Citric acid production by immobilized Aspergillus niger in a fluidized bed reactor

Summary Citric acid production by immobilized of Aspergillus niger in a fluidized bed reactor was performed, evaluating the productivity and the stability of the process when pulsing device was used. The application of a pulsing flow to fluidized bed reactor and the feed nitrogen limited allow to control of bioparticles morphology avoiding bed compactation. When operated at optimum pulsation frequency (0.3 s^–1) the stability of the bioreactor was maintained for more than 30 days, increasing the citric acid production in more than 52.2%.     

Fractionation of Aspergillus niger cellulases by combined ion exchange affinity chromatography

Eight chemically modified cellulose supports were tested for their ability to absorb components of the Aspergillus niger cellulase system. At least two of the most effective adsorbents, aminoethyl cellulose and carboxymethyl cellulose, were shown to be useful for the fractionation of cellulases. These supports apparently owe their resolving capacity to both ion exchange and biospecific binding effects; however, the relative importance of each effect is unknown. These observations form the basis for a new cellulase fractionation technique, combined ion exchange-affinity chromatography.     

黑曲霉原生质体诱变选育果胶酶高产菌株

通过UV和NTG诱变筛选获得了2株高产果胶酶突变株。以果胶酶产生菌黑曲霉EIM6为诱变材料,采用1．5％的溶壁酶和1．5％的纤维素酶处理其对教生长期菌丝体2h获得高质量的原生质体。采用UV25S或50μg／mL NTG诱变30min,构建原生质体突变库,经刚果红果胶平板筛选获得果胶酶突变株,通过液体深层培养复筛获得高产突变株EIM6-U11、EIM6-N5,酶活力分别从46598．08、46598．08U／mL提高至68596．57、68879．56U／mL,分别提高了47．21％、47．82％。连续8次传代经发酵测酶活力表明高产突变株EIM6-U11、EIM6-N5具有较高的遗传稳定性。     

Affinity precipitation of Aspergillus niger pectinase by microwave-treated alginate

Affinity precipitation is a simple, single plate separation process in which the complex of a smart macroaffinity ligand with the target protein (from a crude broth) can be selectively precipitated by application of a suitable stimulus. Alginate is a copolymer of guluronic acid and mannuronic acid residues and precipitates with Ca(2+) ions. It was found to bind to pectinase present in a commercial preparation of Aspergillus niger, Pectinex Ultra-SPL. Microwave pretreatment of alginate at 75 degrees C was found to enhance the selectivity of the affinity precipitation. Using microwave-treated alginate, 83% of the enzyme activity with 20-fold purification could be recovered. SDS-PAGE upon silver staining confirmed the enhanced selectivity of affinity precipitation when microwave-treated alginate was used.     

商品果胶酶中endo－PG的分离纯化及其部分性质研究

以Ａ．ｎｉｇｅｒ来源的果胶酶为材料,经过ＣＭ－ＳｅｐｈａｄｅｘＣ－５０及ＳｅｐｈａｄｅｘＧ－１００两步骤分离纯化得到电泳均一的ｅｎｄｏ－ＰＧ１及ｅｎｄｏ－ＰＧ２,其亚基分子量分别为３５ｋＤ及３７ｋＤ,含糖量为１１．２２％及８．３％,最大紫外吸收峰分别在２７４ｎｍ及２６９ｎｍ处,氨基酸组成分析结果表明Ｇｌｙ含量较高,Ｍｅｔ含量较低,不含Ｃｙｓ,并且酸性氨基酸含量高于碱性氨基酸,圆二色谱结果表明二级结构主要为α螺旋和β折叠,其中ｅｎｄｏ－ＰＧ１含α螺旋４５．１％,β折叠２４．９％;ｅｎｄｏ－ＰＧ２含α螺旋３９．６％,β折叠３６．５％。     

Transformation of yeast using calcium alginate microbeads with surface-immobilized chromosomal DNA

Yeast artificial chromosomes (YACs) are useful cloning vectors that have the capacity to carry large DNA inserts. The largest barrier to using such large DNA molecules in transformation experiments has been their physical instability in solution. We developed a new method of transforming yeast using chromosome-sized DNA. The method uses calcium alginate microbeads to immobilize high-density yeast chromosomal DNA. Chromosomal DNA immobilized on microbeads is physically stabilized compared with naked chromosomal DNA. The microbead-mediated transformation performed well, not only with respect to the transformation frequency with large DNA molecules (> 100 kb) but also in successful transformation using split chromosome DNA that exceeded 450 kb.     

Development of the magnetic beads for dye ligand affinity chromatography and application to magnetically stabilized fluidized bed system

Magnetic poly(2-hydroxyethylmethacrylate) [mPHEMA] beads were prepared by suspension polymerization of HEMA in the presence of Fe₃O₄ nano-powder. Cibacron Blue F3GA was covalently immobilized to the mPHEMA beads via nucleophilic substitution reaction between chloride of its triazine ring and hydroxyl groups of HEMA under alkaline conditions. The mPHEMA/Cibacron Blue F3GA beads (100–140 μm in diameter) carrying 68.3 μmol Cibacron Blue F3GA per gram polymer were used for β-casein adsorption studies. Adsorption studies were performed under different conditions in a batch system (i.e., pH, β-casein initial concentration, temperature, and ionic strength) and then in a magnetically stabilized fluidized bed (MSFB) system. The swelling ratio of the mPHEMA was 62.1%. The maximum adsorption capacity for batch system was 20.2% lower as compared to the value obtained in MSFB. The mPHEMA/Cibacron Blue F3GA beads could be repeatedly applied for β-casein adsorption without significant losses in the adsorption capacity.     

