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20世纪后期,生物工程迅速发展,给人类生活带来了巨大的变化。有人说,生物工程给人类带来了更大的希望,也有人说,它也会相应给人类带来灾难。学者们众说纷纭,褒贬不一。其中,植物转基因工程更是如此。植物转基因工程就是指通过基因枪等基因工程手段,将一种或几种外源基因转移到原本不具有这些基因的植物体内,并使之有效表达,产生相应性状,这种具有相应性状的植物称之为转基因植物。1983年,第一例转基因植物———转基因烟草问世。从此,转基因植物的研究就以惊人的速度发展,人类看到了更大的希望。1986年,抗虫和抗除草剂的转基因棉花首次进入田间实验,此后转基因植物在全球范围内飞速发展,种植面积不断扩大,给人类带来了非常明显的经济效益。在这同时,人类也注意到了它可能潜在着的一系列危害,即可能对环境产生不利影响,影响到生物多样性的保护和持续利用,并且对人类健康也可能有潜在的危害。1转基因植物的利用植物转基因工程的目的旨在通过导入有用的外源基因,获得转基因植物,用于植物的改良和有效成分的生产。目前在抗除草剂、抗虫、抗病、控制果实成熟以及植物生物反应器等方面已获得了一系列令人鼓舞的成果。1.1抗除草剂的转基因植物化学除草剂在现代农业中起着十分重要的作用,理想的除草剂必须具有高效、广谱的杀草能力,而对作物及人畜无害。但这样的除草剂成本越来越高,通过转基因技术,在作物中导入抗除草剂基因,获得抗除草剂作物,就能有效地解决这些问题,提高经济效益,使除草剂的应用更加方便。据报道,现已成功地获得了转aro A基因的番茄、油菜、大豆、杨树等,在田间试验中表现出对除草剂的良好抗性。1.2抗虫的转基因植物虫害对农业生产的危害非常严重,如能在植物体内转入抗虫基因,使植物获得抗虫性,增加对虫害的抵抗力,将对农业生产具有重要意义。基于这个目的,人们现已成功地将苏云金芽孢杆菌(Bacillusthurigiensis)的B.t毒蛋白基因转入了烟草、番茄、马铃薯、甘蓝、棉花、杨树等植物,使这些植物获得了抗虫性。1.3抗病的转基因植物据报道,将烟草花叶病毒(TMV)、黄瓜花叶病毒(CMV)、马铃薯X和Y病毒(PVX和PVY)、大豆花叶病毒(SMV)、苜蓿花叶病毒(AIMV)等病毒的外壳蛋白基因导入不同的植物体后,这些植物均获得了对相应病毒的抗性,这有望应用于农业生产。1.4抗逆的转基因植物68小分子化合物(如脯氨酸、甜菜碱、葡萄糖等)与植物忍受环境渗透胁迫的能力有关,人们若能将与脯氨酸或甜菜碱等合成有关的酶的基因克隆后转入植物,有望提高植物对干旱和盐碱等逆境的抗性。有报道说,人们现已成功地将相关基因转入了烟草、苜蓿、马铃薯等植物,使它们获得了对不同逆境的抗性。1.5植物生物反应器生产药物蛋白生物反应器(bioreactor)是指利用生物系统大规模生产有重要商业价值的外源蛋白质,用于医疗保健和科学研究。将不同的基因转入植物,可使转基因植物产生植物抗体、口服疫苗、植物药物和人类蛋白质等。据报道,到目前为止,人们已成功地获得了4种具有潜在医疗价值的植物抗体。2转基因植物存在的潜在风险2.1转基因作物对生态环境的潜在风险在耕地上栽种那些实验室里培育出来的转基因植物可能会对生态环境造成许多负面影响,转基因植物对非目标生物可能造成危害,转基因植物通过基因漂变对其它物种也可能产生有害影响。2.2对人类健康的潜在危害转基因食品里的新基因可能对消费者造成健康威胁,因为转基因植物是在传统植物接受了动物、植物、微生物的基因的基础上形成的,所以很可能对人类健康产生影响。人们正在关注这样一些问题:毒性问题、过敏反应问题、对抗生素的抵抗作用问题、营养问题等。3展望20世纪末生物技术取得了突飞猛进的发展,其涉及面之广、进展之快乃前所未有。从1986年美国批准第一个转基因作物进行大田试验,至1999年4月,已有4987个转基因作物被批准进行大田试验。自1994年至1999年五年间转基因农作物的种植面积增加了23倍多。美国的转基因抗虫棉花的种植面积已占其棉花总种植面积的13%。从发展趋势看,转基因植物将向多元化发展,例如品质改良、高产、抗逆(抗旱、抗寒、抗低光照、耐盐碱、耐瘠薄等)的基因工程发展。随着转基因技术的深入发展,人们也将把转基因植物应用到医药化工领域,建立基因工厂,从而利用转基因植物生产各种化工原料和药品,摆脱传统化工厂对日益短缺的化工原料的依赖和生产过程中对环境的严重污染。在21世纪,科学技术更加透明,更加公平,人们需要更多、更大的知情权,所以,国际社会对这个问题给予了极大关注,各国政府也高度重视。争论本身就是推动社会前进的动力。通过争论,弄清是非,避免破坏性后果的发生,这将推动科学技术沿着健康的道路发展前进。任何科学技术都不应该滥用,但也不能扼杀能给人类和社会创造巨大财富的技术成果。在应用植物转基因工程技术中,人类应该像对待其它科学技术一样,扬长避短,全面、理性地看问题,把握尺度,使植物转基因工程更加健康地发展,造福全人类。

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Synthesis of optically pure ethyl (S)-4-chloro-3-hydroxybutanoateby Escherichia coli transformant cells coexpressingthe carbonyl reductase and glucose dehydrogenase genes由共表达碳酰还原酶和葡萄糖脱氢酶的大肠杆菌转化细胞合成纯光学(S)-4-氯-3-羟基丁酸乙酯Abstract The asymmetric reduction of ethyl 4-chloro-3-oxobutanoate (COBE) to ethyl (S)-4-chloro-3-hydroxybutanoate((S)-CHBE) was investigated. Escherichia coli cells expressing both the carbonyl reductase (S1) gene from Candida magnoliae and the glucose dehydrogenase (GDH) gene from Bacillus megaterium