Biocatalytic preparation of (S)-phenyl glycidyl ether using newly isolated Bacillus megaterium ECU1001

A bacterial strain (ECU1001) capable of utilizing phenyl glycidyl ether as sole carbon source and energy source was isolated from soil samples through two steps of screening and was identified as a Bacillus megaterium. The epoxide hydrolase from Bacillus megaterium ECU1001 was biosynthesized in parallel with cell growth and a maximum activity of 31.0 U/l was reached after 30 h of culture when the biomass (DCW) was 9.1 g/l. A temperature of 35°C and pH 8.0 were optimal for the bioconversion. The lyophilized whole cells of Bacillus megaterium ECU1001 could preferentially hydrolyze the (R)-enantiomer of phenyl glycidyl ether, yeilding (S)-epoxide and (R)-diol with high enantioselectivity (E=47.8). The (S)-enantiomer of the epoxide remained in the reaction mixture with >99.5% ee (enantiomeric excess) at a conversion of 55.9%. The substrate concentration could be increased up to 60 mM without affecting the ee and (S)-phenyl glycidyl ether could be obtained with an optical purity of 100% ee and 25.6% yield. Therefore, the method is potentially useful for the preparative resolution of epoxides.     

Large‐scale synthesis of tert‐butyl (3R,5S)‐6‐chloro‐3,5‐dihydroxyhexanoate by a stereoselective carbonyl reductase with high substrate concentration and product yield

To biosynthesize the (3R,5S)‐CDHH in an industrial scale, a newly synthesized stereoselective short chain carbonyl reductase (SCR) was successfully cloned and expressed in Escherichia coli. The fermentation of recombinant E. coli harboring SCR was carried out in 500 L and 5000 L fermenters, with biomass and specific activity of 9.7 g DCW/L, 15749.95 U/g DCW, and 10.97 g DCW/L, 19210.12 U/g DCW, respectively. The recombinant SCR was successfully applied for efficient production of (3R,5S)‐CDHH. The scale‐up synthesis of (3R,5S)‐CDHH was performed in 5000 L bioreactor with 400 g/L of (S)‐CHOH at 30°C, resulting in a space‐time yield of 13.7 mM/h/g DCW, which was the highest ever reported. After isolation and purification, the yield and d.e. of (3R,5S)‐CDHH reached 97.5% and 99.5%, respectively. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 33:612–620, 2017     

Optimization of polyhydroxybutyrate production from a wild type and two mutant strains of Rhodobacter sphaeroides using statistical method

Interaction studies using central composite design (CCD) gave the optimum concentrations of acetate at 4 g l(-1) and (NH4)2SO4 at 0.01 g l(-1) with an optimum temperature of 35 degrees C. Rhodobacter sphaeroides N20 gave the highest PHB (7.8 g l(-1)) and biomass (DCW) (8.2 g l(-1)) values compared to the wild type strain and the mutant strain U7. The CCD results predicted that the optimum medium for the mutant strain N20 consisted of 3.90 g l(-1) acetate, 0.01 g l(-1) (NH4)2SO4 at 33.5 degrees C (R2=0.985). Validation of this model by culturing the mutant strain in this optimum medium exhibited similar values of PHB (7.76 g l(-1)), biomass (8.32 g l(-1)) and the PHB content in the cell 93.2% of DCW. Similar amounts of PHB were also obtained in batch fermentations using a 5-l bioreactor. The effect of pH and aeration rate was also studied and the optimum values were found to be pH 7.0 with an aeration rate of 1.0 vvm. Under these optimal conditions, strain N20 produced the highest amount of PHB production (8.76 g l(-1)), PHB content (95.4% of DCW) as well as the product yield (Yp/x) (0.72). These results are the highest values ever obtained from photosynthetic bacteria reported so far.     

pH shift enhancement of Candida utilis pyruvate decarboxylase production

Pyruvate decarboxylase (PDC) catalyses the synthesis of asymmetric carbinols, e.g., chiral precursors for pharmaceuticals such as ephedrine and pseudoephedrine. The production of PDC by Candida utilis in a minimal medium was improved by manipulating the pH during fermentation in a 5 L bioreactor. At an aeration rate of 0.1 vvm with a stirrer speed of 300 rpm at constant pH 6, a specific PDC activity of 141 U/g dry cell weight (DCW) was achieved (average of two fermentations +/-13%). By allowing the yeast to acidify the growth medium from pH 6 to 2.9, the final specific PDC activity increased by a factor of 2.7 to 385 U/g DCW (average from 4 fermentations +/-16%). The effect of this pH drift on PDC production was confirmed by another experiment with a manual shift of pH from 6 to 3 by addition of 5 M sulfuric acid. The final PDC activity was 392 U/g DCW (average from two fermentations +/-5%). However, experiments with constant pH of 6, 5, 4, or 3 resulted in average specific activities of only 102 to 141 U/g DCW, suggesting that a transitional pH change rather than the absolute pH value was responsible for the increased specific PDC activity.     

