大肠杆菌异源生产丁醇途径组装及启动子优化

启动子优化是合成生物学研究的重要工具,可以通过不同强度的启动子调控基因转录水平以优化生物途径。丁醇是一种多用途的基础化工原料,目前有很多代谢工程手段应用在大肠杆菌的丁醇异源表达中,但是并没有进行启动子的精细调控。文中以大肠杆菌为宿主构建异源丁醇合成途径,通过DNA assembler的方法一步组装不同强度启动子组合的丁醇合成途径以优化丁醇合成。以强启动子Alper PLTetO1或弱启动子Alper BB转录硫解酶,以强启动子Braatsch 20或弱启动子Braatsch 10转录丁醇合成操纵子,共构建成4种不同质粒。结果表明以AlperPLTetO1转录硫解酶,Braatsch 10转录丁醇合成操纵子的组合获得最高的丁醇产量28 mg/L,与其他组合相比丁醇产量提高了3~5倍。     

Efficient butanol production under aerobic conditions by coculture of Clostridium acetobutylicum and Nesterenkonia sp. strain F

Clostridium acetobutylicum is widely used for the microbial production of butanol in a process known as acetone–butanol–ethanol (ABE) fermentation. However, this process suffers from several disadvantages including high oxygen sensitivity of the bacterium which makes the process complicated and necessitate oxygen elimination in the culture medium. Nesterenkonia sp. strain F has attracted interests as the only known non-Clostridia microorganism with inherent capability of butanol production even in the presence of oxygen. This bacterium is not delimited by oxygen sensitivity, a challenge in butanol biosynthesis, but the butanol titer was far below Clostridia. In this study, Nesterenkonia sp. strain F was cocultivated with C. acetobutylicum to form a powerful “coculture” for butanol production thereby eliminating the need for oxygen removal before fermentation. The response surface method was used for obtaining optimal inoculation amount/time and media formulation. The highest yield, 0.31 g/g ABE (13.6 g/L butanol), was obtained by a coculture initiated with 1.5 mg/L Nesterenkonia sp. strain F and inoculated with 15 mg/L C. acetobutylicum after 1.5 hr in a medium containing 67 g/L glucose, 2.2 g/L yeast extract, 4 g/L peptone, and 1.4% (vol/vol) P2 solution. After butanol toxicity assessment, where Nesterenkonia sp. strain F showed no butanol toxicity, the coculture was implemented in a 2 L fermenter with continual aeration leading to 20 g/L ABE.     

利用Tn5转座子介导突变提高大肠杆菌丁醇生产水平

目前,对于构建高产丁醇大肠杆菌工程菌株的工作,主要是对丁醇通路和相关途径的基因进行理性改造。为进一步提升菌株的丁醇生产能力,需要发掘基因组上可影响丁醇生产能力的基因,但这很难通过已有认识或计算机模型进行预测。本工作以一株实验室前期构建的产丁醇大肠杆菌工程菌株为研究对象,利用Tn5转座子构建了一个含有1 196个菌株的突变文库。丙酮酸是丁醇的前体,并且在发酵终产物中,副产物丙酮酸的含量与丁醇的含量呈反相关,因此,可以利用丙酮酸的含量来间接反映丁醇的含量,而丙酮酸可用二硝基苯肼显色法进行快速测定,基于此,建立了96孔板——酶标仪快速筛选方法。利用该方法成功筛选到了比对照菌株丁醇产量提高了29%、49%、56%的3个突变体菌株。利用反向PCR及测序的方法,确定了其转座子插入位置分别为:pyk A、tdk、cad C基因。这些基因可以作为进一步提高菌株丁醇产量的靶点,同时这种利用Tn5转座子筛选基因靶标的策略也为构建其他微生物细胞工厂提供了新思路。     

