Production of <Emphasis Type="Italic">Pleurotus sajor-caju</Emphasis> strain PS-2001 biomass in submerged culture

Mushrooms or fruiting bodies of many basidiomycetes are commonly produced in solid-state fermentation, generally after 20-60 days of growth. However, it is also possible to produce biomass from these fungi, in submerged fermentation in shorter time. This work was aimed at evaluating biomass production with the basidiomycete Pleurotus sajor-caju, in a submerged process and to determine the proportion of chemical components of this biomass. Initially, an optimization of the culture medium was done to produce a faster growth of microbial mass by changing the concentrations of ammonium sulfate, soy protein and yeast extract. Using the optimized culture medium, values of approximately 5.5 g L(-1) of biomass in a medium with 10 g L(-1) of glucose were attained. When the optimized culture medium was tested in a 5-L stirred tank bioreactor, using 10 g L(-1) of glucose or sucrose as carbon source, values of 8.18 and 5.94 g L(-1) of biomass concentration were obtained, respectively. In the medium with glucose, high yields (0.82 g g(-1)) and productivity of 0.085 g L(-1) h(-1) were obtained. The exopolysaccharide content (1.58 g dry matter L(-1)) in the culture was higher in the fermentation with sucrose. The nutritional composition of the biomass obtained in the submerged fermentation was similar to that of the fruiting body in terms of quantities of total carbohydrates, ash and calories, but total fat and protein were higher.     

Development of a low-cost technology for mass production of the free-living nematode <Emphasis Type="Italic">Panagrellus redivivus</Emphasis> as an alternative live food for first feeding fish larvae

The free-living nematode Panagrellus redivivus is a suitable food source for first feeding fish. In the present report, a new method for the mass production of P. redivivus is presented. The technique involves multiplication of the nematode in monoxenic (single microorganism: Saccharomyces cerevisiae) solid culture (fluid media supported by 1- to 4-cm(3) sponge cubes) in autoclavable plastic bags (size range: 50 x 30 cm to 75 x 67 cm). Two growing media were tested: oat-meal medium (OM), which is an oat-based medium (16.7% oat-meal flour in 0.8% saline solution), and purified ingredient medium (PIM), a semi-synthetic medium (1.64% meat peptone, 0.94% yeast extract, 12.6% corn starch, 0.24% glucose, 1.48% sunflower oil, in 0.8% saline solution). The bags were inoculated with 350 nematodes/g medium. After an average period of 12 days (11-13 days) at 25 degrees C, the average yield (number of nematodes/g medium) was 241 x 10(3) for OM and 333 x 10(3) for PIM in 12-l bags (50 x 30 cm). The production scale has currently reached a bag volume of 50 l (75 x 67 cm); using PIM and the conditions described above, it was possible to harvest more than 1.3 x 10(9) nematodes/bag (291 x 10(3) nematodes/g medium). In PIM, when sun flower oil was replaced with the same amount of fish oil or cod liver oil, yields of 259 x 10(3) and 290 x 10(3) nematodes/g medium, respectively, were attained. The technology for mass production and formulation of P. redivivus should enable fish-hatchery operators to rely on a cheap, standardised, and permanently available live food product for first feeding fish larvae.     

Enhancement of extracellular bispecific anti‐MUC1 nanobody expression in E. coli BL21 (DE3) by optimization of temperature and carbon sources through an autoinduction condition

Escherichia coli is one of the most suitable hosts for production of antibodies and antibody fragments. Antibody fragment secretion to the culture medium improves product purity in cell culture and diminishes downstream costs. In this study, E. coli strain BL21 (DE3) harboring gene encoding bispecific anti‐MUC1 nanobody was selected, and the autoinduction methodology for expression of bispecific anti‐MUC1 nanobody was investigated. Due to the replacement of IPTG by lactose as inducer, less impurity and toxicity in the final product were observed. To increase both intracellular and extracellular nanobody production, initially, the experiments were performed for the key factors including temperature and duration of protein expression. The highest amount of nanobody was produced after 21 h at 33°C. The effect of different carbon sources, glycerol, glucose, lactose, and glycine as a medium additive at optimum temperature and time were also assessed by using response surface methodology. The optimized concentrations of carbon sources were obtained as 0.75% (w/v), 0.03% (w/v), 0.1% (w/v), and 0.75% (w/v) for glycerol, glucose, lactose, and glycine, respectively. Finally, the production of nanobody in 2 L fermenter under the optimized autoinduction conditions was evaluated. The results show that the total titer of 87.66 µg/mL anti‐MUC1 nanobody, which is approximately seven times more than the total titer of nanobody produced in LB culture medium, is 12.23 µg/L .     

