Extraction and three-phase partitioning behavior of proteases from papaya peels

Dried papaya peels exhibited superior proteolytic activity to the fresh peels. An extraction with phosphate buffer pH 7.0 greatly maintained proteolytic activity when compared to water. SDS-PAGE verified that the extracted dried papaya peels held a wide range of proteins. To optimize the three-phase partitioning (TPP) for isolating the papaya peel proteases required a ratio of crude extract to t-butanol, the (NH₄)₂SO₄ concentration and the TPP cycles. The ratio of the crude extract to t-butanol of 1.0:0.5 with the presence of 20% (NH₄)₂SO₄ resulted in the highest proteolytic recovery at 253.5%, and 15.8-fold of purification in the bottom phase. The TPP was then optimized by adding up to 55% (NH₄)₂SO₄ to the bottom phase of the first step. A purification of 10.1-fold with about 89.4% recovery was obtained. This study showed the TPP can be effectively employed for the extraction of proteases from papaya peels.     

Potential application of aqueous two‐phase systems and three‐phase partitioning for the recovery of superoxide dismutase from a clarified homogenate of Kluyveromyces marxianus

Superoxide dismutase (SOD; EC 1.15.1.1) is an antioxidant enzyme that represents the primary cellular defense against superoxide radicals and has interesting applications in the medical and cosmetic industries. In the present work, the partition behavior of SOD in aqueous two‐phase systems (ATPS) (using a standard solution and a complex extract from Kluyveromyces marxianus as sample) was characterized on different types of ATPS (polymer–polymer, polymer–salt, alcohol–salt, and ionic liquid (IL)–salt). The systems composed of PEG 3350‐potassium phosphate, 45% TLL, 0.5 M NaCl (315 U/mg, 87% recovery, and 15.1‐fold purification) and t‐butanol‐20% ammonium sulfate (205.8 U/mg, 80% recovery and 9.8‐fold purification), coupled with a subsequent 100 kDa ultrafiltration stage, allowed the design of a prototype process for the recovery and partial purification of the product of interest. The findings reported herein demonstrate the potential of PEG‐salt ATPS for the potential recovery of SOD. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:1326–1334, 2014     

Synergistic Effect of Ultrasound and Three Phase Partitioning for the Extraction of Curcuminoids from Curcuma longa and its Bioactivity Profile

In the present work, ultrasound was combined with three-phase partitioning (UA-TPP) for the extraction of curcuminoids from Curcuma longa. The effect of various process parameters viz. solvents, irradiation time, ammonium sulphate concentration, ratio of turmeric aqueous slurry to t-butanol, turmeric powder to aqueous ratio, and ultrasonic power along with duty cycle on UA-TPP was examined. The yield of 67.15 mg/g was achieved using UA-TPP in 20 min irradiation time at room temperature (30 ± 2 °C) using 30% (w/v) ammonium sulphate saturation, 1:1 (v/v) turmeric aqueous slurry to t-butanol ratio, 1:30 (w/v) turmeric powder to solvent ratio with 22 kHz frequency, 60 W power and 60% (6 sec ON and 4 sec OFF) duty cycle. The comparison study was done based on extraction yields, time, energy requirement and process cost required by UA-TPP, conventional TPP and Soxhlet. UA-TPP found useful not only to enhance the process but also to improve the antioxidant capacity and anti-inflammatory activity of the extract in comparison with TPP.     

Three-phase partitioning of α-galactosidase from fermented media of <Emphasis Type="Italic">Aspergillus oryzae</Emphasis> and comparison with conventional purification techniques

Simple, attractive and versatile technique, three-phase partitioning (TPP) was used to purify α-galactosidase from fermented media of Aspergillus oryzae. The various conditions required for attaining efficient purification of the α-galactosidase fractions were optimized. The addition of n-butanol, t-butanol, and isopropanol in the presence of ammonium sulfate pushes the protein out of the solution to form an interfacial precipitate layer between the lower aqueous and upper organic layers. The single step of three-phase partitioning, by saturating final concentration of ammonium sulfate (60%) with 1:1 t-butanol, gave activity recovery of 92% with 12-fold purification at second phase of TPP. The final purified enzyme after TPP showed considerable purification on SDS-PAGE with a molecular weight of 64 kDa. The enzyme after TPP showed improved activity in organic solvents. Results are compared with conventional established processes for the purification of α-galactosidase produced by Aspergillus oryzae and overall the proposed TPP technique resulted in 70% reduction of purification cost compared to conventional chromatographic protocols.     

