/group). These supplemental doses of l-arginine were equivalent to 0, 286, and 573 mg l-arginine/kg body-weight/day, respectively, in humans. After a 13-week supplementation period, blood samples were obtained from rats for biochemical analyses. Supplementation with l-arginine increased plasma concentrations of arginine, ornithine, proline, homoarginine, urea, and nitric oxide metabolites without affecting those for lysine, histidine, or methylarginines, while reducing plasma concentrations of ammonia, glutamine, free fatty acids, and triglycerides. l-Arginine supplementation enhanced protein gain and reduced white-fat deposition in the body. Based on general appearance, feeding behavior, and physiological parameters, all animals showed good health during the entire experimental period; Plasma concentrations of all measured hormones (except leptin) did not differ between control and arginine-supplemented rats. l-Arginine supplementation reduced plasma levels of leptin. Additionally, l-arginine supplementation increased l-arginine:glycine amidinotransferase activity in kidneys but not in the liver or small intestine, suggesting tissue-specific regulation of enzyme expression by l-arginine. Collectively, these results indicate that dietary supplementation with l-arginine (e.g., 3.6 g/kg body-weight/day) is safe in rats for at least 91 days. This dose is equivalent to 40 g l-arginine/kg body-weight/day for a 70-kg person. Our findings help guide clinical studies to determine the safety of long-term oral administration of l-arginine to humans.     

An optimized fed-batch culture strategy integrated with a one-step fermentation improves <Emphasis Type="SmallCaps">l</Emphasis>-lactic acid production by <Emphasis Type="Italic">Rhizopus oryzae</Emphasis>

In previous work, we proposed a novel modified one-step fermentation fed-batch strategy to efficiently generate l-lactic acid (l-LA) using Rhizopus oryzae. In this study, to further enhance efficiency of l-LA production through one-step fermentation in fed-batch cultures, we systematically investigated the initial peptone- and glucose-feeding approaches, including different initial peptone and glucose concentrations and maintained residual glucose levels. Based on the results of this study, culturing R. oryzae with initial peptone and glucose concentrations of 3.0 and 50.0 g/l, respectively, using a fed-batch strategy is an effective approach of producing l-LA through one-step fermentation. Changing the residual glucose had no obvious effect on the generation of l-LA. We determined the maximum LA production and productivity to be 162 g/l and 6.23 g/(l·h), respectively, during the acid production stage. Compared to our previous work, there was almost no change in l-LA production or yield; however, the productivity of l-LA increased by 14.3%.     

Production of <Emphasis Type="SmallCaps">d</Emphasis>-alanine from <Emphasis Type="SmallCaps">dl</Emphasis>-alanine using immobilized cells of <Emphasis Type="Italic">Bacillus subtilis</Emphasis> HLZ-68

Immobilized cells of Bacillus subtilis HLZ-68 were used to produce d-alanine from dl-alanine by asymmetric degradation. Different compounds such as polyvinyl alcohol and calcium alginate were employed for immobilizing the B. subtilis HLZ-68 cells, and the results showed that cells immobilized using a mixture of these two compounds presented higher l-alanine degradation activity, when compared with free cells. Subsequently, the effects of different concentrations of polyvinyl alcohol and calcium alginate on l-alanine consumption were examined. Maximum l-alanine degradation was exhibited by cells immobilized with 8% (w/v) polyvinyl alcohol and 2% (w/v) calcium alginate. Addition of 400 g of dl-alanine (200 g at the beginning of the reaction and 200 g after 30 h of incubation) into the reaction solution at 30 °C, pH 6.0, aeration of 1.0 vvm, and agitation of 400 rpm resulted in complete l-alanine degradation within 60 h, leaving 185 g of d-alanine in the reaction solution. The immobilized cells were applied for more than 15 cycles of degradation and a maximum utilization rate was achieved at the third cycle. d-alanine was easily extracted from the reaction solution using cation-exchange resin, and the chemical and optical purity of the extracted d-alanine was 99.1 and 99.6%, respectively.     