were used as thecatalyst. In an organic-solvent-water two-phase system,(S)-CHBE formed in the organic phase amounted to 2.58 M (430 g/l), the molar yield being 85%. E. coli transformant cells coproducing S1 and GDH accumulated 1.25 M (208 g/l) (S)-CHBE in an aqueous monophase system by continuously feeding on COBE, which is unstable in an aqueous solution. In this case, the calculated turnover of NADP+ (the oxidized form of nicotinamide adenine dinucleotide phosphate) to CHBE was 21,600 mol/mol. The optical purity of the (S)-CHBE formed was 100% enantiomeric excess in both systems. The aqueous system used for the reduction reaction involving E. coli HB101 cells carrying a plasmid containing the S1 and GDH genes as a catalyst is simple. Furthermore, the system does not require the addition of commercially available GDH or an organic solvent. Therefore this system is highly advantageous for the practical synthesis of optically pure (S)-CHBE.本本篇文献研究了利用COBE不对称合成(S)-4-氯-3-羟基丁酸乙酯(CHBE)。大肠杆菌细胞作为催化剂同时表达了来自念珠菌属magnoliae的碳酰还原酶和来自巨大芽孢杆菌的葡萄糖脱氢酶基因。在水/有机溶剂两相体系中,(S)-CHBE在有机相中的浓度可以达到2.58M(430g/l),摩尔产率达到85%。大肠杆菌的副产物S1和GDH也达到了1.25M(208g/l),COBE在水相中不稳定,所以(S)-CHBE可以在水单相中不停的生成。在这种情况下,适当的从NADP+到CHBE的转变达到了21,600 mol/mol。所形成的CHBE的旋光度在这种体系中100%对映体过量。在水相中用携带含有S1和GDH基因质粒的E. coli HB101作为催化剂不对称还原是比较简单的。并且,这种体系并不额外需要商业GDH或者有机溶剂。因此,这种体系对于实际合成纯光学活性的(S)-CHBE是非常方便的。Optically active 4-chloro-3-hydroxybutanoic acid esters are useful chiral building blocks for the synthesis of pharmaceuticals. The (R)-enantiomer is a precursor of L-carnitine (Zhou et al. 1983), and (S)-enantiomer is an important starting material for hydroxymethylglutaryl- CoA (HMG-CoA) reductase inhibitors (Karanewsky et al. 1990). Many studies have described the microbial or enzymatic asymmetric reduction of 4-chloro-3-oxobutanoic acid esters (Aragozzini and Valenti 1992; Bare et al.1991; Hallinan et al. 1995; Patel et al. 1992; Shimizu et al. 1990; Wong et al. 1985) based on the reduction by baker’s yeast (Zhou et al. 1983).We have previously showed that Candida magnoliae AKU4643 cells reduced ethyl 4-chloro-3-oxobutanoate (COBE) to (S)-CHBE with an optical purity of 96% enantiomeric excess (e.e.) (Yasohara et al. 1999). As this yeast has at least three different stereoselective reductases (Wada et al. 1998, 1999a, b), the (S)-CHBE produced by this yeast was not optically pure. From among these three enzymes, an NADPH-dependent carbonyl reductase, designated as S1, was purified and characterized in some detail (Wada et al. 1998). We cloned and sequenced the gene encoding S1 and overexpressed it in Escherichia coli cells. This E. coli transformant reduced COBE to optically pure (S)-CHBE in the presence