Construction of bioengineered yeast platform for direct bioethanol production from alginate and mannitol

Brown macroalgae are a sustainable and promising source for bioethanol production because they are abundant in ocean ecosystems and contain negligible quantities of lignin. Brown macroalgae contain cellulose, hemicellulose, mannitol, laminarin, and alginate as major carbohydrates. Among these carbohydrates, brown macroalgae are characterized by high levels of alginate and mannitol. The direct bioconversion of alginate and mannitol into ethanol requires extensive bioengineering of assimilation processes in the standard industrial microbe Saccharomyces cerevisiae. Here, we constructed an alginate-assimilating S. cerevisiae recombinant strain by genome integration and overexpression of the genes encoding endo- and exo-type alginate lyases, DEH (4-deoxy-l-erythro-5-hexoseulose uronic acid) transporter, and components of the DEH metabolic pathway. Furthermore, the mannitol-metabolizing capacity of S. cerevisiae was enhanced by prolonged culture in a medium containing mannitol as the sole carbon source. When the constructed strain AM1 was anaerobically cultivated in a fermentation medium containing 6% (w/v) total sugars (approximately 1:2 ratio of alginate/mannitol), it directly produced ethanol from alginate and mannitol, giving 8.8 g/L ethanol and yields of up to 32% of the maximum theoretical yield from consumed sugars. These results indicate that all major carbohydrates of brown macroalgae can be directly converted into bioethanol by S. cerevisiae. This strain and system could provide a platform for the complete utilization of brown macroalgae.     

Tea extract as an inexpensive inducer of pectin lyase in Penicillium griseoroseum cultured on sucrose

Extracts of tea, coffee, cocoa, and yeast induced pectin lyase (PL) in Penicillium griseoroseum cultured in a mineral medium with sucrose as the carbon source. PL activity and fungal growth were similar in the treatments with 0.5% tea extract, the highest concentration tested, and 0.03% yeast extract. When tea extract was added singly to the culture medium, P. griseoroseum produced 59% and 17% of the PL activity and mycelial mass, respectively, obtained in a treatment with tea extract and sucrose. These results suggest that the production of the enzyme was not proportional to mycelial growth. No PL was produced in the medium with sucrose and without inducers. The small amounts of pectic substances present in the tea extract could not be responsible for PL induction. PL activity was detected after 12 h of growth in the medium containing sucrose and tea extract added at time zero, and after 48 h of growth when tea extract was added at times 12 and 24 h. Mycelial mass in all treatments was similar after 48 h of incubation. However, the addition of tea extract at time zero increased PL activity by 20–25%. Cyclic AMP at 5 and 10 mM in the culture medium induced 20 and 30%, respectively, of the PL activity obtained with 0.03% yeast extract, suggesting that PL induction brought about by either yeast extract or tea extract might involve the intracellular metabolism of cAMP. Received 22 October 1996/ Accepted in revised form 09 January 1997     

Polysaccharide Produced by the Genus Pullularia: I. Production of Polysaccharide by Growing Cells

A dextranlike polysaccharide was found to be produced on substrates of sucrose, maltose, glucose, and fructose by growing cells of various strains of the genus Pullularia. The polysaccharide, obtainable in amounts as large as 2 to 3 g per 100 ml of culture medium using various carbohydrates as the carbon source, was soluble in cold water but not in 50% alcohol. The polysaccharide obtained had a α_d = +197.5° (c = 0.2 in water), and its molecular weight, determined by the light-scattering method, was found to be approximately 250,000.     