Efficient production of α-ketoglutarate in the <Emphasis Type="Italic">gdh</Emphasis> deleted <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> by novel double-phase pH and biotin control strategy

Production of l-glutamate using a biotin-deficient strain of Corynebacterium glutamicum has a long history. The process is achieved by controlling biotin at suboptimal dose in the initial fermentation medium, meanwhile feeding NH₄OH to adjust pH so that α-ketoglutarate (α-KG) can be converted to l-glutamate. In this study, we deleted glutamate dehydrogenase (gdh1 and gdh2) of C. glutamicum GKG-047, an l-glutamate overproducing strain, to produce α-KG that is the direct precursor of l-glutamate. Based on the method of l-glutamate fermentation, we developed a novel double-phase pH and biotin control strategy for α-KG production. Specifically, NH₄OH was added to adjust the pH at the bacterial growth stage and NaOH was used when the cells began to produce acid; besides adding an appropriate amount of biotin in the initial medium, certain amount of additional biotin was supplemented at the middle stage of fermentation to maintain a high cell viability and promote the carbon fixation to the flux of α-KG production. Under this control strategy, 45.6 g/L α-KG accumulated after 30-h fermentation in a 7.5-L fermentor and the productivity and yield achieved were 1.52 g/L/h and 0.42 g/g, respectively.     

Investigations on in vitro anti-carcinogenic potential of <Emphasis Type="SmallCaps">l</Emphasis>-carnosine in liver cancer cells

This study was carried out to investigate the anti-carcinogenic effect of l-carnosine in human carcinoma cells (SNU-423). The SNU-423 cancer cells were cultured at a density of 2 × 10⁴ cells/well in Dulbecco modified Eagle medium. After 24 h of adherence, the cells were treated with l-carnosine (0.2 and 1 mg/mL) for 48 h. Then, cell viability was assessed by sulforhodamine assay, while mitochondrial dysfunction was measured by fluorescence microscopy using chromatin-specific dye Hoechst 33258. Intracellular levels of ROS were assayed by fluorescence spectroscopy with 2′,7′-dichlorofluorescein diacetate (DCFDA). l-Carnosine significantly inhibited the growth of the SNU-423 cells (p < 0.05). The inhibitory effect of l-carnosine was confirmed by results from mitochondrial fragmentation assay. The relative fluorescent unit was increased in a dose-dependent manner by l-carnosine, with values of 79.43, 186.87 and 400.89 for 0.6, 0.8 and 1 mg/mL of l-carnosine, respectively (p < 0.05). These results demonstrate that l-carnosine exerts anti-carcinogenic effects in human liver cancer cells.     

An <Emphasis Type="SmallCaps">l</Emphasis>-Glutamine Transporter Isoform for Neurogenesis Facilitated by <Emphasis Type="SmallCaps">l</Emphasis>-Theanine

l-Theanine (=γ-glutamylethylamide) is an amino acid ingredient in green tea with a structural analogy to l-glutamine (l-GLN) rather than l-glutamic acid (l-GLU), with regards to the absence of a free carboxylic acid moiety from the gamma carbon position. l-theanine markedly inhibits [³H]l-GLN uptake without affecting [³H]l-GLU uptake in cultured neurons and astroglia. In neural progenitor cells with sustained exposure to l-theanine, upregulation of the l-GLN transporter isoform Slc38a1 expression and promotion of both proliferation and neuronal commitment are seen along with marked acceleration of the phosphorylation of mammalian target of rapamycin (mTOR) and relevant downstream proteins. Stable overexpression of Slc38a1 leads to promotion of cellular growth with facilitated neuronal commitment in pluripotent embryonic carcinoma P19 cells. In P19 cells stably overexpressing Slc38a1, marked phosphorylation is seen with mTOR and downstream proteins in a fashion insensitive to the additional stimulation by l-theanine. The green tea amino acid l-theanine could thus elicit pharmacological actions to up-regulate Slc38a1 expression for activation of the mTOR signaling pathway required for cell growth together with accelerated neurogenesis after sustained exposure in undifferentiated neural progenitor cells. In this review, I summarize a novel pharmacological property of the green tea amino acid l-theanine for embryonic and adult neurogenesis with a focus on the endogenous amino acid analog l-GLN. A possible translational strategy is also discussed on the development of dietary supplements and nutraceuticals enriched of l-theanine for the prophylaxis of a variety of untoward impairments and malfunctions seen in patients with different neurodegenerative and/or neuropsychiatric disorders.     