Redesigning Escherichia coli metabolism for anaerobic production of isobutanol

Fermentation enables the production of reduced metabolites, such as the biofuels ethanol and butanol, from fermentable sugars. This work demonstrates a general approach for designing and constructing a production host that uses a heterologous pathway as an obligately fermentative pathway to produce reduced metabolites, specifically, the biofuel isobutanol. Elementary mode analysis was applied to design an Escherichia coli strain optimized for isobutanol production under strictly anaerobic conditions. The central metabolism of E. coli was decomposed into 38,219 functional, unique, and elementary modes (EMs). The model predictions revealed that during anaerobic growth E. coli cannot produce isobutanol as the sole fermentative product. By deleting 7 chromosomal genes, the total 38,219 EMs were constrained to 12 EMs, 6 of which can produce high yields of isobutanol in a range from 0.29 to 0.41 g isobutanol/g glucose under anaerobic conditions. The remaining 6 EMs rely primarily on the pyruvate dehydrogenase enzyme complex (PDHC) and are typically inhibited under anaerobic conditions. The redesigned E. coli strain was constrained to employ the anaerobic isobutanol pathways through deletion of 7 chromosomal genes, addition of 2 heterologous genes, and overexpression of 5 genes. Here we present the design, construction, and characterization of an isobutanol-producing E. coli strain to illustrate the approach. The model predictions are evaluated in relation to experimental data and strategies proposed to improve anaerobic isobutanol production. We also show that the endogenous alcohol/aldehyde dehydrogenase AdhE is the key enzyme responsible for the production of isobutanol and ethanol under anaerobic conditions. The glycolytic flux can be controlled to regulate the ratio of isobutanol to ethanol production.     

Metabolic engineering strategies for butanol production in Escherichia coli

The global market of butanol is increasing due to its growing applications as solvent, flavoring agent, and chemical precursor of several other compounds. Recently, the superior properties of n-butanol as a biofuel over ethanol have stimulated even more interest. (Bio)butanol is natively produced together with ethanol and acetone by Clostridium species through acetone-butanol-ethanol fermentation, at noncompetitive, low titers compared to petrochemical production. Different butanol production pathways have been expressed in Escherichia coli, a more accessible host compared to Clostridium species, to improve butanol titers and rates. The bioproduction of butanol is here reviewed from a historical and theoretical perspective. All tested rational metabolic engineering strategies in E. coli to increase butanol titers are reviewed: manipulation of central carbon metabolism, elimination of competing pathways, cofactor balancing, development of new pathways, expression of homologous enzymes, consumption of different substrates, and molecular biology strategies. The progress in the field of metabolic modeling and pathway generation algorithms and their potential application to butanol production are also summarized here. The main goals are to gather all the strategies, evaluate the respective progress obtained, identify, and exploit the outstanding challenges.     

利用核糖体工程选育丙酮丁醇菌提高丁醇产量

利用核糖体工程技术对丙酮丁醇梭菌Clostridium acetobutylicum L7进行诱变筛选,以获得丁醇高产菌株。使用链霉素诱变C.acetobutylicum L7并结合设计的平板转接逐次提高链霉素浓度的筛选路线,获得丁醇产量较高的菌株S3。结果表明,S3丁醇产量为(12.48±0.03)g/L,乙醇产量为(1.70±0.07)g/L,相对于原始菌分别提高了11.2%及50%;丁醇/葡萄糖转化率由原始菌的0.19提高到0.22,丁醇生产率达到0.24 g/(L.h),相比提高30.5%;耐受丁醇浓度由原始菌的12 g/L提高到14 g/L;发酵液粘度下降到4 mPa/s,同比降低了60%,利于后续分离工作的进行,降低发酵成本。进一步研究工作表明,S3菌株遗传稳定性良好。因此,核糖体工程技术是一种选育丁醇高产菌株的有效方法。     

电子载体对丁醇发酵的影响

研究在培养基中加入不同电子载体对丁醇发酵的影响。结果表明:添加微量的苄基紫精可以促进丁醇的产生,同时可强烈抑制丙酮的合成,丁醇体积分数由66.92%提高到82.35%。苄基紫精可促进菌株快速进入产溶剂期,发酵周期明显缩短,丁醇生产强度显著提高。7%玉米培养基中加入40 mg/L苄基紫精,丁醇产量最高达16.10 g/L,生产强度为0.37 g/(L.h),分别较对照提高10.96%和60.87%。在初始丁醇体积分数较低的条件下,苄基紫精对丁醇合成的促进作用更明显。     