Purification of alpha-amylase isoenzymes from Scytalidium thermophilum on a fluidized bed of alginate beads followed by concanavalin A-agarose column chromatography

An alpha-amylase has been purified from the thermophilic fungus Scytalidium thermophilum. A ninefold purification was achieved in a single step using fluidized bed chromatography wherein alginate was used as the affinity matrix. There are at least two isoenzymes as shown by concanavalin A (Con A)-agarose column chromatography. The isoenzyme binding to Con A is stable for at least 3 h at 80 degrees C in the presence of calcium ions. The isoenzymes have similar molecular weights of around 45,000 Da as shown by SDS-PAGE analysis. The isoenzymes differ only slightly in their pH optima and temperature optima but the isoenzyme binding to Con A-agarose has slightly higher thermal stability.     

Affinity chromatography of amine oxidase from Aspergillus niger

ω-Aminohexyl-Sepharose 4B served as an excellent biospecific adsorbent for affinity chromatography of amine oxidase (monoamine:O₂ oxidoreductase (deaminating), EC 1.4.3.4) from Aspergillus niger. The enzyme was completely adsorbed on this affinity resin when applied to a column in 0.1 M potassium phosphate buffer (pH 7.2). Although a small part of the enzyme was retained on the column through ionic interaction and eluted with 1.0 M potassium phosphate buffer (pH 7.2), most of the enzyme adsorbed was eluted with 0.5 M potassium phosphate buffer (pH 7.2) containing 10 mM butylamine. Essentially no retention of the enzyme on a column of ε-aminopentyl-Sepharose or δ-aminobutyl-Sepharose occurred under the same conditions, indicating that an appropriate length (more than approx. 12 Å) of a hydrocarbon extension between the agarose matrix and the terminal amino group would be necessary for efficient adsorption of amine oxidase. The modification of the enzyme with 3-methyl-2-benzothiazolinone hydrazone (carbonyl inhibitor) or dithionite (reducing agent) resulted in loss of the ability to bind to ω-aminohexyl-Sepharose. I was also demonstrated that the affinity chromatography on ω-aminohexyl-Sepharose can be used as a powerful means of purifying this enzyme from crude extracts of Aspergillus niger. All of the three adsorbents were effective as a substrate in the amine oxidase reaction, but their substrate activities were as low as the corresponding free diamines.     

Evaluation of cellulose-based biospecific adsorbents as a stationary phase for lectin affinity chromatography

Macroporous cellulose Granocel was evaluated as a matrix for the immobilization of two lectins Concanavalin A (ConA) (108 kDa) and Wheat Germ Agglutinin (WGA) (36 kDa). Two different methods were employed for the immobilization of the lectins via their protein moieties by a Schiff's bases reaction. One of them results in covalent coupling of the lectin directly to the support and the other gives the attachment through a long spacer arm which benefits the immobilization of voluminous ConA molecules. The adsorbents were characterized by the glycoproteins sorption recording adsorption kinetic data and isotherms. The adsorbents demonstrated high affinity to glycoproteins with a sorption capacity in the column up to 7.4 mg/ml support and a high recovery (up to 93%). The adsorption isotherms of glucose oxidase (GOD) onto ConA adsorbents reveals an adsorption behavior with high and low affinity binding sites. The dissociation constant K(d) of the ligand-sorbate complex is approximately 1 x 10(-6) and 0.4 x 10(-5)M, respectively. It was supposed that the second step is related to the sorption of solvated GOD onto already adsorbed GOD forming sorbate dimers.     

Aspergillus niger pH 2.1 optimum acid phosphatase with high affinity for phytate

An extracellular acid phosphatase isolated from the culture of a wild strain Aspergillus niger, producing the dephosphorylating 3-phytase, was obtained in a homogeneous form by sequential application of ultrafiltration through PS 50 membrane, gel filtration on Sephadex G-100 and ion exchange chromatography on DEAE-Sepharose CL 6B and CM-Sepharose CL 6B. The enzyme showed a maximum catalytic value in a strongly acidic range (pH 2.0-2.4) with pHopt 2.1 and topt 66 degrees C. The acid phosphatase showed a wide substrate specificity and a high affinity for sodium phytate, 2.5x higher than with 4-nitrophenyl phosphate. This property of the acid phosphatase demonstrated that it is a potent 3-phytase at pH 2.1 and is of great significance for a practical application of the dephosphorylating complex--its addition to the diets of monogastric animals in view of the low pH values in the digestive tract.     

Affinity chromatography of amine oxidase from Aspergillus niger.