不同寡营养培养条件下南海水体细菌群落结构及其对碳源的利用特征

【背景】绝大多数海洋微生物不可培养,为挖掘海洋生态系统中可培养的微生物资源,研究者尝试寡营养培养等方法。【目的】比较不同寡营养培养条件下南海水体细菌数量、群落结构及其对碳源的利用特征差异。【方法】采用原2216E培养液(Y)、稀释10倍(Y-10)和稀释50倍(Y-50)的2216E培养液培养南海海水样品,用荧光定量PCR法和16S rRNA基因检测细菌数量和菌群结构;利用平板计数法计数异养细菌的数量,纯化鉴定可培养细菌;采用Biolog EcoPlateTM微板法分析不同培养基中细菌群落对碳源的利用特征。【结果】Y组细菌总数高于Y-10组和Y-50组,差异不显著(P>0.05),但异养细菌数量显著高于Y-10组和Y-50组(P<0.05)。16S rRNA基因测序结果表明,不同稀释倍数下的细菌群落结构差异明显,Y组检测出10门193属,优势类群为Proteobacteria(56.44%)和Bacteroides (37.27%);Y-10组检测出15门220属,优势类群为Proteobacteria (40.30%)、Bacteroides(36.91%)和Firmic...     

Enhanced production of surfactin from Bacillus subtilis by addition of solid carriers

Addition of a small quantity of solid porous carriers (e.g., activated carbon or expanded clay) into fermentation broth significantly increased surfactin production with Bacillus subtilis ATCC 21332. Culture medium containing 25 g L(-1) of activated carbon gave an optimal surfactin yield of 3600 mg L(-1), which was approximately 36-fold higher than that obtained from carrier-free liquid culture. The marked increase in surfactin production was primarily attributed to stimulation of cell growth due to the presence of activated carbon carriers. Concentration of limiting carbon substrate (glucose) is also an important factor affecting the production of surfactin, as an initial glucose concentration of 40 g L(-1) resulted in optimal surfactin production. An appropriate agitation rate also benefited surfactin production, as the best yield appeared at an agitation rate of 200 rpm. Surfactin was purified from fermentation broth via a series of acidic precipitation and solvent extraction. The resulting product was nearly 90% pure with a recovery efficiency of ca. 72%. The purified surfactin reduced the surface tension of water from 72 to 27 mN m(-1) with a critical micelle concentration of ca. 10 mg L(-1). The surfactin product also attained an emulsion index of 70% for kerosene and diesel at a low concentration of 100 and 600 mg L(-1), respectively.     

Defining an optimal carbon source/methionine feed strategy for growth and cephalosporin C formation by Cephalosporium acremonium.

The effect of the method of methionine addition, growth-limiting carbon source (glucose vs sucrose), and culture growth rate on cephalosporin C production was investigated in a Cephalosporium acremonium defined medium fed batch fermentation. Batch addition of methionine, at a concentration of 3 g/L, prior to the start of a fed sucrose fermentation was found to interfere with the ability of the culture to utilize this sugar, thus limiting growth and decreasing cephalosporin C production. Batch methionine addition had no effect on glucose-limited cultures. Concurrent exponential feeding of methionine with sucrose improved both culture growth and productivity. Under the control of identical carbon source limiting feed profiles, sucrose was observed to support greater cephalosporin C production than glucose. Optimal cephalosporin C production in a C. acremonium defined medium fed batch fermentation was obtained through controlling culture growth during the rapid growth phase at a relatively low level with respect to mumax (mu approximately 0.036 h-1) until achieving a desired cell mass with a concurrent sucrose and methionine feed, followed by maintaining relatively vigorous growth (mu approximately 0.01 h-1) with sucrose for the duration of the fermentation.     