添加有机酸对Clostridium acetobutylicum合成丙酮和丁醇的影响

为提高丙酮-丁醇梭菌厌氧发酵生产丙酮和丁醇的能力,在发酵过程中添加有机酸（乙酸和丁酸）,考察其对菌体生长、溶剂合成影响。实验表明：当添加1.5 g/L乙酸时能够促进菌体的生长,促进丙酮的合成,在600 nm处的最大OD值比参照值高出18.4%,丙酮的最终质量分数提高了21.05%,但不能促进丁醇的合成;当添加1.0g/L丁酸时能够促进菌体生长,促进丁醇的合成,在600 nm处的最大OD比参照值高22.29%,丁醇的最终质量分数比对照组提高了24.32%,但不能促进丙酮的合成。     

高抗逆高丁比拜氏梭菌的选育及其性能考察简

以抗逆突变株Clostridium beijerinckii IB4为出发菌株,通过常压室温等离子体诱变（ ARTP ）,刃天青平板初筛,摇瓶发酵复筛,筛选出1株高抗逆高丁比的突变菌株C.beijerinckii IT111。发酵结果表明：该突变菌株利用多种C源时均展现其高丁醇比的特性,以玉米芯酸解糖液为C源时,溶剂产量达到10.5 g/L,丁醇8.0 g/L,丁醇比高达76％。抑制物抗逆性测试结果显示：糠醛和酸类对C.beijerinckii发酵影响较小,酚类物质对C.beijerinckii抑制作用较强,其中以香草醛为最。综上所述,C.beijerinckii IT111是1株极具潜力的利用木质纤维原料制备丁醇的菌株。     

Engineering the robustness of Clostridium acetobutylicum by introducing glutathione biosynthetic capability

To improve the aero- and solvent tolerance of the solvent-producing Clostridium acetobutylicum, glutathione biosynthetic capability was introduced into C. acetobutylicum DSM1731 by cloning and over-expressing the gshAB genes from Escherichia coli. Strain DSM1731(pITAB) produces glutathione, and shows a significantly improved survival upon aeration and butanol challenge, as compared with the control. In addition, strain DSM1731(pITAB) exhibited an improved butanol tolerance and an increased butanol production capability, as compared with the recombinant strains with only gshA or gshB gene. These results illustrated that introducing glutathione biosynthetic pathway, which is redundant for the metabolism of C. acetobutylicum, can increase the robustness of the host to achieve a better solvent production.     

丁醇基因在大肠杆菌中表达的现状与展望

随着化石能源过度开采带来的能源短缺与环境恶化,丁醇凭借着其优越的理化性质成为了最具潜力的绿色燃料之一。近几年微生物在生物能源生产研究中受到广泛关注,主要集中在梭菌丁醇合成途径的异源表达。目前利用大肠杆菌产丁醇的产量已经接近产丁醇的天然菌株的产量。然而,大肠杆菌产丁醇仍存在很多限制性因素。主要从乙酰辅酶A依赖途径评述大肠杆菌生产丁醇的限制因素,并讨论提高丁醇产量需要解决的问题。     

萃取耦合技术对玉米秸秆水解液发酵产丁醇的影响

本研究以玉米秸秆水解液为原料,通过萃取发酵技术生产燃料丁醇,以提高丁醇产量,降低生产成本。通过对萃取剂的筛选与条件优化,确定纤维丁醇发酵的萃取剂为油醇,添加时间为发酵0 h,添加比例为1:1 (V/V)。该条件下发酵32 g/L糖浓度的玉米秸秆水解液,丁醇和总溶剂产量分别为3.28 g/L和4.72 g/L,比对照分别提高958.1%和742.9%。以D301树脂脱毒后5%总糖浓度的玉米秸秆水解液进行丁醇萃取发酵,丁醇和总溶剂产量分别达到10.34 g/L和14.72 g/L,发酵得率为0.31 g/g,与混合糖发酵结果相当。研究结果表明萃取发酵技术能够显著提高原料的利用率和丁醇产量,为纤维丁醇工业化生产提供了技术支撑。     