of glucose, NADP+, and commercially available glucose dehydrogenase (GDH) as a cofactor generator (Yasoharaet al. 2000). Here, we describe the construction of three E. coli transformants coexpressing the S1 from C. magnoliae and GDH from Bacillus megaterium genes and analyze the reduction of COBE catalyzed by these strains. Previous reports on the enzymatic reduction of COBE to (R)-CHBE with an optical purity of 92% e.e. (Kataoka et al. 1999; Shimizu et al. 1990) recommended an organic- solvent two-phase system reaction for an enzymatic or microbial reduction, because the substrate (COBE) is unstable in an aqueous solvent and inactivates enzymes. We examined the reduction of COBE to optically pure (S)-CHBE by E. coli transformants in a water monophase system reaction and discuss the possible use of this type of reaction system in industrial applications。具有旋光性的(S)-4-氯-3-羟基丁酸乙酯在药物制剂的合成中是重要的手性化合物。其右旋体是L-卡尼汀的前体,其左旋体是羟甲基戊二酰辅酶A还原酶抑制剂的起始材料。许多研究描述了以面包酵母为基础微生物或者酶的COBE的不对称还原。我们先前已经知道利用来自念珠菌属magnoliae AKU4643 细胞催化COBE生成光学纯度96%的CHBE。这种酵母至少有三种立体选择性的还原酶,这种酵母产生的CHBE并非纯光学的,在这三种酶之中,NADPH-依赖碳酰还原酶,我们克隆并测序编码S1的基因,并在大肠杆菌中过表达。大肠杆菌转化细胞在葡萄糖,NADP+和商业化的葡萄糖脱氢酶作为辅酶因子的启动子催化COBE生成纯光学的CHBE。我们构建这三种大肠杆菌转化细胞共表达来自的S1和来自巨大芽孢杆菌的GDH,并分析COBE被这几种菌株催化还原的反应机理。先前的报道表明,利用酶催化还原COBE生成CHBE光学纯度可达92%,也提到了因为底物(COBE)在水相中不稳定,并且酶容易钝化,所以利用酶或者微生物在有机溶剂/水两相体系中催化反应。我们研究了在水单相体系中由COBE还原生成纯光学的CHBE,还讨论了这种反应体系在工业应用中可能的用途。Materials and methodsBacterial strain and plasmids The E. coli strains used in this study were JM109 and HB101.Plasmid pGDA2, in which the GDH gene from B. megaterium is inserted into pKK223-3, was kindly provided by Professor I. Urabe, Osaka University (Makino et al. 1989). Plasmids pSL301 and pTrc99A were purchased from Invitrogen (USA), and Amersham Pharmacia Biotech (UK), respectively. Plasmids pUC19 and pSTV28 (Homma et al. 1995; Takahashi et al. 1995) were purchased from Takara Shuzo (Japan).材料和方法菌株和质粒本次实验中使用的大肠杆菌是JM109 and HB101。来自B. megaterium的GDH基因插入到Pkk233-3质粒中,而带有GDH基因片段的pGDA2质粒由到由大阪大学的urabe教授提供。质粒pSL301和 pTrc99A是由美国的Invitrogen公司和英国的公司分别购买的。质粒pUC19和pST28是由日本takara公司购买的。The recombinant plasmid used in this study was constructed as follows (Fig. 1): Plasmid pGDA2 was double-digested with EcoRI and PstI to isolate a DNA fragment of about 0.9 kilobase pairs (kb) including the GDH gene. This fragment was inserted into the EcoRI-PstI site of plasmid pSL301 to construct plasmid pSLG. Plasmid pSLG was double-digested with EcoRI and XhoI to isolate a DNA fragment of about 0.9 kb including the GDH gene.这次实验使用的重组质粒构建如下:质粒pGDA2 被EcoRI 和 PstI双酶切从而分离出一个大小约为0.9kb的包含有GDH基因的DNA片段。这个片段被插入到质粒Psl301的EcoRI-PstI酶切位点从而构建出质粒pSLG。