利用重组大肠杆菌产聚-4-羟基丁酸的研究

重组大肠杆菌 E.coli XL-1 Blue（pKSSE5.3）携带Ralstonia　eutropha　H16的 PHA聚合酶基因（phaC）和Clostridium kluyveri的4-羟基丁酸:CoA转移酶基因（orfZ）,可以利用葡萄糖和4-羟基丁酸为碳源合成均聚的聚-4-羟基丁酸[P（4HB）]。优化培养基和培养条件后,进行了补料分批培养。结果表明,经68h左右培养,E.coli XL-1 Blue（pKSSE5.3）的发酵液中菌体干重达13g/L,P（4HB）的密度达5g/L,P（4HB）百分含量为36％。从收获的冻干细胞中提纯得到40g均聚的P（4HB）,为进一步分析检测P（4HB）生物、理化、加工特性及其应用价值成为可能。     

影响木薯次生胚状体发生及植株再生因素的研究

研究了在外植体的不同发育阶段中,碳源以及不同的生长激素配比对木薯次生胚状体诱导及植株再生的影响。结果表明：以固体成熟培养基上生长１５ｄ的胚状体子叶为外植体,次生胚状体的产量最高,达２９．３个成熟胚状体／１个外植体。在次生胚状体的诱导阶段,以麦芽糖（４０ｇ／Ｌ）代替蔗糖作碳源,能同时提高次生胚状体的产量（３２．５个胚次体／１个外植体）及植株再生频率（７４．３％）。２,４－Ｄ与ＰＰ３３３;（０．１ｍｇ／Ｌ）配合能提高植株再生频率到７７．６％。２,４－Ｄ与ＢＡＰ（２ｍｇ／Ｌ）或激动素（２．０ｍｇ／Ｌ）配合则大大降低了胚状体诱导及植株再生频率。     

Activity of pollulan synthesis by diploid culture of Pollularia pollulans on media with different sources of carbon

The diploid culture of Pullularia pullulans 1125(4)(13) synthesizes pullulan from different carbon sources. The activity is highest on a mineral medium with melassa (23.18 g/L). Pullulan is accumulated in great effectiveness on a medium with corn flour hydrolysate (48.23% of the carbon source amount).     

水产动物益生菌乳酸杆菌LH发酵工艺的研究

目的从生产实际出发,对1株高效乳酸杆菌（Lactobacillus spp）LH进行液体发酵培养基优化及发酵条件研究。方法通过碳源、氮源、无机盐、促生长素等单因子筛选及正交试验设计获得以下最佳培养基：糖蜜12 g/L,酵母膏5 g/L,蛋白胨1 g/L,葡萄糖4 g/L,玉米浆3 g/L,乙酸钠5 g/L,NaC l 5 g/L,K2HPO42.5 g/L,KH2PO42.5 g/L,MgSO40.5g/L,MnSO40.25 g/L。在此培养基上研究了该菌株最佳发酵条件。结果培养基初始pH 6.0,接种量2%（v/v,相对装液量）,500 m l三角瓶中装液量为500 m l,发酵温度为30～35℃,静置培养。在最佳培养条件下,LH活菌量达到1.74×10^9CFU/m l。结论通过活菌平板计数法测定了乳酸杆菌LH生长曲线,24 h为最佳种龄,生产收获时间是36 h。     

Rhamnolipid production in batch and fed-batch fermentation using<Emphasis Type="Italic">Pseudomonas aeruginosa</Emphasis> BYK-2 KCTC 18012P

The optimization of culture conditions for the bacteriumPseudomonas aeruginosa BYK-2 KCTC 18012P, was performed to increase its rhamnolipid production. The optimum level for carbon, nitrogen sources, temperature and pH, for rhamnolipid production in a flask, were identified as 25 g/L fish oil, 0.01% (w/v) urea, 25 and pH 7.0, respectively. Optimum conditions for batch culture, using a 7-L jar fermentor, were 200 rpm of agitation speed and a 2.0 L/min aeration rate. Under the optimum conditions, on fish oil for 216 h, the final cell and rhamnolipid concentrations were 5.3 g/L and 17.0 g/L respectively. Fed-batch fermentation, with different feeding conditions, was carried out in order to increase, cell growth and rhamnolipid production by thePseudomonas aeruginosa, BYK-2 KCTC 18012P. When 2.5 g of fish oil and 100 mL basal salts medium, containing 0.01% (w/v) urea, were fed intermittently during the fermentation, the final cell and rhamnolipid concentrations at 264 h, were 6.1 and 22.7 g/L respectively. The fed-batch culture resulted in a 1.2-fold increase in the dry cell mass and a 1.3-fold increase in rhamnolipid production, compared to the production of the batch culture. The rhamnolipid production-substrate conversion factor (0.75 g/g) was higher than that of the batch culture (0.68 g/g).     

