真养产碱杆菌Alcaligenes eutrphus从不同碳源合成可降解塑料:发酵过程及产物种类确定

真养产碱菌利用不同碳源合成可降解塑料聚羟基丁酸(PHB)和聚(羟基丁酸-羟基戊酸)(PHBV).二者可由碳-13核磁共振谱区分,从作者所研究的未见诸文献的该菌碳源衣康酸得到的聚合物,被用来举例说明如何确定它为PHB.此外还述及发酵程序、影响产率的因素及所得可降解塑料应用近况等.     

聚羟基烷酸酯 (PHA) 改性研究进展

本文简述了生物制造聚羟基烷酸酯(PHA),包括聚3-羟基丁酸酯(PHB)、聚(3-羟基丁酸酯-3-羟基戊酸酯)(PHBV)、聚(3-羟基丁酸酯-4-羟基丁酸酯)(P3/4HB)、聚(3-羟基丁酸酯-3-羟基己酸酯)(PHBH)的产业化现状,综述了针对PHA材料热稳定性差、加工窗口较窄等缺点而进行的一些改性研究。选用适当方法对PHA进行改性,可使其性能得到优化,应用领域得到拓展。     

微生物合成塑料——聚羟基链烷酯

许多原核生物在非平衡生长条件下,在胞内合成并积累不同烷侧基的脂肪族聚-3-羟基脂类物质--聚羟基链烷酯(PHA),其中含甲基侧链的聚羟基丁酯(PHB)和含乙基侧链的聚羟基戊酯(PHV)是聚合物的主要成分,它们是高结晶热塑性物质,与化学合成的塑料一样能铸造成型、压制成型并能制成薄膜和纤维状材料。     

细菌产生的高分子材料——聚羟基丁酯

当Pseudomonas sp．生长在植物油或正烷烃中时能产生大量的聚羟基丁酯(简称PHB)。其合适的培养基为2％正烷烃、O．05％尿素和0．05％酵母膏。从对数生长期至稳定期该菌累积的PHB量可达干细胞重的30-40％。该菌中获得的PHB的红外光谱图的吸收峰与其他细菌中获得的PHB相同。     

短须嗜热单孢菌聚羟基脂肪酸酯解聚酶的表达、热稳定性改造及在PHB降解中的应用

聚羟基脂肪酸酯解聚酶(polyhydroxyalkanoate depolymerase,PHAD)可用于聚羟基脂肪酸酯(polyhydroxyalkanoate,PHA)的降解回收,为开发热稳定性好的PHAD,本研究在大肠杆菌(Escherichiacoli)BL21(DE3)中成功表达了来自短须嗜热单孢菌(Thermomonospora umbrina)的PHA解聚酶(TumPHAD),并通过二硫键理性设计获得了热稳定性提升的突变体A190C/V240C,其最适温度为60℃,比野生型提高20℃,50℃半衰期为7h,是野生型酶的21倍。将突变体A190C/V240C用于典型PHA之一的聚羟基丁酸酯(polyhydroxybutyrate,PHB)降解,在50℃条件下,PHB的2 h和12 h降解率较野生型分别提高了2.1倍和3.8倍。本研究获得的TumPHAD突变体A190C/V240C具有耐高温、热稳定性好和PHB降解能力强的特点,对PHB的降解回收具有重要意义。     

英ICI公司在国内正式生产生物聚合物“BIOPOL”

英国帝国化学工业(ICI)公司决定在英国国内正式工业生产生物聚合物“BIOPOL”,在印度建厂生产的计划告吹。 “BIOPOL”是以糖类为原料用真养产碱菌(Alcaligenes eutrophus)好气发酵生产的聚合物。其主要成分为聚羟基丁酸(PHB)。该公司还建立了发酵生产羟基丁酸中混入羟基戊酸的聚合物(最大混会比28％)。控制聚合物不同分子量可配制成组分各异     

PHB/PLLA组织工程前交叉韧带支架材料改性的实验研究

目的:探索体外构建组织工程前交叉韧带(anterior cruciate ligament,ACL)的三维支架材料。方法:以聚羟基丁酸已酯/聚左旋乳酸(PHB/PLLA1:1)制备"三明治"样结构共聚物并测量其孔隙率等指标。以I型胶原对制备的PHB/PLLA支架进行杂化,获得PHB/PLLA胶原杂化支架。扫描电镜观察其表面结构。将兔皮肤成纤维细胞(SF)接种于PHB/PLLA支架与PHB/PLLA胶原杂化支架,观察其在材料上生长情况。结果:PHB/PLLA支架杂化后胶原填充于纤维空隙,分布比较均匀。体外培养的胶原杂化支架材料上要比PHB/PLLA支架有更多的皮肤成纤维细胞生长。结论:胶原杂化有利于细胞种植和生长,PHB/PLLA胶原杂化支架具有良好的三维构型和生物相容性,有望为前交叉韧带损伤的修复提供了一种新型的支架材料。     