Multi-copy expression and fed-batch production of Rhodotorula araucariae epoxide hydrolase in Yarrowia lipolytica

Epoxide hydrolases (EHs) of fungal origin have the ability to catalyze the enantioselective hydrolysis of epoxides to their corresponding diols. However, wild type fungal EHs are limited in substrate range and enantioselectivity. Additionally, the production of fungal epoxide hydrolase (EH) by wild-type strains is typically very low. In the present study, the EH-encoding gene from Rhodotorula araucariae was functionally expressed in Yarrowia lipolytica, under the control of a growth phase inducible hp4d promoter, in a multi-copy expression cassette. The transformation experiments yielded a positive transformant, with a final EH activity of 220 U/g dw in shake-flask cultures. Evaluation of this transformant in batch fermentations resulted in ~ 7-fold improvement in EH activity over the flask scale. Different constant specific feed rates were tested in fed-batch fermentations, resulting in an EH activity of 1,750 U/g dw at a specific feed rate of ~ 0.1 g/g/h, in comparison to enzyme production levels of 0.3 U/g dw for the wild type R. araucariae and 52 U/g dw for an Escherichia coli recombinant strain expressing the same gene. The expression of EH in Y. lipolytica using a multi-copy cassette demonstrates potential for commercial application.     

Nutritional requirements for the production of dithiolopyrrolone antibiotics by Saccharothrix algeriensis NRRL B-24137

The amino acid and humic acid requirements of Saccharothrix algeriensis NRRL B-24137 for growth and production of the dithiolopyrrolone antibiotics were studied in a semi-synthetic medium (SSM). Nature and concentration of amino acids and humic acid strongly influenced the growth and dithiolopyrrolone specific production.

The highest value of thiolutin (acetyl-pyrrothine) specific production was obtained in the presence of 1 g/l humic acid (336 mg/g DCW), and in the presence of 5 mM l-cystine (309 mg/g DCW) as compared to 19 mg/g DCW obtained with the control. Furthermore, thiolutin production was increased about six-fold, four-fold and three-fold in the presence of l-proline, l-glutamic acid and dl-histidine, respectively. In contrast, the production of thiolutin was reduced by addition of other amino acids such as l-glutamine, dl-ethionine, l-methionine and l-arginine. The highest value of isobutyryl-pyrrothine production was obtained in the presence of 2,6-diaminopimelic acid and l-lysine (7.8 and 1.0 mg/g DCW, respectively). However, the highest value of butanoyl-pyrrothine production was obtained in the presence of humic acid (6.6 mg/g DCW), followed by l-cysteine and l-proline (3.6 and 3.2 mg/g DCW, respectively). In addition, the maximum specific production of senecioyl-pyrrothine (29 mg/g DCW) and tigloyl-pyrrothine (21 mg/g DCW) was obtained in the presence of humic acid. We found that, except for isobutyryl-pyrrothine, production of all dithiolopyrrolones was favoured by addition of l-proline. The maximum specific production was obtained with l-proline at concentrations of 2.50 mM for thiolutin (133 mg/g DCW), 1.25 mM for senecioyl-pyrrothine, tigloyl-pyrrothine and butanoyl-pyrrothine production (29, 23 and 3.9 mg/g DCW, respectively). Production of all dithiolopyrrolones strongly decreased as the l-methionine or dl-ethionine concentration was increased in the culture medium.     