Isolation and characterization of <Emphasis Type="Italic">Lentinus edodes</Emphasis> (Berk.) singer extracellular lectins

Lectin preparations have been isolated and purified from the culture liquid of the xylotrophic basidiomycete Lentinus edodes (Berk.) Singer [Lentinula edodes (Berk.) Pegler]. The culture of L. edodes F-249 synthesizes two extracellular lectins different in composition and physicochemical properties. Extracellular lectin L1 from L. edodes is a glycoprotein of mono-subunit structure with molecular weight of 43 kD. L1 is comprised of 10.5 +/- 1.0% (w/w) carbohydrates represented by glucose (Glc). Extracellular lectin L2 is a proteoglycan of mono-subunit structure with molecular weight of 37 kD. L2 is comprised of 90.3 +/- 1.0% (w/w) carbohydrates represented by Glc (73% of the total mass of the carbohydrate moiety of the lectin molecule) and galactose (Gal) (27% of the total mass of the carbohydrate part of the lectin molecule). The content of Asn in L2 is high, i.e. 42% (w/w) of total amino acids. This fact along with the composition of the carbohydrate part of the molecule (Glc + Gal) allows one to assign L2 to N-asparagine-bound proteins. Both lectins are specific to D-Gal and lactose (Lac) at an equal for L1 and L2 minimal inhibiting concentration of these carbohydrates (2.08 mM Gal and 8.33 mM Lac). Other carbohydrates to which the lectins show affinity are different for the two lectins: Rha (4.16 mM) for L1 and Ara (4.16 mM) and mannitol (8.33 mM) for L2. The purified extracellular lectins of L. edodes are highly selective at recognition of definite structures on the surface of trypsinized rabbit erythrocytes and do not react with the erythrocytes of other animals and humans.     

趋化因子受体CX3CR1调控人主动脉瓣膜间质细胞成骨分化的作用研究

目的:探究趋化因子受体CX3CR1调控人主动脉瓣膜间质细胞成骨分化的作用和机制,为钙化性主动脉瓣膜疾病的早期干预和治疗提供新思路。方法:取非钙化主动脉瓣(3例)和钙化主动脉瓣(5例),免疫组织化学染色检测成骨相关转录因子Runx2、骨桥蛋白OPN和骨钙蛋白OCN的表达;取3例非钙化的主动脉瓣,采用胶原酶连续消化法分离人主动脉瓣膜间质细胞,观察细胞形态及生长状态,并采用细胞免疫荧光进行表型鉴定。对成骨诱导培养的人主动脉瓣膜间质细胞分别过表达和干扰趋化因子受体CX3CR1,平行设置CM组、OM组和negative control+OM组,采用qPCR和Western blot检测Runx2、OPN和OCN的表达,Western blot检测AKT和p-AKT的表达。茜素红S染色评价晚期钙结节形成情况。结果:临床标本显示钙化的主动脉瓣较非钙化的主动脉瓣高表达CX3CR1(P 0. 05);成功分离人主动脉瓣膜间质细胞,α-SMA和Vimentin阳性,vWF阴性。与CM、OM、negative control组比较,CX3CR1+OM组Runx2、OPN和p-AKT表达上调(P 0. 05),且茜素红S染色可见明显钙结节;与CM、OM、negative siRNA control+OM组比较,si CX3CR1+OM组Runx2、OPN和p-AKT表达下调(P 0. 05),且茜素红S染色可见钙结节减少。结论:趋化因子受体CX3CR1可能通过AKT信号通路促进人主动脉瓣膜间质细胞成骨分化。     

不同浓度活性炭对墨兰离体培养的影响

以墨兰(Cymbidium sinense)地下根状茎段为外植体,探讨不同浓度活性炭对其离体培养的影响。结果表明,在MS+NAA 2.0 mg/L+10%椰汁的培养基中加入1.0 g/L活性炭对原球茎诱导效果最好;MS+BA 3.0 mg/L+NAA 0.5 mg/L+4.0 g/L活性炭适合于不定芽分化;在1/2 MS+NAA 1.0 mg/L+BA 0.5 mg/L+10%椰汁的培养基中加入0.5~3.0 g/L活性炭有利于提高成苗率。     