质粒pSLG被EcoRI和XhoI To construct plasmid pNTS1G, this 0.9-kb fragment was inserted into the EcoRI-SalI site of pNTS1, which was constructed to overproduce S1 as described previously (Yasohara et al. 2000). To construct plasmid pNTGS1, plasmid pNTG was first generated. Two synthetic primers (primer 1, TAGTCCATATGTATAAAGATTTAG,and primer 2 TCTGAGAATTCTTATCCGCGTCCT) were prepared for polymerase chain reaction (PCR) using pGDA2 as the template. The PCR-generated fragment was double- digested with NdeI and EcoRI and then inserted into the NdeI EcoRI site of plasmid pUCNT, which was constructed from pUC19 and pTrc99A, as reported (Nanba et al. 1999), to obtain pNTG. To construct plasmid pNTGS1, two synthetic primers (primer 3, GCCGAATTCTAAGGAGGTTAATAATGGCTAAGAACTTCTCCAACG, and primer 4, GCGGTCGACTTAGGGAAGCGTGTAGCCACCGTC) were prepared using pUCHE, which contains the S1 gene as the template. The PCR-generated fragment was double-digested with EcoRI and SalI and then inserted into the EcoRI-SalI site of pNTG to obtain pNTGS1. Plasmid pNTS1G, pNTGS1 or pNTG was transformed into E. coli HB101.构建pNTS1是为了过表达前文所提到的S1,这个0.9kb大小的片段被插入到pNTS1的EcoRI-SalI酶切位点从而构建pNTS1G。为了构建质粒pNTGS1,首先需要构建pNTG。两个合成引物(引物1,TAGTCCATATGTATAAAGATTTAG和引物2,TCTGAGAATTCTTATCCGCGTCCT)和作为模板的pGDA2是PCR反应需要的。PCR得到的片段是由NdeI 和EcoRI双酶切和并插入到质粒pUCNT的NdeI EcoRI酶切位点来得到pNTG。根据报道,pUCNT是由pUC19和 pTrc99A构建而来。为了构建质粒pNTGS1,两个合成引物(引物 3, GCCGAATTCTAAGGAGGTTAATAATGGCTAAGAACTTCTCCAACG, and 引物 4, GCGGTCGACTTAGGGAAGCGTGTAGCCACCGTC),包括了S1基因作为模板。Pcr产物片段被EcoRI和SalI双酶切然后被插入到pntg的EcoRI-SalI酶切位点得到pntg1.质粒pNTS1G, pNTGS1或者 pNTG都是导入大肠杆菌HB101.Plasmid pGDA2 was double-digested with EcoRI and PstI to isolate a DNA fragment of about 0.9 kb including the GDH gene. To construct plasmid pSTVG, this fragment was inserted into the EcoRI-PstI site of plasmid pSTV28. Plasmid pSTVG was transformed into E. coli HB101. 质粒pGDA2被EcoRI 和 PstI双酶切得到包含GDH基因的0.9kb大小的DNA片段。为了构建pSTVG质粒,这个片段被插入到pSTV28质粒的EcoRI-PstI的酶切位点。pSTVG质粒被导入到E. coli HB101。Medium and cultivationThe 2×YT medium comprised 1.6% Bacto-tryptone, 1.0% yeastextract, and 0.5% NaCl, pH 7.0. E. coli HB 101 carrying pNTS1,pNTG, pNTS1G, or pNTGS1 was inoculated into a test tube containing2 ml 2×YT medium supplemented with 0.1 mg/ml ampicillin,followed by incubation at 37 °C for 15 h with reciprocal shaking.This preculture (0.5 ml) was transferred to a 500-ml shakingflask containing 100 ml 2×YT medium. The cells were cultivatedat 37 °C for 13 h with reciprocal shaking. E. coli HB101 carryingpNTS1 and pSTVG was similarly cultivated in 2×YT mediumsupplemented with 0.1 mg/ml ampicillin and 0.1 mg/ml chloramphenicol.培养基和培菌2*YT培养基 包含有1.6%细菌用胰蛋白胨,1.0%酵母提取物,0.5% NaCl,pH7.0.携带有pNTS1,pNTG, pNTS1G, 或 pNTGS1的大肠杆菌HB101被接种到有0.1mg/ml氨苄青霉素的2ml的2*YT培养基,37°C摇床15小时。