Characterization of aspartate kinase and homoserine dehydrogenase from <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> IWJ001 and systematic investigation of <Emphasis Type="SmallCaps">l</Emphasis>-isoleucine biosynthesis

Previously we have characterized a threonine dehydratase mutant TD^F383V (encoded by ilvA1) and an acetohydroxy acid synthase mutant AHAS^{P176S, D426E, L575W} (encoded by ilvBN1) in Corynebacterium glutamicum IWJ001, one of the best l-isoleucine producing strains. Here, we further characterized an aspartate kinase mutant AK^A279T (encoded by lysC1) and a homoserine dehydrogenase mutant HD^G378S (encoded by hom1) in IWJ001, and analyzed the consequences of all these mutant enzymes on amino acids production in the wild type background. In vitro enzyme tests confirmed that AK^A279T is completely resistant to feed-back inhibition by l-threonine and l-lysine, and that HD^G378S is partially resistant to l-threonine with the half maximal inhibitory concentration between 12 and 14 mM. In C. glutamicum ATCC13869, expressing lysC1 alone led to exclusive l-lysine accumulation, co-expressing hom1 and thrB1 with lysC1 shifted partial carbon flux from l-lysine (decreased by 50.1 %) to l-threonine (4.85 g/L) with minor l-isoleucine and no l-homoserine accumulation, further co-expressing ilvA1 completely depleted l-threonine and strongly shifted carbon flux from l-lysine (decreased by 83.0 %) to l-isoleucine (3.53 g/L). The results demonstrated the strongly feed-back resistant TD^F383V might be the main driving force for l-isoleucine over-synthesis in this case, and the partially feed-back resistant HD^G378S might prevent the accumulation of toxic intermediates. Information exploited from such mutation-bred production strain would be useful for metabolic engineering.     

Genome shuffling and high-throughput screening of <Emphasis Type="Italic">Brevibacterium flavum</Emphasis> MDV1 for enhanced <Emphasis Type="SmallCaps">l</Emphasis>-valine production

l-valine is an essential branched-amino acid that is widely used in multiple areas such as pharmaceuticals and special dietary products and its use is increasing. As the world market for l-valine grows rapidly, there is an increasing interest to develop an efficient l-valine-producing strain. In this study, a simple, sensitive, efficient, and consistent screening procedure termed 96 well plate-PC-HPLC (96-PH) was developed for the rapid identification of high-yield l-valine strains to replace the traditional l-valine assay. l-valine production by Brevibacterium flavum MDV1 was increased by genome shuffling. The starting strains were obtained using ultraviolet (UV) irradiation and binary ethylenimine treatment followed by preparation of protoplasts, UV irradiation inactivation, multi-cell fusion, and fusion of the inactivated protoplasts to produce positive colonies. After two rounds of genome shuffling and the 96-PH method, six l-valine high-yielding mutants were selected. One genetically stable mutant (MDVR2-21) showed an l-valine yield of 30.1 g/L during shake flask fermentation, 6.8-fold higher than that of MDV1. Under fed-batch conditions in a 30 L automated fermentor, MDVR2-21 accumulated 70.1 g/L of l-valine (0.598 mol l-valine per mole of glucose; 38.9% glucose conversion rate). During large-scale fermentation using a 120 m³ fermentor, this strain produced?>?66.8 g/L l-valine (36.5% glucose conversion rate), reflecting a very productive and stable industrial enrichment fermentation effect. Genome shuffling is an efficient technique to improve production of l-valine by B. flavum MDV1. Screening using 96-PH is very economical, rapid, efficient, and well-suited for high-throughput screening.     

Enhanced biocatalytic production of <Emphasis Type="SmallCaps">l</Emphasis>-cysteine by <Emphasis Type="Italic">Pseudomonas</Emphasis> sp. B-3 with in situ product removal using ion-exchange resin

Bioconversion of dl-2-amino-Δ²-thiazoline-4-carboxylic acid (dl-ATC) catalyzed by whole cells of Pseudomonas sp. was successfully applied for the production of l-cysteine. It was found, however, like most whole-cell biocatalytic processes, the accumulated l-cysteine produced obvious inhibition to the activity of biocatalyst and reduced the yield. To improve l-cysteine productivity, an anion exchange-based in situ product removal (ISPR) approach was developed. Several anion-exchange resins were tested to select a suitable adsorbent used in the bioconversion of dl-ATC for the in situ removal of l-cysteine. The strong basic anion-exchange resin 201 × 7 exhibited the highest adsorption capacity for l-cysteine and low adsorption for dl-ATC, which is a favorable option. With in situ addition of 60 g L^?1 resin 201 × 7, the product inhibition can be reduced significantly and 200 mmol L^?1 of dl-ATC was converted to l-cysteine with 90.4 % of yield and 28.6 mmol L^?1 h^?1 of volumetric productivity. Compared to the bioconversion without the addition of resin, the volumetric productivity of l-cysteine was improved by 2.27-fold using ISPR method.     