微生物合成可降解塑料聚羟基链烷酸（PHA）

本文综述利用微生物合成主要包括聚羟基丁酸（ＰＨＢ）和聚羟基丁酸－羟基戊酸（ＰＨＢＶ）在内的聚羟基链烷酸的若干要素,如微生物种资源、生物合成途径、发酵以及产物的性质和应用。     

真养产碱杆菌聚羟基烷酸合成酶基因在欧文氏菌中的表达

将含有真养产碱杆菌(Alcaligenes eutrophus)合成聚羟基烷酸(PHA)基因(phaCA3)的质粒pTZl8U—PHB改造成为具有卡那霉素抗性的质粒pJMCl．并以电击法将pJMCl引入利用碳源广泛的胡罗卜软腐欧文氏茵(Erwinia carotovora)非致病菌系(Eccl3B)中,phaCAB可获得高效表达,膨大的转基因菌[Eccl3B(pJMCl)]细胞内几乎充满PHA颗粒。以蔗糖为碳源,初步在5L发酵罐中对转基因菌进行分批补料培养35h,菌体干重达28g／L,PHA占菌体干重的68％,具有生产潜力。将该菌合成的PHA提取纯化(纯度达99％)后,进行核磁共振分析,发现它只有单一的聚-β-羟基丁酸(PHB)组分。     

废弃活性污泥中产聚羟基脂肪酸酯菌株Bacillus sp. PB-3的发酵条件优化

通过尼罗红染色法结合荧光显微镜镜检,从废弃活性污泥中分离得到1株高产聚羟基脂肪酸酯(PHAs)的菌株Bacillus sp.PB-3,经气相色谱法鉴定该菌株胞内产物为聚β-羟基丁酸酯(PHB)。对培养基成分及发酵条件优化后,获得最佳培养方案:12 g/L的葡萄糖为C源,2 g/L的牛肉膏为N源,初始pH 7.5,培养基装液量80 mL,转速为200 r/min,37℃培养48 h,PHB质量分数可达菌体干质量的32.09%,比优化前提高30%。     

Studies on intracellular degradation of polyhydroxyalkanoic acid-polyethylene glycol copolymer accumulated by Azotobacter chroococcum MAL-201

Azotobacter chroococcum MAL-201 accumulates poly(3-hydroxybutyric acid) [PHB] when grown in glucose containing nitrogen-free Stockdale medium. The same medium supplemented with valerate alone and valerate plus polyethylene glycol (PEG) leads to the accumulation of poly(3-hydroxybutyrate-co-3-hydroxyvalerate) [PHBV] and PEG containing PHBV-PEG polymers, respectively. The intracellular degradation of these polymers as studied in carbon-free Stockdale medium showed a rapid degradation of PHB followed by PHBV, while it was least in case of PHBV-PEG. The rate of such degradation was 44.16, 26.4 and 17.0 mg h(-1)l(-1) for PHB, PHBV and PHBV-PEG, respectively. During the course of such of PHBV and PHBV-PEG degradation the 3HB mol% of polymers decreased significantly with increase of 3HV mol fraction, the EG mol% in PHBV-PEG, however, remained constant. After 50h of degradation the decrease in intrinsic viscosity and molecular mass of PHBV-PEG were 37.5 and 43.6%, respectively. These values appeared low compared to PHB and PHBV. Moreover, the increasing EG content of polymer retarded their extent of degradation. Presence of PEG, particularly of low molecular weight PEG was inhibitory to intracellular PHA depolymerise (i-PHA depolymerase) activity and the relative substrate specificity of the i-PHA depolymerase of MAL-201 appeared to be PHB > PHBV > PHBV-PEG.     

Synthesis of poly(3-hydroxybutyrate-co-3-hydroxyvalerate) from activated sludge

Poly-3-hydroxybutyrate (PHB) and poly(3-hydroxybutyrate- co-3-hydroxyvalerate) (PHBV) was produced using a co-culture of activated sludge. When butyric acid was used as sole carbon source, PHB was produced. When valeric acid was added to the medium, PHBV was produced. The 3-hydroxyvalerate (3HV) mole fraction in the PHBV reached a maximum of 54% when valeric acid was used as sole carbon source. When the 3HV units in the co-polymer increased from 0.0 to 54.0 mol%, the melting temperature ( T m ) decreased from 178 to 99°C. The composition, and hence the mechanical properties, of the co-polymer produced by activated sludge can be controlled by adjusting the medium composition.     