Production of a platelet aggregation inhibitor, salmosin, by high cell density fermentation of recombinant Escherichia coli

Optimal conditions for a high cell density fermentation were investigated in a recombinant Escherichia coli producing salmosin, a platelet aggregation inhibitor. The optimized carbon and nitrogen sources were glycerol 10 g/l, yeast extract 30 g/l, and bacto-tryptone 10 g/l, yielding the dry cell weight (DCW) of 10.61 g/l in a 500 ml flask culture. The late-stage induction with 1% L-arabinose in a 5 l jar fermentor showed the highest DCW of 65.70 g/l after 27 h of the fed-batch fermentation. Around 2,200 mg/l of the protein was expressed as an inclusion body that was then refolded to obtain the active salmosin of 96 mg/l. We also confirmed the inhibitory activity against platelet aggregation of the active salmosin from the high cell density fermentation.     

The genotoxicity of enantiomeric aliphatic epoxides

The (R)- and (S)-optical isomers of 9 epoxides, benzyloxymethyloxirane, epichlorohydrin, glycidol, glycidyl 3-nitrobenzenesulfonate, glycidyl 4-nitrobenzoate, glycidyl tosylate, styrene oxide, glycidyl 1-naphthyl ether and glycidyl 4-nitrophenyl ether, have been compared for their in vivo and in vitro genotoxicity. The in vitro short-term test employed was the Ames mutagenicity assay with Salmonella strain TA100. The in vivo tests were chromosomal aberrations (CA) as well as sister-chromatid exchange (SCE) in bone-marrow cells of mice following intraperitoneal administration of these epoxides. Differences in mutagenicity between isomers were established with TA100 for all the compounds. While 13 of the isomers were genotoxic compared to a negative control by CA measurements, only in the case of glycidyl 4-nitrobenzoate could a significant difference be found between isomers by this test. However, with SCE evaluations, differences were detected between the (R)- and (S)-isomers for all the pairs of compounds with the exception of those for benzyloxymethyloxirane and glycidyl 4-nitrophenyl ether. At least in part, differences in the patterns of genotoxicity among compounds can be related to their differences in reaction pathways.     

Coenzyme Q10 production in a 150-l reactor by a mutant strain of Rhodobacter sphaeroides

For the commercial production of CoQ₁₀, batch-type fermentations were attempted in a 150-l fermenter using a mutant strain of R. sphaeroides. Optimum temperature and initial aeration rate were found to be 30°C and 2 vvm, respectively. Under optimum fermentation conditions, the maximum value of specific CoQ₁₀ content was achieved reproducibly as 6.34 mg/g DCW after 24 h, with 3.02 g/l of DCW. During the fermentation, aeration shift (from the adequate aeration at the early growth phase to the limited aeration in active cellular metabolism) was a key factor in CoQ₁₀ production for scale-up. A higher value of the specific CoQ₁₀ content (8.12 mg/g DCW) was achieved in fed-batch fermentation and comparable to those produced by the pilot-scale fed-batch fermentations of A. tumefaciens, which indicated that the mutant strain of R. sphaeroides used in this study was a potential high CoQ₁₀ producer. This is the first detailed study to demonstrate a pilot-scale production of CoQ₁₀ using a mutant strain of R. sphaeroides.     

Biotransformation of the double bond in allyl glycidyl ether to an epoxide ring. Evidence from hemoglobin adducts in mice

Allyl glycidyl ether (AGE) is used industrially in the production of various epoxy resins. The compound is mutagenic and evidence for carcinogenicity in mice and rats has been reported. A previous study in mice showed that AGE reacts directly, without metabolic activation, with N-terminal valine in hemoglobin to form adducts (AGEVal). Metabolism of AGE may lead to formation of diglycidyl ether (I) through epoxidation of the double bond or 1-allyloxy-2,3-dihydroxypropane (II) through hydrolysis of the epoxide ring. 2,3-Dihydroxypropyl glycidyl ether (III) may be formed either by hydrolysis of I or epoxidation of II. The main aim of the present study was to investigate if AGE is metabolized to the reactive epoxides I or III by analysis of adducts with hemoglobin. Nine male mice (C3H/Hej) were administered AGE dissolved in tricaprylin, 4 mg/mouse, by intraperitoneal (i.p.) injection. Eleven male mice were administered 4 mg/mouse of AGE dissolved in acetone, by skin application. Adducts of I or III with N-terminal valine, N-(2-hydroxy-3-(2,3-dihydroxy)propyloxy)propylvaline (diOHPrGEVal), were demonstrated in mice administered AGE by i.p. injection. The levels were in the range 1600-5600 pmol/g globin. The level of diOHPrGEVal in mice administered AGE by skin application (n = 5) was below the detection limit of the analytical method, 20 pmol/g globin. The level of AGEVal, analyzed in mice administered AGE by skin application (n = 6), was about 20 pmol/g globin (median value), as compared with 1600 pmol/g globin previously found in mice administered AGE by i.p. injection. Neither AGEVal nor diOHPrGEVal were detected in control animals. Both adducts were analyzed using a modified Edman method for derivatization and using gas chromatography/tandem mass spectrometry for detection. The hydroxyl groups of the Edman derivative of diOHPrGEVal were protected by acetylation.     