将0.5ml菌液接种到100ml2*YT培养基的500ml烧瓶中。在37°C摇床培养13小时。携带有pNTS1 和 pSTVG质粒的大肠杆菌HB101在2*YT培养基中培养方法相似,只是培养基中要加入0.1 mg/ml的氨苄青霉素和 0.1 mg/ml的氯霉素。Preparation of cell-free extracts and the enzyme assay Cells were harvested from 100 ml of culture broth by centrifugation, suspended in 50 ml of 100 mM potassium phosphate buffer (pH 6.5), and then disrupted by ultrasonication. The cell debris was removed by centrifugation; the supernatant was recovered as the cell-free extract. Carbonyl reductase S1 activity (COBE-reducing activity) was determined spectrophotometically as follows: The assay mixture consisted of 100 mM potassium phosphate buffer (pH 6.5), 0.1 mM NADPH, and 1 mM COBE. The reactions were incubated at 30 °C and monitored for the decrease in absorbance at 340 nm. The assay mixture for GDH activity consisted of 1 M Tris-HCl buffer (pH 8.0), 100 mM glucose, and 2 mM NADP+. The reactions were incubated at 25 °C and monitored for the increase in absorbance at 340 nm. One unit of S1 or GDH was defined as the amount catalyzing the reduction of 1 μmol NADP+ or oxidation of 1 μmol NADPH per minute, respectively. Protein concentrations were measured with a proteinassay kit containing Coomassie brilliant blue (Nacalai Tesque, Japan),using bovine serum albumin as the standard (Bradford 1976).无细胞抽提液和酶鉴定将100ml培养液离心收获菌体,用50ml0.1mol/LpH为6.5的磷酸缓冲液悬浮,然后超声粉碎。细胞碎片通过离心可以去除,收集上层清液就是无细胞抽提物。碳酰还原酶S1的活性由分光光度计测量如下:测定的混合物包括:0.1mol/LpH6.5的磷酸二氢钾缓冲液,0.1mMNADPH和1mMCOBE。反应在30°C条件下反应,并且随时监测其在340nm处的吸光值。测GDH混合物包括:1M pH 8.0的Tris-HCl的缓冲液,100mM的葡萄糖,2mM的NADP+。反应在25°C下进行,监测其在340nm处的吸光值。一个单位S1或GDH被定义为每分钟催化还原1μmol NADP+或氧化1 μmol NADPH的量。蛋白质的测定通过含有考马斯亮蓝的蛋白质测定试剂利用牛血清白蛋白作为标准进行测定。Study of enzyme stabilityOne milliliter of 100 mM potassium phosphate buffer (pH 6.5) containing the cell-free extracts of E. coli HB101 carrying pNTS1 (S1: 20 U/ml) was mixed with an equal volume of each test organic solvent in a closed vessel. After the mixture was shaken at 30 °C for 48 h, the remaining enzyme activities in an aqueous phase were assayed as described above. The mixture, containing 100 mM potassium phosphate buffer (pH 6.5), S1 (20 U/ml), and various concentrations of CHBE, was incubated at 30 °C for 24 h in order to study the enzyme’s stability in the presence of CHBE.The remaining enzyme activities were assayed as described above.酶稳定性的研究一毫升含有含有pNTS1质粒的E. coli HB101的无细胞抽提液的100mM磷酸氢二钾缓冲液(pH6.5)与等体积的有机溶剂混合。混合物在30 °C震摇48小时后,水相中残留的酶活力即是上述的酶活力。