Accumulation of a poly(hydroxyalkanoate) copolymer containing primarily 3-hydroxyvalerate from simple carbohydrate substrates by Rhodococcus sp. NCIMB 40126

A number of taxonomically-related bacteria have been identified which accumulate poly(hydroxyalkanoate) (PHA) copolymers containing primarily 3-hydroxyvalerate (3HV) monomer units from a range of unrelated single carbon sources. One of these, Rhodococcus sp. NCIMB 40126, was further investigated and shown to produce a copolymer containing 75 mol% 3HV and 25 mol% 3-hydroxybutyrate (3HB) from glucose as sole carbon source. Polyesters containing both 3HV and 3HB monomer units, together with 4-hydroxybutyrate (4HB), 5-hydroxyvalerate (5HV) or 3-hydroxyhexanoate (3HHx), were also produced by this organism from certain accumulation substrates. With valeric acid as substrate, almost pure (99 mol% 3HV) poly(3-hydroxyvalerate) was produced. N.m.r. analysis confirmed the composition of these polyesters. The thermal properties and molecular weight of the copolymer produced from glucose were comparable to those of PHB produced by Alcaligenes eutrophus.     

Incorporation of polyethylene glycol in polyhydroxyalkanoic acids accumulated by Azotobacter chroococcum MAL-201

Azotobacter chroococcum MAL-201 (MTCC 3853), a free-living nitrogen-fixing bacterium accumulates poly(3-hydroxybutyric acid) [PHB, 69% of cell dry weight (CDW)] when grown on glucose and poly(3-hydroxybutyrate-co-3-hydroxyvalerate) [PHBV with 19.2 mol% 3HV] when grown on glucose and valerate. Use of ethylene glycol (EG) and/or polyethylene glycols (PEGs) of low molecular weight as sole carbon source were detrimental to A. chroococcum growth and polymer yields. PEG-200, however, in the presence of glucose was incorporated into the polyhydroxyalkanoate (PHA) polymer. Addition of PEG-200 (150 mM) to culture medium during mid-log phase growth favored increased incorporation of EG units (12.48 mol%) into the PHB polymer. In two-step culture experiments, where valerate and PEG simultaneously were used in fresh medium, EG was incorporated most effectively in the absence of glucose, leading to the formation of a copolymer containing 18.05 mol% 3HV and 14.78 mol% EG. The physico-mechanical properties of PEG-containing copolymer (PHBV–PEG) were compared with those of the PHB homopolymer and the PHBV copolymer. The PHBV–PEG copolymer appeared to have less crystallinity and greater flexibility than the short-chain-length (SCL) PHA polymers.     

真养产碱杆菌合成3-羟基丁酸与3-羟基戊酸共聚物发酵条件研究

在摇瓶条件下,对真养产碱杆菌（Ａｌｃａｌｉｇｅｎｅｓｅｕｔｒｏｐｈｕｓ）的３羟基丁酸与３羟基戊酸共聚物（ＰＨＢＶ）发酵过程中ＨＶ组分的前体物质———丙酸的加入时间和加入量进行了研究,结果表明,ＰＨＢＶ中ＨＶ组分含量与丙酸的加入时间和加入量有密切的关系,丙酸的最佳加入时间为菌体生长阶段结束后的多聚物合成初期;尽管高浓度丙酸下可获得较高的ＨＶ组分含量,但会明显抑制菌体的生长和产物的合成。通过对２Ｌ小罐中ＰＨＢＶ合成阶段流加不同糖／酸比混合液所得的发酵结果的比较,并在综合考虑ＰＨＢＶ浓度、ＨＶ组分含量、生产强度和生产成本等基础上,提出了在ＰＨＢＶ合成期流加液的糖／酸比应随菌体对丙酸利用能力的下降而不断增加的流加策略,在此条件下,细胞干重、ＰＨＢＶ浓度和ＰＨＢＶ含量和ＨＶ摩尔分率分别达到５２１ｇ／Ｌ、４０８ｇ／Ｌ、７８３％和１６２ｍｏｌ％,ＨＶ组分对丙酸的产率系数为０５ｇ／ｇ,ＰＨＢＶ的生产强度达到０７４ｇ／（Ｌ／ｈ）。     