Novel microbial epoxide hydrolases for biohydrolysis of glycidyl derivatives

Microbial isolates from biofilters and petroleum-polluted bioremediation sites were screened for the presence of enantioselective epoxide hydrolases active towards tert-butyl glycidyl ether, benzyl glycidyl ether, and allyl glycidyl ether. Out of 270 isolated strains, which comprised bacteria, yeasts, and filamentous fungi, four were selected based on the enantioselectivities of their epoxide hydrolases determined in biotransformation reactions. The enzyme of Aspergillus niger M200 preferentially hydrolyses (S)-tert-butyl glycidyl ether to (S)-3-tert-butoxy-1,2-propanediol with a relatively high enantioselectivity (the enantiomeric ratio E is about 30 at a reaction temperature of 28 °C). Epoxide hydrolases of Rhodotorula mucilaginosa M002 and Rhodococcus fascians M022 hydrolyse benzyl glycidyl ether with relatively low enantioselectivities, the former reacting predominantly with the (S)-enantiomer, the latter preferring the (R)-enantiomer. Enzymatic hydrolysis of allyl glycidyl ether by Cryptococcus laurentii M001 proceeds with low enantioselectivity (E = 3). (R)-tert-Butyl glycidyl ether with an enantiomeric excess (ee) of over 99%, and (S)-3-tert-butoxy-1,2-propanediol with an ee-value of 86% have been prepared on a gram-scale using whole cells of A. niger M200. An enantiomeric ratio of approximately 100 has been determined under optimised biotransformation conditions with the partially purified epoxide hydrolase from A. niger M200. The regioselectivity of this enzyme was determined to be total for both (S)-tert-butyl glycidyl ether and (R)-tert-butyl glycidyl ether.     

Use of fed-batch cultivation for achieving high cell densities for the pilot-scale production of a recombinant protein (phenylalanine dehydrogenase) in Escherichia coli

A fed-batch process for the high cell density cultivation of E. coli TG1 and the production of the recombinant protein phenylalanine dehydrogenase (PheDH) was developed. A model based on Monod kinetics with overflow metabolism and incorporating acetate utilization kinetics was used to generate simulations that describe cell growth, acetate production and reconsumption, and glucose consumption during fed-batch cultivation. Using these simulations a predetermined feeding profile was elaborated that would maintain carbon-limited growth at a growth rate below the critical growth rate for acetate formation (mu < mu(crit)). Two starvation periods are incorporated into the feed profile in order to induce acetate utilization. Cell concentrations of 53 g dry cell weight (DCW)/L were obtained with a final intracellular product concentration of recombinant protein corresponding to approximately 38% of the total cell protein. The yield of PheDH was 129 U/mL with a specific activity of 1.2 U/mg DCW and a maximum product formation rate of 0.41 U/mg DCW x h. The concentration of aectate was maintained below growth inhibitory levels until 3 h before the end of the fermentation when the concentration reached a maximum of 10.7 g/L due to IPTG induction of the recombinant protein.     

高对映选择性环氧化物水解酶产生菌的筛选及特性研究

从土壤中分离的芽孢杆菌Bacillus megaterium ECU1001所产五氧化物水解酶能高对映选择性水解缩水甘油苯基醚（对映选择率E值可达47.8）,当转化率为55.9%时,剩余的（S）－缩水甘油苯基醚的光学纯度（对映体过量值,ee）可达99.5%;当底物浓度提高到60mmol/L时,光学纯（S）－缩水基油苯基醚的收率达到25.6%。     

Enantioselective detoxication of optical isomers of glycidyl ethers

The detoxication of the enantiomers of glycidyl 4-nitrophenyl ether (GNPE), (?)-(R)- and (+)-(S)-GNPE, and glycidyl 1-naphthyl ether (GNE), (?)-(R)- and (+)-(S)-GNE, by rat liver glutathione transferase and epoxide hydrolase was studied. Enantioselectivity was observed with both enzymes favoring the (R)-isomers as determined by the formation of conjugate, diol, and remaining substrate measured by HPLC. Enantiomers of GNE were detoxified by cytosolic epoxide hydrolase but those of GNPE were not. Substantial nonenzymatically formed conjugates of enantiomers of GNPE were detected showing (S)-GNPE the more reactive of the pair. © 1993 Wiley-Liss, Inc.     