COBE reduction with E. coli cells expressing the S1 gene and E. coli cells expressing GDH genes in a two-phase system reaction The reaction mixture comprised 15 ml culture broth of E. coli HB101 carrying pNTG, 17 ml culture broth of E. coli HB101 carrying pNTS1, 1.6 mg NADP+, 4 g glucose, 2.5 g COBE, 25 ml n-butyl acetate, and about 25 mg Triton X-100. The pH of the reaction mixture was controlled at 6.5 with 5 M sodium hydroxide. At 2 h, 1.25 g COBE and 2.5 g glucose were added to the reaction mixture. To compare the reaction by E. coli transformant coexpressing the GDH and S1 genes, 30 ml culture broth of E. coliHB101 carrying pNTS1G was used instead of culture broth of E. coli HB101 carrying pNTG and E. coli HB101 carrying pNTS1. Other components and the procedure were the same as described above.表达S1基因和GDH基因的大肠杆菌细胞在两相反应体系中的还原反应混合物包含有带有pNTG质粒的大肠杆菌HB101的菌液15ml,pNTS1质粒的大肠杆菌HB101的菌液17ml,1.6 mg NADP+,4 g葡萄糖,2.5g的COBE,25ml的n-butyl acetate丁酰醋酸盐和大约25mg的聚乙二醇辛基苯基醚Triton X-100。用5M的NaOH溶液将pH控制在6.5。在反应两小时后,加入1.25gCOBE和2.5g葡萄糖到该混合物中。比较大肠杆菌转化细胞共表达GDH和S1基因,携带有pNTS1G质粒的大肠杆菌HB10130ml菌液取代了携带有pNTG和pNTS1质粒的大肠杆菌HB101菌液。其他的成分和步骤和上述的方法相似。 COBE reduction to (S)-CHBE in a two-phase system reaction The reaction mixture contained 50 ml of culture broth of an E. coli HB101 transformant, 3.2 mg NADP+, 11 g glucose, 10 g COBE, 50 ml n-butyl acetate, and about 50 mg Triton X-100. The reaction mixture was stirred at 30 °C, and the pH was controlled at 6.5 with 5 M sodium hydroxide. Five grams of COBE/5.5 g glucose and 10 g COBE/11 g glucose were added to the reaction mixture at 3 h and 7 h, respectively; 3.2 mg NADP+ was added at 26 h.COBE在两相系统中还原生成(S)-CHBE反应混合物包含50ml E. coli HB101转化细胞的培养液,3.2mgNADP+,11g葡萄糖,10gCOBE,50ml丁酰醋酸,和大概50mg聚乙二醇辛基苯基醚Triton X-100.在30°C温度下将其混合均匀,并用5M的NaOH溶液将pH控制在6.5。在第3小时加入5gCOBE和5.5g葡萄糖或者在第7小时加入10gCOBE和11g葡萄糖,分别在第26小时加入3.2gNADP+。 COBE reduction to (S)-CHBE in an aqueous system reaction The reaction mixture was made up of 50 ml of culture broth of an E. coli HB101 transformant, 3.1 mg NADP+, 11 g glucose, and about 50 mg Triton X-100. The reaction mixture was stirred at 30 °C. Fifteen grams of COBE was fed continuously by means of a micro-feeding machine at a rate of about 0.02 g/min for about 12 h. The pH of the reaction mixture was controlled at 6.5 with 5 M sodium hydroxide. The reaction mixture was extracted with 100 ml ethyl acetate. The organic layer was dried over anhydrous sodium sulfate and then evaporated in vacuo. COBE在水相中还原成(S)-CHBE的反应反应的体系是由50ml大肠杆菌HB101转化细胞的菌液,3.1mgNADP+,11g葡萄糖和大约50mg聚乙二醇辛基苯基醚Triton X-100。反应混合物在30°C15mg的COBE通过微量添加机器以0.02 g/min的速率连续12小时恒定的加入到体系中。用5M的NaOH溶液将pH控制在6.5。反应混合物用100ml乙酸乙酯萃取。有机层用无水硫酸钠吸干,并在真空中脱水。