Purification and characterization of methyl mercaptan oxidase from<Emphasis Type="Italic">Thiobacillus thioparus</Emphasis> for mercaptan detection

Methyl mercaptan oxidase was successfully induced inThiobacillus thioparus TK-m using methyl mercaptan gas, and was purified for the detection of mercaptans. The purification procedure involved a DEAE (diethylaminoethyl)-Sephacel, or Superose 12, column chromatography, with recovery yields of 47.5 and 48.5%, and specific activities of 374 and 1240.8 units/mg-protein, respectively. The molecular weight of the purified methyl mercaptan oxidase was 66.1kDa, as determined by SDS-PAGE. The extract, from gel filtration chromatography, oxidizes methyl mercaptan, producing formaldehyde, which can be easily detected by the purpald-coloring method. The optimized temperature for activity was found to be at 55°C. This enzyme was inhibited by both NH₄Cl and (NH₄)₂SO₄, but was unaffected by either KCl or NaCl at less than 200 mM. With K₂SO₄, the activity decreased at 20 mM, but recovered at 150 mM. In the presence of methanol, full activity was maintained, but decreased in the presence of glycerin, ethanol and acetone 43, 78 and 75%, respectively.     

Three-phase partitioning as a rapid and efficient method for purification of invertase from tomato

Three-phase partitioning (TPP), a technique used in protein purification, was used to purify invertase from tomato (Lycopersicon esculentum). The method consists of simultaneous addition of ammonium sulfate and t-butanol to the crude enzyme extract in order to obtain the three phases. Different parameters (ammonium sulfate saturation, crude extract to t-butanol ratio and pH) essential for the extraction and purification of invertase were optimized to get highest purity fold and yield. It was seen that, 50% (w/v) ammonium sulfate saturation with 1:1 (v/v) ratio of crude extract to t-butanol at pH 4.5 gave 8.6-fold purification with 190% activity recovery of invertase in a single step. Finally, the purified enzyme was also characterized and the general biochemical properties were determined. The sodium dodecyl sulfate-polyacrylamide gel electrophoresis analysis of enzyme showed considerable purification and its molecular weight was nearly found to be as 20 kDa. This work shows that, TPP is a simple, quick and economical technique for purification of invertases.     

槐尺蠖多酚氧化酶的纯化及酶学特征

经40%饱和度硫酸铵分级沉淀,Sephadex G-100凝胶过滤等步骤,将槐尺蠖Semiothisa cinerearia Bremer et Grey 多酚氧化酶纯化,纯化倍数为6.96倍。该酶对焦性没食子酸,邻苯二酚和L多巴的Km值分别为0.23 mmol/L, 0.48 mmol/L和0.49 mmol/L。多酚氧化酶在pH 7.0,37℃时活性最高,并在40℃以上条件下,随着保温时间的延长酶活力下降。用槲皮苷和硫脲作抑制剂对该酶活性的抑制结果表明,这两种抑制剂分别属于竞争性和非竞争性抑制剂。     

Extraction of peroxidase from bitter gourd (Momordica charantia) by three phase partitioning with dimethyl carbonate (DMC) as organic phase

Three phase partitioning (TPP) is most renowned technique used for extraction and purification of natural products. In previous studies of TPP, t-butanol is mainly used as an organic phase. This is the first report that explores ability of dimethyl carbonate (DMC) in the field of TPP as an alternate solvent for t-butanol. In the present study TPP process with t-butanol and DMC as organic phase along with different salts was applied to waste bitter gourd powder to obtained peroxidase enzyme. DMC was found to be compatible with most of salts such as ammonium sulphate and sodium citrate and explored as more efficient solvent than t-butanol. This TPP system provides 4.84 fold purity of peroxidase enzyme at optimum source concentration of 0.15 g/mL, with a system comprising DMC as organic phase, sodium citrate (20%) as salt, agitation speed 120 rpm, pH 7, temperature 30 °C and extraction time of 3 h. Present study has aimed for extraction and separation of peroxidase from bitter gourd waste with TPP technique and ensures the scope of carbonated solvents in extraction and purification of proteins.     