Production of targeted poly(3-hydroxyalkanoates) copolymers by glycogen accumulating organisms using acetate as sole carbon source

One of the main limitations in bacterial polyhydroxyalkanoate (PHA) production with mixed cultures is the fact that primarily polyhydroxybutyrate (PHB) homopolymers are generated from acetate as the main carbon source, which is brittle and quite fragile. The incorporation of different 3-hydroxyalkanoate (HA) components into the polymers requires the addition of additional carbon sources, leading to extra costs and complexity. In this study, the production of poly(3-hydroxybutyrate (3HB)-co-3-hydroxyvalerate (3HV)-co-3-hydroxy-2-methylvalerate (3HMV)), with 7-35C-mol% of 3HV fractions from acetate as the only carbon source was achieved with the use of glycogen accumulating organisms (GAOs). An enriched GAO culture was obtained in a lab-scale reactor operated under alternating anaerobic and aerobic conditions with acetate fed at the beginning of the anaerobic period. The production of PHAs utilizing the enriched GAO culture was investigated under both aerobic and anaerobic conditions. A polymer content of 14-41% of dry cell weight was obtained. The PHA product accumulated by GAOs under anaerobic conditions contained a relatively constant proportion of non-3HB monomers (30+/-5C-mol%), irrespective of the amount of acetate assimilated. In contrast, under aerobic conditions, GAOs only produced 3HB monomers from acetate causing a gradually decreasing 3HV fraction during this aerobic feeding period. The PHAs were characterized by gel permeation chromatography (GPC) and differential scanning calorimetry (DSC). The data demonstrated that the copolymers possessed similar characteristics to those of commercially available poly(3HB-co-3HV) (PHBV) products. The PHAs produced under solely anaerobic conditions possessed lower melting points and crystallinity, higher molecular weights, and narrower molecular-weight distributions, compared to the aerobically produced polymers. This paper hence demonstrates the significant potential of GAOs to produce high quality polymers from a simple and cheap carbon source, contributing considerably to the growing research body on bacterial PHA production by mixed cultures.     

Microbial production of polyhydroxyalkanoate block copolymer by recombinant Pseudomonas putida

Polyhydroxyalkanoate (PHA) synthesis genes phaPCJ _Ac cloned from Aeromonas caviae were transformed into Pseudomonas putida KTOY06ΔC, a mutant of P. putida KT2442, resulting in the ability of the recombinant P. putida KTOY06ΔC (phaPCJ _A.c ) to produce a short-chain-length and medium-chain-length PHA block copolymer consisting of poly-3-hydroxybutyrate (PHB) as one block and random copolymer of 3-hydroxyvalerate (3HV) and 3-hydroxyheptanoate (3HHp) as another block. The novel block polymer was studied by differential scanning calorimetry (DSC), nuclear magnetic resonance, and rheology measurements. DSC studies showed the polymer to possess two glass transition temperatures (T _g), one melting temperature (T _m) and one cool crystallization temperature (T _c). Rheology studies clearly indicated a polymer chain re-arrangement in the copolymer; these studies confirmed the polymer to be a block copolymer, with over 70 mol% homopolymer (PHB) of 3-hydroxybutyrate (3HB) as one block and around 30 mol% random copolymers of 3HV and 3HHp as the second block. The block copolymer was shown to have the highest tensile strength and Young’s modulus compared with a random copolymer with similar ratio and a blend of homopolymers PHB and PHVHHp with similar ratio. Compared with other commercially available PHA including PHB, PHBV, PHBHHx, and P3HB4HB, the short-chain- and medium-chain-length block copolymer PHB-b-PHVHHp showed differences in terms of mechanical properties and should draw more attentions from the PHA research community.     

Production of the copolymer poly(3-hydroxybutyrate-co-3-hydroxyvalerate) with varied composition using different nitrogen sources with Haloferax mediterranei