Analysis The organic layer was obtained on centrifugation of the reaction mixture and was assayed for CHBE and COBE by gas chromatography. Optical purity of CHBE was analyzed by high-performance liquid chromatography (HPLC), as described previously (Yasohara et al. 1999).Enzymes and chemicals Restriction enzymes and DNA polymerase were purchased fromTakara Shuzo (Japan). COBE (molecular weight: 164.59) was purchasedfrom Tokyo Kasei Kogyo (Japan). Racemic CHBE (molecularweight: 166.60) was synthesized by reduction of COBE withNaBH4. All other chemicals used were of analytical grade andcommercially available.分析离心反应混合物得到的有机层通过气相色谱法测定其CHBE和COBE。COBE的光学纯度如前所述通过高效液相色谱法进行分析。酶和化学试剂限制性内切酶和DNA聚合酶由takara公司购得,COBE(分子量:164.59)由东京Tokyo Kasei Kogyo公司购得,消旋体CHBE(分子量166.6)通过COBE及NaBH4合成。所有其他化学试剂都是分析等级和商业化的试剂。Construction of E. coli transformants overproducing S1 and GDHTo express the carbonyl reductase S1 and GDH genes in the same E. coli cells, four expression vectors were constructed (Fig. 1). Plasmids pNTS1G and pNTGS1 contain the S1 gene from C. magnoliae, the GDH gene from B. megaterium, the lac promoter derived from pUC19, and the terminator derived from pTrc99A. Plasmid pNTS1 contains the S1 gene, the lac promoter derived from pUC19, and the terminator derived from pTrc99A. The enzyme activities in cell-free extracts of the E. coli transformants are shown in Table 1. E. coli HB101 cells carrying the vector plasmid pUCNT had no detectable S1 or GDH activity. E. coli HB101 carrying either pNTS1G or pNTGS1 showed S1 and GDH activity without isopropyl-β-D-thiogalactopyranoside (IPTG) induction. The S1 activities of these two transformants were lower than the GDH activities. To obtain a transformant whose S1 activity was equal to or greater than the level of GDH activity, we used a lower copy vector, pSTV28 (Homma et al. 1995; Takahashi et al. 1995), to express the GDH gene. It may be possible to raise the S1 activity by lowering the GDH activity. Plasmid pSTVG contains the GDH gene, the lac promoter, the chloramphenicol resistance gene, and the replicative origin derived from pACYC184 for compatibility with the plasmid pNTS1. In E. coli HB101 carrying pNTS1 and pSTVG, the S1 activity was higher than the GDH activity, but this GDHlevel may be too low to regenerate in a COBE reduction reaction as described below.过产生S1和GDH的大肠杆菌转化细胞的构建为了在同一大肠杆菌细胞中表达碳酰还原酶S1和GDH基因,要构建四个表达型载体。质粒pNTS1G 和 pNTGS1包含有来自C. magnoliae的S1基因,来自B. megaterium的GDH基因,来自pUC19的LAC启动子,从pTrc99A的来的终止子,质粒pNTS1包含有S1基因,来自pUC19的LAC启动子,从pTrc99A的来的终止子。在大肠杆菌转化细胞的无细胞抽提物的酶活力如表一所示。携带有运输质粒pUCNT的大肠杆菌细胞无法检测到其S1和GDH活性。携带有pNTS1G 或 pNTGS1质粒在没有IPTG的诱导下有S1和GDH的活性。在这两个转化菌种中,S1的活力小于GDH的活力。为了得到S1活性等于或者大于GDH的大肠杆菌转化菌株,我们使用低拷贝的载体pSTV28,来表达GDH基因。它可能可以通过降低GDH的活性从而提高S1的活性。质粒pSTVG包含有GDH基因,lac启动子,和氯霉素抗性基因,以及与pNTS1具有相容性的从pACYC184得来的复制起始位点。在携带有pNTS1和pSTVG的大肠杆菌转化细胞中,S1的活性要高于GDH的活性,但是GDH的活性可能会太低而在COBE还原反应中不能再生。 太长了,字数有限制,所以不能发完。分数我无所谓啦,我很少登录的。这应该算是基因工程的吧,是我以前自己翻的,不是很好。如果你要的话可以联系我的邮箱。