碱性果胶酶在重组毕赤酵母中高效表达的关键因素研究

为提高重组毕赤酵母生产碱性果胶酶的产量和生产强度, 在摇瓶条件下优化了重组毕赤酵母生产碱性果胶酶的关键因素。结果表明, 以下条件：初始甘油浓度40 g/L、初始甲醇浓度3.1 g甲醇/g DCW、每24 h添加0.51 g甲醇/g DCW、诱导表达周期72 h、250 mL三角瓶诱导培养基装液量30 mL、初始pH 6.0, 最适于菌体生长与产物表达。在此基础上, 7 L罐上通过恒速流加甘油进一步提高细胞密度, 诱导阶段甲醇采取前期恒速流加和后期DO-stat, 发酵结束菌体干重达80 g/L, 酶活为217 U/mL, 比摇瓶结果提高了66.2%。     

碱性果胶酶在重组毕赤酵母中高效表达的关键因素研究

为提高重组毕赤酵母生产碱性果胶酶的产量和生产强度,在摇瓶条件下优化了重组毕赤酵母生产碱性果胶酶的关键因素。结果表明,以下条件：初始甘油浓度40g／L、初始甲醇浓度3.1g甲醇／gDCW、每24h添加0.51g甲醇／gDCW、诱导表达周期72h、250mL三角瓶诱导培养基装液量30mL、初始pH6,0,最适于菌体生长与产物表达。在此基础上,7L罐上通过恒速流加甘油进一步提高细胞密度,诱导阶段甲醇采取前期恒速流加和后期DO-stat,发酵结束菌体干重达80g／L,酶活为217U／mL,比摇瓶结果提高了66.2％。     

Nutritional requirements for the production of dithiolopyrrolone antibiotics by Saccharothrix algeriensis NRRL B-24137

The amino acid and humic acid requirements of Saccharothrix algeriensis NRRL B-24137 for growth and production of the dithiolopyrrolone antibiotics were studied in a semi-synthetic medium (SSM). Nature and concentration of amino acids and humic acid strongly influenced the growth and dithiolopyrrolone specific production.The highest value of thiolutin (acetyl-pyrrothine) specific production was obtained in the presence of 1 g/l humic acid (336 mg/g DCW), and in the presence of 5 mM l-cystine (309 mg/g DCW) as compared to 19 mg/g DCW obtained with the control. Furthermore, thiolutin production was increased about six-fold, four-fold and three-fold in the presence of l-proline, l-glutamic acid and dl-histidine, respectively. In contrast, the production of thiolutin was reduced by addition of other amino acids such as l-glutamine, dl-ethionine, l-methionine and l-arginine. The highest value of isobutyryl-pyrrothine production was obtained in the presence of 2,6-diaminopimelic acid and l-lysine (7.8 and 1.0 mg/g DCW, respectively). However, the highest value of butanoyl-pyrrothine production was obtained in the presence of humic acid (6.6 mg/g DCW), followed by l-cysteine and l-proline (3.6 and 3.2 mg/g DCW, respectively). In addition, the maximum specific production of senecioyl-pyrrothine (29 mg/g DCW) and tigloyl-pyrrothine (21 mg/g DCW) was obtained in the presence of humic acid. We found that, except for isobutyryl-pyrrothine, production of all dithiolopyrrolones was favoured by addition of l-proline. The maximum specific production was obtained with l-proline at concentrations of 2.50 mM for thiolutin (133 mg/g DCW), 1.25 mM for senecioyl-pyrrothine, tigloyl-pyrrothine and butanoyl-pyrrothine production (29, 23 and 3.9 mg/g DCW, respectively). Production of all dithiolopyrrolones strongly decreased as the l-methionine or dl-ethionine concentration was increased in the culture medium.     