Omega-Aminohexyl-Sepharose 4B served as an excellent biospecific adsorbent for affinity chromatography of amine oxidase (monoamine:O2 oxidoreductase (deaminating), EC 1.4.3.4) from Aspergillus niger. The enzyme was completely adsorbed on this affinity resin when applied to a column in 0.1 M potassium phosphate buffer (pH 7.2). Although a small part of the enzyme was retained on the column through ionic interaction and eluted with 1.0 M potassium phosphate buffer (pH 7.2), most of the enzyme adsorbed was eluted with 0.5 M potassium phosphate buffer (pH 7.2) containing 10 mM butylamine. Essentially no retention of the enzyme on a column of epsilon-aminopentyl-Sepharose or delta-aminobutyl-Sepharose occurred under the same conditions, indicating that an appropriate length (more than approx. 12 A) of a hydrocarbon extension between the agarose matrix and the terminal amino group would be necessary for efficient adsorption of amine oxidase. The modification of the enzyme with 3-methyl-2-benzothiazolinone hydrazone (carbonyl inhibitor) or dithionite (reducing agent) resulted in loss of the ability to bind to omega-aminohexyl-Sepharose. It was also demonstrated that the affinity chromatography on omega-aminohexyl-Sepharose can be used as a powerful means of purifying this enzyme from crude extracts of Aspergillus niger. All of the three adsorbents were effective as a substrate in the amine oxidase reaction, but their substrate activities were as low as the corresponding free diamines.     

Dephosphorylation of phytate by using the Aspergillus niger phytase with a high affinity for phytate.

A phytase (EC 3.1.3.8) with a high affinity for phytic acid was found in Aspergillus niger SK-57 and purified to homogeneity in four steps by using ion-exchange chromatography (two types), gel filtration, and chromatofocusing. Sodium dodecyl sulfate-polyacrylamide gel electrophoresis of the purified enzyme gave a single stained band at a molecular mass of approximately 60 kDa. The Michaelis constant of the enzyme for phytic acid (18.7 +/- 4.6 microM) was statistically analyzed. In regard to the orthophosphate released from phytic acid, a significant difference between a low K(m) phytase from A. niger SK-57 and a high K(m) phytase from Aspergillus ficuum was recognized.     

Synthesis of functional proteins using Escherichia coli extract entrapped in calcium alginate microbeads

In this report, we describe the construction and analysis of a cell-free protein synthesis system immobilized in calcium alginate microbeads. When incubated in a feeding solution that contained amino acids and other low-molecular-weight substrates, the microbeads transcribed and translated coimmobilized DNA into functional proteins. Protein synthesis continued for more than 15 h with the diffusional supply of substrates and removal of by-products. In addition, functional proteins were generated from PCR-amplified genes as efficiently as from plasmid, suggesting that these cell-like microbeads could be used for functional screening of genomic libraries.     

Biodiesel production using Aspergillus niger as a whole‐cell biocatalyst in a packed‐bed reactor

Enzymatic lipase transesterification of palm oil to biodiesel in a packed‐bed reactor (PBR) using a novel strain of the fungus Aspergillus niger, immobilized within polyurethane biomass support particles (BSPs), was investigated. A three‐step addition of methanol was used to reduce lipase inhibition by immiscible methanol. The influence of water content and PBR flow rate was investigated. FAME yield was enhanced with an increase of PBR flow rate in the range of 0.15–30 L h^?1, where inefficient mixing of the reaction mixture at lower flow rates resulted in low conversion rates i.e. 69% after 72‐h reaction. Adding the third mole equivalent of methanol resulted in lipase inhibition due to methanol migration into the accumulated glycerol layer. Glutaraldehyde (GA) solution (0.5 vol.%) was used to stabilize lipase activity, which led to a high FAME yield (>90%) in the PBR after 72‐h of reaction time at a flow rate of 15 L h^?1, and a water content of 15%. Moreover, a high conversion rate (>85%) was maintained after four palm oil batch conversion cycles in the PBR. In contrast, lipase activity of non‐GA‐treated cells decreased with each PBR batch cycle, where only 70% FAME was produced after the forth PBR cycle. Transesterification of palm oil in a PBR system using BSPs‐immobilized A. niger as a whole‐cell biocatalyst is a viable process for enzymatic biodiesel production.     

Use of a tapered fluidized bed as a Continuous bioreactor

Reactor systems based on tapered fluidized beds are being developed for aqueous bioprocesses in which adhering microorganisms or immobilized active biological fractions are used. The use of a fluidized bed prevents biomass buildup, accommodates particulates in the feed stream, is compatible with gas sparging, and allows easy removal or addition of the active materials. The tapered reactor tends to stabilize the fluidized bed, thus allowing a much wider range of operating conditions. Preliminary experimental results and an empirical mathematical model of the tapered bed indicate that bed stability is associated with a decreasing velocity and void-fraction profile up the bed and the pressure drop across the bed decreases with increasing flow rates. The tapered fluidized bed bioreactor is being evaluated for use in the enzymatic production of hydrogen, microbiological denitrification, and microbiological degradation of coal conversion aqueous waste streams. The enzyme catalyzed conversion of lactose to glucose and galactose was used in the evaluation of the reactor concept.