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海洋嗨阳

基因工程技术的现状和前景发展 【摘要】从20世纪70年代初发展起来的基因工程技术,经过30多年来的进步与发展,已成为生物技术的核心内容。许多科学家预言,生物学将成为21世纪最重要的学科,基因工程及相关领域的产业将成为21世纪的主导产业之一。基因工程研究和应用范围涉及农业、工业、医药、能源、环保等许多领域。【关键词】基因工程技术;前景;现状一、基因工程应用于植物方面 农业领域是目前转基因技术应用最为广泛的领域之一。农作物生物技术的目的是提高作物产量,改善品质,增强作物抗逆性、抗病虫害的能力。基因工程在这些领域已取得了令人瞩目的成就。由于植物病毒分子生物学的发展,植物抗病基因工程也也已全面展开。自从发现烟草花叶病毒(TMV)的外壳蛋白基因导入烟草中,在转基因植株上明显延迟发病时间或减轻病害的症状,通过导入植物病毒外壳蛋白来提高植物抗病毒的能力,已用多种植物病毒进行了试验。在利用基因工程手段增强植物对细菌和真菌病的抗性方面,也已取得很大进展。植物对逆境的抗性一直是植物生物学家关心的问题。由于植物生理学家、遗传学家和分子生物学家协同作战,耐涝、耐盐碱、耐旱和耐冷的转基因作物新品种(系)也已获得成功。植物的抗寒性对其生长发育尤为重要。科学家发现极地的鱼体内有一些特殊蛋白可以抑制冰晶的增长,从而免受低温的冻害并正常地生活在寒冷的极地中。将这种抗冻蛋白基因从鱼基因组中分离出来,导入植物体可获得转基因植物,目前这种基因已被转入番茄和黄瓜中。随着生活水平的提高,人们越来越关注口味、口感、营养成分、欣赏价值等品质性状。实践证明,利用基因工程可以有效地改善植物的品质,而且越来越多的基因工程植物进入了商品化生产领域,近几年利用基因工程改良作物品质也取得了不少进展,如美国国际植物研究所的科学家们从大豆中获取蛋白质合成基因,成功地导入到马铃薯中,培育出高蛋白马铃薯品种,其蛋白质含量接近大豆,大大提高了营养价值,得到了农场主及消费者的普遍欢迎。在花色、花香、花姿等性状的改良上也作了大量的研究。二、基因工程应用于医药方面目前,以基因工程药物为主导的基因工程应用产业已成为全球发展最快的产业之一,发展前景非常广阔。基因工程药物主要包括细胞因子、抗体、疫苗、激素和寡核甘酸药物等。它们对预防人类的肿瘤、心血管疾病、遗传病、糖尿病、包括艾滋病在内的各种传染病、类风湿疾病等有重要作用。在很多领域特别是疑难病症上,基因工程工程药物起到了传统化学药物难以达到的作用。我们最为熟悉的干扰素(IFN)就是一类利用基因工程技术研制成的多功能细胞因子,在临床上已用于治疗白血病、乙肝、丙肝、多发性硬化症和类风湿关节炎等多种疾病。 目前,应用基因工程研制的艾滋病疫苗已完成中试,并进入临床验证阶段;专门用于治疗肿瘤的“肿瘤基因导弹”也将在不久完成研制,它可有目的地寻找并杀死肿瘤,将使癌症的治愈成为可能。由中国、美国、德国三国科学家及中外六家研究机构参与研制的专门用于治疗乙肝、慢迁肝、慢活肝、丙肝、肝硬化的体细胞基因生物注射剂,最终解决了从剪切、分离到吞食肝细胞内肝炎病毒,修复、促进肝细胞再生的全过程。经4年临床试验已在全国面向肝炎患者。此项基因学研究成果在国际治肝领域中,是继干扰素等药物之后的一项具有革命性转变的重大医学成果。三、基因工程应用于环保方面工业发展以及其它人为因素造成的环境污染已远远超出了自然界微生物的净化能力,已成为人们十分关注的问题。基因工程技术可提高微生物净化环境的能力。美国利用DNA重组技术把降解芳烃、萜烃、多环芳烃、脂肪烃的4种菌体基因链接,转移到某一菌体中构建出可同时降解4种有机物的“超级细菌”,用之清除石油污染,在数小时内可将水上浮油中的2/3烃类降解完,而天然菌株需1年之久。也有人把Bt蛋白基因、球形芽孢杆菌、且表达成功。它能钉死蚊虫与害虫,而对人畜无害,不污染环境。现已开发出的基因工程菌有净化农药的DDT的细菌、降解水中的染料、环境中有机氯苯类和氯酚类、多氯联苯的工程菌、降解土壤中的TNT炸药的工程菌及用于吸附无机有毒化合物(铅、汞、镉等)的基因工程菌及植物等。90年代后期问世的DNA改组技术可以创新基因,并赋予表达产物以新的功能,创造出全新的微生物,如可将降解某一污染物的不同细菌的基因通过PCR技术全部克隆出来,再利用基因重组技术在体外加工重组,最后导入合适的载体,就有可能产生一种或几种具有非凡降解能力的超级菌株,从而大大地提高降解效率。四、前景展望由于基因工程运用DNA分子重组技术,能够按照人们预先的设计创造出许多新的遗传结合体,具有新奇遗传性状的新型产物,增强了人们改造动植物的主观能动性、预见性。而且在人类疾病的诊断、治疗等方面具有革命性的推动作用,对人口素质、环境保护等作出具大贡献。所以,各国政府及一些大公司都十分重视基因工程技术的研究与开发应用,抢夺这一高科技制高点。其应用前景十分广阔。我国基因工程技术尚落后于发达国家,更应当加速发展,切不可坐失良机。但是,任何科学技术都是一把“双刃剑”,在给人类带来利益的同时,也会给人类带来一定的灾难。比如基因药物,它不仅能根治遗传性疾病、恶性肿瘤、心脑血管疾病等,甚至人的智力、体魄、性格、外表等亦可随意加以改造;还有,克隆技术如果不加限制,任其自由发展,最终有可能导致人类的毁灭。还有,尽管目前的转基因动植物还未发现对人类有什么危害,但不等于说转基因动植物就是十分安全的,毕竟这些东西还是新生事物,需要实践慢慢地检验。转基因生物和常规繁殖生长的品种一样,是在原有品种的基础上对其部分性状进行修饰或增加新性状,或消除原来的不利性状,但常规育种是通过自然选择,而且是近缘杂交,适者生存下来,不适者被淘汰掉。而转基因生物远远超出了近缘的范围,人们对可能出现的新组合、新性状会不会影响人类健康和环境,还缺乏知识和经验,按目前的科学水平还不能完全精确地预测。所以,我们要在抓住机遇,大力发展基因工程技术的同时,需要严格管理,充分重视转基因生物的安全性。【参考文献】[1]楼士林,杨盛昌,龙敏南,等.基因工程[M].北京:科学出版社,2002.[2]李庆军,董艳桐,施冰.植物抗虫基因的研究进展[J].林业科技,2002,27(2):22 26. 这还有一篇

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