响应面法优化甘蔗糖蜜发酵产丁醇

以甘蔗糖蜜为底物,用响应面法对高丁醇比突变菌株拜氏梭菌(Clostridium beijerinckii)ART124发酵生产丁醇的培养条件进行优化.首先利用Plackett - Burman试验设计筛选出影响丁醇生产的3个重要因素CaCO3和NH4 HCO3和K2HPO4的用量,再通过最陡爬坡路径逼近最大向应区域,最后根据响应面中心组合设计理论,确定主要影响因素的最佳条件:CaCO3、NH4HCO3和K2HPO4的质量浓度分别为2.65、2.16和0.43 g/L.利用数学模型分析预测得甘蔗糖蜜质量浓度为30 g/L时,最佳的丁醇产量为8.10 g/L,比优化前提高了53.14％.在最佳工艺条件下得到的实验结果与模型预测值很吻合,说明所建立的模型是有效的.     

Screening and characterization of butanol‐tolerant micro‐organisms

Aims: Poor butanol tolerance of solventogenic stains directly limits their butanol production during industrial‐scale fermentation process. This study was performed to search for micro‐organisms possessing elevated tolerance to butanol. Methods and Results: Two strains, which displayed higher butanol tolerance compared to commonly used solventogenic Clostridium acetobutylicum, were isolated by evolution and screening strategies. Both strains were identified as lactic acid bacteria (LAB). On this basis, a LAB culture collection was tested for butanol tolerance, and 60% of the strains could grow at a butanol concentration of 2·5% (v/v). In addition, an isolated strain with superior butanol tolerance was transformed using a certain plasmid. Conclusions: The results indicate that many strains of LAB possessed inherent tolerance of butanol. Significance and Impact of the Study: This study suggests that LAB strains may be capable of producing butanol to elevated levels following suitable genetic manipulation.     

丁醇合成途径关键酶基因在大肠杆菌中的克隆和表达

【目的】克隆丙酮丁醇梭状芽胞杆菌(Clostridium acetobutylicum)ATCC824丁醇合成途径关键酶基因,构建产丁醇的工程大肠杆菌。【方法】以C.acetobutylicum ATCC824基因组为模板,分别扩增丁醇合成途径关键酶基因thil,adhE2和BCS operon(crt-bcd-etfB-etfA-hbd)基因序列,构建BCS operon-adhE2-thil/pTrc99a/MG1655(pBAT)。重组菌E.coli pBAT采用0.1 mmol异丙基-β-硫代半乳糖苷(IPTG)诱导5 h,测定乙酰基转移酶(THL)、3-羟基丁酰辅酶A脱氢酶(HBD)、3-羟基丁酰辅酶A脱水酶(CRT)、丁酰辅酶A脱氢酶(BCD)、醛醇脱氢酶(BYDH/BDH)的酶活。并以该基因工程菌作为发酵菌种,采用好氧、厌氧和微好氧三种培养方式,检测丁醇产量。【结果】酶活测定结果显示:THL酶活达到0.160 U/mg protein,酶活力提高了近30倍;HBD酶活力提高了近5倍;CRT酶活达到1.53 U/mg protein,野生菌株无此酶活;BCD酶活力提高了32倍;BYDH/BDH酶活力无显著提高。3种发酵培养结果显示在微好氧和厌氧条件下,均有丁醇产生,且丁醇的最大产量约为84 mg/L。【结论】本实验通过构建产丁醇基因工程大肠杆菌,实现了丁醇关键酶基因在大肠杆菌中的活性表达以及发酵产丁醇,为发酵法生产丁醇开辟了一条新的途径。     

Metabolic engineering of Escherichia coli for 1-butanol production

Compared to ethanol, butanol offers many advantages as a substitute for gasoline because of higher energy content and higher hydrophobicity. Typically, 1-butanol is produced by Clostridium in a mixed-product fermentation. To facilitate strain improvement for specificity and productivity, we engineered a synthetic pathway in Escherichia coli and demonstrated the production of 1-butanol from this non-native user-friendly host. Alternative genes and competing pathway deletions were evaluated for 1-butanol production. Results show promise for using E. coli for 1-butanol production.     