The extreme haloarchaea Haloferax mediterranei accumulates poly(3-hydroxybutyrate-co-3-hydroxyvalerate) (PHBV) without the need for specific precursors. In this study, growth kinetics and PHBV synthesis were characterised under nitrogen-excess and nitrogen-limiting conditions in ammonium and, for the first time, nitrate. With excess nitrogen, ammonium and nitrate cultures generated 10.7 g/L biomass containing 4.6 wt% PHBV and 5.6 g/L biomass with 9.3 wt% PHBV, respectively. Copolymer composition varied with the nitrogen source used: PHBV from ammonium cultures had 16.9 mol% 3-hydroxyvalerate (HV), while PHBV from nitrate cultures contained 12.5 mol% HV. Nitrogen limitation was achieved with carbon-to-nitrogen (C/N) molar ratios of 25 or higher. Nitrogen limitation reduced biomass generation and polymer concentration, but polymer accumulation increased to 6.6 and 9.4% for ammonium and nitrate, respectively, with C/N 42. PHBV composition was also affected and cultures with lower C/N ratios produced richer HV polymers. Copolymer formation was not a uniform process: HV was only detected after a minimum accumulation of 0.45 g/L PHB and lasted for a maximum of 48 h. The understanding of copolymer synthesis and the influence of culture conditions such as the nitrogen source will help in designing novel strategies for the production of PHBV with more regular structure and material properties.

     

Occurrence, metabolism, metabolic role, and industrial uses of bacterial polyhydroxyalkanoates.

Polyhydroxyalkanoates (PHAs), of which polyhydroxybutyrate (PHB) is the most abundant, are bacterial carbon and energy reserve materials of widespread occurrence. They are composed of 3-hydroxyacid monomer units and exist as a small number of cytoplasmic granules per cell. The properties of the C4 homopolymer PHB as a biodegradable thermoplastic first attracted industrial attention more than 20 years ago. Copolymers of C4 (3-hydroxybutyrate [3HB]) and C5 (3-hydroxyvalerate [3HV]) monomer units have modified physical properties; e.g., the plastic is less brittle than PHB, whereas PHAs containing C8 to C12 monomers behave as elastomers. This family of materials is the centre of considerable commercial interest, and 3HB-co-3HV copolymers have been marketed by ICI plc as Biopol. The known polymers exist as 2(1) helices with the fiber repeat decreasing from 0.596 nm for PHB to about 0.45 nm for C8 to C10 polymers. Novel copolymers with a backbone of 3HB and 4HB have been obtained. The native granules contain noncrystalline polymer, and water may possibly act as a plasticizer. Although the biosynthesis and regulation of PHB are generally well understood, the corresponding information for the synthesis of long-side-chain PHAs from alkanes, alcohols, and organic acids is still incomplete. The precise mechanisms of action of the polymerizing and depolymerizing enzymes also remain to be established. The structural genes for the three key enzymes of PHB synthesis from acetyl coenzyme A in Alcaligenes eutrophus have been cloned, sequenced, and expressed in Escherichia coli. Polymer molecular weights appear to be species specific. The factors influencing the commercial choice of organism, substrate, and isolation process are discussed. The physiological functions of PHB as a reserve material and in symbiotic nitrogen fixation and its presence in bacterial plasma membranes and putative role in transformability and calcium signaling are also considered.     

Development of Halomonas TD01 as a host for open production of chemicals

Genetic engineering of Halomonas spp. was seldom reported due to the difficulty of genetic manipulation and lack of molecular biology tools. Halomonas TD01 can grow in a continuous and unsterile process without other microbial contaminations. It can be therefore exploited for economic production of chemicals. Here, Halomonas TD01 was metabolically engineered using the gene knockout procedure based on markerless gene replacement stimulated by double-strand breaks in the chromosome. When gene encoding 2-methylcitrate synthase in Halomonas TD01 was deleted, the conversion efficiency of propionic acid to 3-hydroxyvalerate (3HV) monomer fraction in random PHBV copolymers of 3-hydroxybutyrate (3HB) and 3HV was increased from around 10% to almost 100%, as a result, cells were grown to accumulate 70% PHBV in dry weight (CDW) consisting of 12 mol% 3HV from 0.5 g/L propionic acid in glucose mineral medium. Furthermore, successful deletions on three PHA depolymerases eliminate the possible influence of PHA depolymerases on PHA degradation in the complicated industrial fermentation process even though significant enhanced PHA content was not observed. In two 500 L pilot-scale fermentor studies lasting 70 h, the above engineered Halomonas TD01 grew to 112 g/L CDW containing 70 wt% P3HB, and to 80 g/L CDW with 70 wt% P(3HB-co-8 mol% 3HV) in the presence of propionic acid. The cells grown in shake flasks even accumulated close to 92% PHB in CDW with a significant increase of glucose to PHB conversion efficiency from around 30% to 42% after 48 h cultivation when pyridine nucleotide transhydrogenase was overexpressed. Halomonas TD01 was also engineered for producing a PHA regulatory protein PhaR which is a robust biosurfactant.