Strain‐specific consumption and transformation of alga‐derived dissolved organic matter by members of the Limnohabitans‐C and Polynucleobacter‐B clusters of Betaproteobacteria

We investigated changes in quality and quantity of extracellular and biomass‐derived organic matter (OM) from three axenic algae (genera Rhodomonas, Chlamydomonas, Coelastrum) during growth of Limnohabitans parvus, Limnohabitans planktonicus and Polynucleobacter acidiphobus representing important clusters of freshwater planktonic Betaproteobacteria. Total extracellular and biomass‐derived OM concentrations from each alga were approximately 20 mg l^?1 and 1 mg l^?1 respectively, from which up to 9% could be identified as free carbohydrates, polyamines, or free and combined amino acids. Carbohydrates represented 54%–61% of identified compounds of the extracellular OM from each alga. In biomass‐derived OM of Rhodomonas and Chlamydomonas 71%–77% were amino acids and polyamines, while in that of Coelastrum 85% were carbohydrates. All bacteria grew on alga‐derived OM of Coelastrum, whereas only Limnohabitans strains grew on OM from Rhodomonas and Chlamydomonas. Bacteria consumed 24%–76% and 38%–82% of all identified extracellular and biomass‐derived OM compounds respectively, and their consumption was proportional to the concentration of each OM compound in the different treatments. The bacterial biomass yield was higher than the total identifiable OM consumption indicating that bacteria also utilized other unidentified alga‐derived OM compounds. Bacteria, however, also produced specific OM compounds suggesting enzymatic polymer degradation or de novo exudation.     

Quantitative analysis of carbon balance in the reproductive organs and leaves of <Emphasis Type="Italic">Cinnamomum camphora</Emphasis> (L.) Presl

We investigated seasonal changes in dry mass and CO₂ exchange rate in fruit and leaves of the evergreen tree Cinnamomum camphora with the aim of quantitatively determining the translocation balance between the two organs. The fruit dry mass growth peaked in both August and October: the first increase was due to fruit pulp development and the second to seed development. Fruit respiration also increased with the rapid increase in fruit dry mass. Therefore, the carbohydrates required for fruit development showed two peaks during the reproductive period. Fruit photosynthesis was relatively high in early August, when fruit potentially re-fixed 75% of respired CO₂, indicating that fruit photosynthesis contributed 15–35% of the carbon requirement for fruit respiration. Current-year leaves completed their growth in June when fruit growth began. Current-year leaves translocated carbohydrates at a rate of approximately 10–25 mg dry weight (dw) leaf⁻¹ day⁻¹ into other organs throughout the entire fruit growth period. This rate of translocation from current-year leaves was much higher than the amount of carbohydrate required for reproduction (ca. 3 mg dw fruit⁻¹ day⁻¹). Given the carbon balance between fruit and current-year leaves, carbohydrates for reproduction were produced within the current-year fruit-bearing shoots. C. camphora would be adaptive for steadily supplying enough amount of carbohydrate to the fruits, as there was little competition for carbohydrates between the two organs. As assimilates by leaves are used for processes such as reproduction and the formation of new shoots, photosynthesis by reproductive organs is considered to be important to compensate for reproductive cost.     

营养条件对光滑球拟酵母积累α-酮戊二酸的影响

以光滑拟球酵母为研究模型,研究α-酮戊二酸的浓度情况。通过单因素实验得到α-酮戊二酸积累最佳浓度的各单因素条件为：葡萄糖浓度140g／L,NH4Cl浓度5g／L。在碳源（30g/L葡萄糖初始浓度）匮乏条件下加入丙酮酸30g／L,在此条件下丙酮酸转化为α－酮戊二酸的转化率最高达53．7％。以30g／L丙酮酸为唯一碳源时在7L发酵罐中光滑拟球酵母可生成浓度为10．7g/Lα-酮戊二酸,外源丙酮酸的转化率可达66．9％。这一结果表明,T．glabrata具有将丙酮酸转化为α-KG的能力。