α-Chymotrypsin shows higher activity in water as well as organic solvents after three phase partitioning

Alpha-Chymotrypsin was found to show a 119% increase in activity after three phase partitioning. The k_cat/K_m of the partitioned enzyme (TPP-C) for hydrolysis of Bz-Tyr-OEt in aqueous medium at 25°C was found to be 48.3×10⁴ mM^?1 min^?1 as compared to the corresponding value of 17.7×10⁴ mM^?1 min^?1 for the untreated control (C). The λ_max of the fluorescence emission spectrum of TPP-C showed 178% increase in the quantum yield when compared to C. TPP-C showed a 2.94 and 3.58 fold increase (as compared to C) in initial rates for formation of the ester Ac-Phe-OEt (from Ac-Phe and ethanol) in low water containing toluene and n-octane, respectively. It was found that TPP-C also showed the phenomenon of pH memory. At 5% (v v^?1) water (in t-amyl alcohol), while no esterification was observed with C, TPP-C still showed significant level of esterification activity.

Bz-Tyr-OEt, Benzoyl tyrosine ethyl ester; Ac-Phe, N-acetyl phenylalanine; Ac-Phe-OEt, N-acetyl phenylalanine ethyl ester; TPP, Three phase partitioning; C, Untreated α-chymotrypsin; TPP-C, α-Chymotrypsin subjected to TPP; k_cat, Catalytic efficiency; K_m, Michaelis constant     

Are nociceptin(1‐13)NH2 and its structural analogue [ORN9]nociceptin(1‐13)NH2 able to affect brain antioxidant status in control and kainic acid‐treated rats?

In‐vivo effects of nociceptin (N/OFQ(1‐13)NH₂) on the levels of lipid peroxidation and cell enzyme (superoxide dismutase, glutathione peroxidase and glutathione reductase) and non‐enzyme (glutathione) antioxidants in brain of control and kainic acid‐treated rats were studied. N/OFQ(1‐13)NH₂ effects were compared with those of its structural analogue [Orn⁹]N/OFQ(1‐13)NH₂. Kainic acid (25 µg, i.c.v) increased the lipid peroxidation (4 and 24 h after kainic acid treatment) and decreased the glutathione level (1 h after kainic acid injection). We failed to find, any changes in antioxidant enzyme activities, independently of the time of kainic acid treatment. At the background of kainic acid‐effects, N/OFQ(1‐13)NH₂ and [Orn⁹] N/OFQ(1‐13)NH₂, injected 30 min before kainic acid, had no effects on all parameters, tested in brain. In addition, the neuropeptides did not change the antioxidant status in brain of control animals. It might be concluded that N/OFQ(1‐13)NH₂ and [Orn⁹]N/OFQ(1‐13)NH₂ have neither pro‐ nor anti‐oxidant activity. Copyright © 2009 John Wiley & Sons, Ltd.     