高浓度丁醇浸泡及N＋束注入诱变双重作用筛选丁醇高产菌

通过高浓度丁醇浸泡处理丙酮丁醇梭菌（Clostridiumacetobutylicum）CL-2,筛选得到一株丁醇耐受能力提高并溶剂产量增加的菌株BR30—2,丁醇产量达11．77g/L,比CL-2提高了16．65％。以BR30—2作为出发菌株,进行N＋束注入诱变,筛选得到高产菌株BH．9,丁醇产量达14．5g/L,总溶剂为23．14g／L。在BH-9发酵过程中添加0．1％丁酸钠,丁醇产量达到16．59g/L,丁醇比例提高至67．38％。     

Development of a cost-effective glucose-corn steep medium for production of butanol by Clostridium beijerinckii

Corn steep water (CSW) medium (1.6% solids plus 6% glucose) was evaluated for growth and butanol production by Clostridium beijerinckii NCIMB 8052 wild-type and hyper-amylolytic, hyper-butanol-producing mutant strain BA101. CSW alone was not a suitable substrate, whereas addition of glucose supported growth and butanol production by both strains. In a batch-scale fermentation using an optimized 6% glucose-1.6% solids CSW medium, C. beijerinckii NCIMB 8052 and strain BA101 produced 10.7 g L⁻¹ and 14.5 g L⁻¹ of butanol, respectively. The total solvents (acetone, butanol, and ethanol) produced by C. beijerinckii NCIMB 8052 and strain BA101 were 14 g L⁻¹ and 20 g L⁻¹, respectively. Initial fermentation in small-scale flasks containing 6% maltodextrin-1.6% solids concentration CSW medium resulted in 6 g L⁻¹ and 12.6 g L⁻¹ of butanol production by C. beijerinckii NCIMB 8052 and strain BA101, respectively. CSW can serve as an economic source of nitrogen, vitamins, amino acids, minerals, and other nutrients. Thus, it is feasible to use 6% glucose-1.6% solids CSW medium in place of semi-defined P2 medium. Received 9 February 1998/ Accepted in revised form 1 September 1998     

Fermentative butanol production by Clostridia

Butanol is an aliphatic saturated alcohol having the molecular formula of C(4)H(9)OH. Butanol can be used as an intermediate in chemical synthesis and as a solvent for a wide variety of chemical and textile industry applications. Moreover, butanol has been considered as a potential fuel or fuel additive. Biological production of butanol (with acetone and ethanol) was one of the largest industrial fermentation processes early in the 20th century. However, fermentative production of butanol had lost its competitiveness by 1960s due to increasing substrate costs and the advent of more efficient petrochemical processes. Recently, increasing demand for the use of renewable resources as feedstock for the production of chemicals combined with advances in biotechnology through omics, systems biology, metabolic engineering and innovative process developments is generating a renewed interest in fermentative butanol production. This article reviews biotechnological production of butanol by clostridia and some relevant fermentation and downstream processes. The strategies for strain improvement by metabolic engineering and further requirements to make fermentative butanol production a successful industrial process are also discussed.     

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Consolidated bioprocessing (CBP) by using microbial consortium was considered as a promising approach to achieve direct biofuel production from lignocellulose. In this study, the interaction mechanism of microbial consortium consisting of Thermoanaerobacterium thermosaccharolyticum M5 and Clostridium acetobutylicum NJ4 was analyzed, which could achieve efficient butanol production from xylan through CBP. Strain M5 possesses efficient xylan degradation capability, as 19.73 g/L of xylose was accumulated within 50 hr. The efficient xylose utilization capability of partner strain NJ4 could relieve the substrate inhibition to hydrolytic enzymes of xylanase and xylosidase secreted by strain M5. In addition, the earlier solventogenesis of strain NJ4 was observed due to the existence of butyrate generated by strain M5. The mutual interaction of these two strains finally gave 13.28 g/L of butanol from 70 g/L of xylan after process optimization, representing a relatively high butanol production from hemicellulose. Moreover, 7.61 g/L of butanol was generated from untreated corncob via CBP. This successfully constructed microbial consortium exhibits efficient cooperation performance on butanol production from lignocellulose, which could provide a platform for the emerging butanol production from lignocellulose.