中国九省（区）农民超重肥胖的变化趋势及人口经济因素的影响

目的：分析1991—2015年我国18~64岁成年农民超重肥胖的变化趋势,并探讨人口经济因素对其的影响。方法：利用“中国健康与营养调查”1991—2015年间9轮队列研究的基本信息、社会经济因素和体格测量数据,选择18~64岁职业为“农民、渔民或猎人（以下简称农民）”的成年人作为研究对象。采用《中国成人超重和肥胖症预防控制指南》中的体质指数（BMI）切点值判定肥胖程度。应用多因素Logistic模型分析人口经济因素对肥胖发生危险性的影响。结果：1991—2015年间,我国农民超重和肥胖率均呈逐渐上升趋势,超重率从11.42%上升至35.80%,肥胖率从1.37%上升至13.92%。多因素Logistics分析结果显示,女性超重肥胖危险性高于男性。随着年龄的增加,农民超重肥胖危险性明显增加,35~49岁、50~64岁年龄组肥胖危险性高于18~34岁年龄组。北方及中部地区农民超重肥胖危险性高于南方地区。高收入水平的农民超重肥胖危险性高于低收入水平的农民。高中及以上文化程度的农民超重肥胖危险性高于小学及以下组。结论：性别、年龄、收入水平、地理位置是农民超重肥胖的重要影响因素。建议根据分布特征,将优质资源集中到中部、北方地区,并加强对中老年人进行营养知识和健康生活方式的宣教。同时也要关注高收入地区及男性农民的超重肥胖问题。     

Production of epoxide hydrolases in batch fermentations of <Emphasis Type="Italic">Botryosphaeria rhodina</Emphasis>

The filamentous fungus Botryosphaeria rhodina (ATCC 9055) was investigated related to its ability for epoxide hydrolase (EH) production. Epoxide hydrolase activity is located at two different sites of the cells. The larger part is present in the cytosol (70%), while the smaller part is associated to membranes (30%). In media optimization experiments, an activity of 3.5 U/gDW for aromatic epoxide hydrolysis of para-nitro-styrene oxide (pNSO) could be obtained. Activity increased by 30% when pNSO was added to the culture during exponential growth. An increase of enzyme activity up to 6 U/gDW was achieved during batch-fermentations in a bioreactor with 2.7 l working volume. Evaluation of fermentations with 30 l working volume revealed a relation of oxygen uptake rate to EH expression. Oxygen limitation resulted in a decreased EH activity. Parameter estimation by the linearization method of Hanes yielded Km values of 2.54 and 1.00 mM for the substrates S-pNSO and R-pNSO, respectively. vmax was 3.4 times higher when using R-pNSO. A protein purification strategy leading to a 47-fold increase in specific activity (940 U/mgProtein) was developed as a first step to investigate molecular and structural characteristics of the EH.     

Mutagenicities of glycidyl ethers for Salmonella typhimurium: relationship between mutagenic potencies and chemical reactivity

The lethal and mutagenic effects of ethyl, benzyl, 1-naphthylmethyl, 2-naphthylmethyl, 1-naphthylethyl, 2-naphthylethyl and 9-anthrylmethyl glycidyl ethers on Salmonella typhimurium (TA100, TA1535, TA98 and TA1538) were investigated. LD30-value became smaller with an increase in compound hydrophobicity. The mutagenicities of these compounds in TA100 increased in the order: 1-naphthylethyl glycidyl ether less than 2-naphthylethyl glycidyl ether less than benzyl glycidyl ether less than 2-naphthylmethyl glycidyl ether less than 1-naphthylmethyl glycidyl ether less than 9-anthrylmethyl glycidyl ether. 1-Naphthylmethyl and 2-naphthylmethyl glycidyl ethers were mutagenic toward TA1535. In TA98, 1-naphthylmethyl and 9-anthrylmethyl glycidyl ethers showed mutagenic activity and 9-anthrylmethyl glycidyl ether was more mutagenic than 1-naphthylmethyl glycidyl ether. 9-Anthrylmethyl glycidyl ether was also active in TA1538. In the reaction of glycidyl ethers with deoxyguanosine and related compounds, glycidyl ethers attacked at only N-7 of guanine. The alkylation rates of glycidyl ethers toward guanine residues in DNA were determined and the exciplex-formation ability of 7-substituted guanines was studied. The reactivity of glycidyl ethers with guanine residues in DNA has not provided a sufficient explanation for the variation in mutagenic potencies of glycidyl ethers.