An efficient biocatalytic synthesis of imidazole-4-acetic acid

Objective

To develop a new and efficient biocatalytic synthesis method of imidazole-4-acetic acid (IAA) from l-histidine (l-His).

Results

l-His was converted to imidazole-4-pyruvic acid (IPA) by an Escherichia coli whole-cell biocatalyst expressing membrane-bound l-amino acid deaminase (ml-AAD) from Proteus vulgaris firstly. The obtained IPA was subsequently decarboxylated to IAA under the action of H₂O₂. Under optimum conditions, 34.97 mM IAA can be produced from 50 mM l-His, with a yield of 69.9%.

Conclusions

Compared to the traditional chemical synthesis, this biocatalytic method for IAA production is not only environmentally friendly, but also more cost effective, thus being promising for industrial IAA production.

     

<Emphasis Type="SmallCaps">l</Emphasis>-carnosine induces apoptosis/cell cycle arrest via suppression of NF-κB/STAT1 pathway in HCT116 colorectal cancer cells

l-carnosine, a dipeptide of the amino acids β-alanine and histidine, is found in various tissues, such as the central nervous system and skeletal muscles. Recently, l-carnosine has been reported to possess anti-tumor activity; however, the molecular mechanism underlying its activity in colorectal cancer is still unknown. Therefore, we investigated the effect of l-carnosine using a human colorectal cancer cell line, HCT116. Treatment with l-carnosine (0, 100, or 200 mM) for 24 h gradually reduced cellular proliferation according to immunochemistry and 7-aminoactinomycin D (7-AAD) analyses and induced G0/G1 phase arrest. In the RT-PCR analysis, l-carnosine decreased the mRNA levels of cell cycle-related genes in HCT116 cells. In the Western blot analysis, levels of the cyclin D1, BAX/Bcl-2, cleaved caspase-3, p21, and p53 proteins were significantly increased in cells treated with l-carnosine. We next determined whether STAT1/NF-κB pathway is involved in regulation of cell cycle arrest- and cell death-associated gene in HCT116. The l-carnosine treatment significantly inhibited the phosphorylation of STAT1 on Tyr701 and NF-κB p65 on Ser276 and Ser536, and then, we exogenously blocked the NF-κB phosphorylation using Bay 11-7082. Based on our findings, l-carnosine induces cell cycle arrest and apoptosis in human colorectal cancer cells by suppressing of NF-κB/STAT1 signaling.     

Increased productivity of <Emphasis Type="SmallCaps">l</Emphasis>-2-aminobutyric acid and total turnover number of NAD<Superscript>+</Superscript>/NADH in a one-pot system through enhanced thermostability of <Emphasis Type="SmallCaps">l</Emphasis>-threonine deaminase

Objective

To strengthen NADH regeneration in the biosynthesis of l-2-aminobutyric acid (l-ABA).

Results

l-Threonine deaminase (l-TD) from Escherichia coli K12 was modified by directed evolution and rational design to improve its endurance to heat treatment. The half-life of mutant G323D/F510L/T344A at 42 °C increased from 10 to 210 min, a 20-fold increase compared to the wild-type l-TD, and the temperature at which the activity of the enzyme decreased by 50% in 15 min increased from 39 to 53 °C. The mutant together with thermostable l-leucine dehydrogenase from Bacillus sphaericus DSM730 and formate dehydrogenase from Candida boidinii constituted a one-pot system for l-ABA biosynthesis. Employing preheat treatment in the one-pot system, the biosynthesis of l-ABA and total turnover number of NAD⁺/NADH were 0.993 M and 16,469, in contrast to 0.635 M and 10,531 with wild-type l-TD, respectively.

Conclusions

By using the engineered l-TD during endured preheat treatment, the one-pot system has achieved a higher productivity of l-ABA and total turnover number of coenzyme.

     

Biological production of <Emphasis Type="SmallCaps">l</Emphasis>-malate: recent advances and future prospects

As intermediates in the TCA cycle, l-malate and its derivatives have been widely applied in the food, pharmaceutical, agriculture, and bio-based material industries. In recent years, biological routes have been regarded as very promising approaches as cost-effective ways to l-malate production from low-priced raw materials. In this mini-review, we provide a comprehensive overview of current developments of l-malate production using both biocatalysis and microbial fermentation. Biocatalysis is enzymatic transformation of fumarate to l-malate, here, the source of enzymes, catalytic conditions, and enzymatic molecular modification may be concluded. For microbial fermentation, the types of microorganisms, genetic characteristics, biosynthetic pathways, metabolic engineering strategies, fermentation substrates, and optimization of cultivation conditions have been discussed and compared. Furthermore, the combination of enzyme and metabolic engineering has also been summarized. In future, we also expect that novel biological approaches using industrially relevant strains and renewable raw materials can overcome the technical challenges involved in cost-efficient l-malate production.     

Mitogen activated protein kinase 6 and MAP kinase phosphatase 1 are involved in the response of <Emphasis Type="Italic">Arabidopsis</Emphasis> roots to <Emphasis Type="SmallCaps">l</Emphasis>-glutamate

Key message

The function and components of l-glutamate signaling pathways in plants have just begun to be elucidated. Here, using a combination of genetic and biochemical strategies, we demonstrated that a MAPK module is involved in the control of root developmental responses to this amino acid.

Abstract

Root system architecture plays an essential role in plant adaptation to biotic and abiotic factors via adjusting signal transduction and gene expression. l-Glutamate (l-Glu), an amino acid with neurotransmitter functions in animals, inhibits root growth, but the underlying genetic mechanisms are poorly understood. Through a combination of genetic analysis, in-gel kinase assays, detailed cell elongation and division measurements and confocal analysis of expression of auxin, quiescent center and stem cell niche related genes, the critical roles of l-Glu in primary root growth acting through the mitogen-activated protein kinase 6 (MPK6) and the dual specificity serine–threonine–tyrosine phosphatase MKP1 could be revealed. In-gel phosphorylation assays revealed a rapid and dose-dependent induction of MPK6 and MPK3 activities in wild-type Arabidopsis seedlings in response to l-Glu. Mutations in MPK6 or MKP1 reduced or increased root cell division and elongation in response to l-Glu, possibly modulating auxin transport and/or response, but in a PLETHORA1 and 2 independent manner. Our data highlight MPK6 and MKP1 as components of an l-Glu pathway linking the auxin response, and cell division for primary root growth.

     

Synthesis of a tetra- and a trisaccharide related to an anti-tumor saponin “Julibroside J<Subscript>28</Subscript>” from <Emphasis Type="Italic">Albizia julibrissin</Emphasis>

Simple and convergent synthesis of a tetra- and a trisaccharide portions of an antitumor compound Julibroside J₂₈, isolated from Albizia julibrissin, that showed significant in vitro antitumor activity against HeLa, Bel-7402 and PC-3M-1E8 cancer cell lines is reported. The tetrasaccharide has been synthesized as its p-methoxyphenyl glycoside starting from commercially available d-glucose, l-rhamnose and l-arabinose. The trisaccharide part has been synthesized from commercially available N-acetyl d-glucosamine, d-fucose and d-xylose using simple protecting group manipulations. Sulfuric acid immobilized on silica has been used successfully as a Brönsted acid catalyst for the crucial glycosylation steps.     

Rational design and analysis of an <Emphasis Type="Italic">Escherichia coli</Emphasis> strain for high-efficiency tryptophan production

l-tryptophan (l-trp) is a precursor of various bioactive components and has great pharmaceutical interest. However, due to the requirement of several precursors and complex regulation of the pathways involved, the development of an efficient l-trp production strain is challenging. In this study, Escherichia coli (E. coli) strain KW001 was designed to overexpress the l-trp operator sequences (trpEDCBA) and 3-deoxy-D-arabinoheptulosonate-7-phosphate synthase (aroG ^fbr ). To further improve the production of l-trp, pyruvate kinase (pykF) and the phosphotransferase system HPr (ptsH) were deleted after inactivation of repression (trpR) and attenuation (attenuator) to produce strain KW006. To overcome the relatively slow growth and to increase the transport rate of glucose, strain KW018 was generated by combinatorial regulation of glucokinase (galP) and galactose permease (glk) expression. To reduce the production of acetic acid, strain KW023 was created by repressive regulation of phosphate acetyltransferase (pta) expression. In conclusion, strain KW023 efficiently produced 39.7 g/L of l-trp with a conversion rate of 16.7% and a productivity of 1.6 g/L/h in a 5 L fed-batch fermentation system.