Liquid–liquid extraction of antimicrobial peptide P34 by aqueous two-phase and micellar systems

Antimicrobial peptide P34 is a promising biopreservative for utilization in the food industry. In this work, aqueous biphasic systems (ABS) and aqueous biphasic micellar systems (ABMS) were studied as prestep for purification of peptide P34. The ABS was prepared with polyethylene glycol (PEG) and inorganic salts and the ABMS with Triton X-114 was chosen as the phase-forming surfactant. Results indicate that peptide P34 partitions preferentially to PEG-rich phase and extraction with ammonium sulfate [(NH₄)₂SO₄], yielding a 75% recovery of the antimicrobial activity, specific activity of 1,530 antimicrobial units per mg of protein, and purification fold of 2.48. Protein partition coefficient and partition coefficient for the biological activity with (NH₄)₂SO₄ system were 0.48 and 64, respectively. Addition of sodium chloride did not affect recovery, but decreased protein amount in the PEG-rich phase, indicating a higher partition of biomolecules. ABMS did not yield good recovery of antimicrobial activity. Purification fold using PEG–(NH₄)₂SO₄ and 1.0?mol l^?1 sodium chloride was twice higher than that obtained by conventional protocol, indicating a successful utilization of ABS as a step for purification of peptide P34.     

Application of microwave‐assisted extraction coupled with high‐speed counter‐current chromatography for separation and purification of Dehydrocavidine from Corydalis saxicola Bunting

Introduction – Dehydrocavidine is a major component of Corydalis saxicola Bunting with sedative, analgesic, anticonvulsive and antibacterial activities. Conventional methods have disadvantages in extracting, separating and purifying dehydrocavidine from C. saxicola. Hence, an efficient method should be established. Objective – To develop a suitable preparative method in order to isolate dehydrocavidine from a complex C. saxicola extract by preparative HSCCC. Methodology – The methanol extract of C. saxicola was prepared by optimised microwave‐assisted extraction (MAE). The analytical HSCCC was used for the exploration of suitable solvent systems and the preparative HSCCC was used for larger scale separation and purification. Dehydrocavidine was analysed by high‐performance liquid chromatography (HPLC) and further identified by ESI‐MS and 1H NMR. Results – The optimised MAE experimental conditions were as follows: extraction temperature, 60°C; ratio of liquid to solid, 20; extraction time, 15 min; and microwave power, 700 W. In less than 4 h, 42.1 mg of dehydrocavidine (98.9% purity) was obtained from 900 mg crude extract in a one‐step separation, using a two‐phase solvent system composed of chloroform–methanol–0.3 m hydrochloric acid (4 : 0.5 : 2, v/v/v). Conclusion – Microwave‐assisted extraction coupled with high‐speed counter‐current chromatography is a powerful tool for extraction, separation and purification of dehydrocavidine from C. saxicola. Copyright © 2009 John Wiley & Sons, Ltd.     

A new approach to ammonium sulphate feeding for fed‐batch Arthrospira (Spirulina) platensis cultivation in tubular photobioreactor

Arthrospira platensis was cultivated in tubular photobioreactor using different photosynthetic photon flux densities (PPFD) and protocols of (NH₄)₂SO₄ fed‐batch supply. Results were evaluated by variance analysis selecting maximum cell concentration (X_m), cell productivity (P_x), nitrogen‐to‐cell conversion factor (Y_X/N) and biomass, protein and lipid contents as responses. At PPFD of 120 and 240 μmol‐photons/m² s, a parabolic profile of (NH₄)₂SO₄ addition aiming at producing biomass with 7% nitrogen content ensured X_m values (14.1 and 12.2 g/L, respectively) comparable to those obtained with NaNO₃. At PPFD of 240 μmol‐photons/m² s, P_x (1.69 g/Ld) was 36% higher, although the photosynthetic efficiency (3.0%) was less than one‐half that at PPFD of 120 μmol‐photons/m² s. Biomass was shown to be constituted by about 35% proteins and 10% lipids, without any dependence on PPFD or kind of nitrogen source. These results highlight the possible use of (NH₄)₂SO₄ as alternative, cheap nitrogen source for A. platensis cultivation in tubular photobioreactors. © 2010 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Separation and determination of tetracycline hydrochloride in real water samples using binary small molecule alcohol‐salt aqueous two‐phase system coupled with high‐performance liquid chromatography

An environmental and sensitive sample pretreatment method was established and combined with high‐performance liquid chromatography (HPLC) for the analysis of tetracycline hydrochloride (TC) in feed water and lake water. One element small molecule alcohol‐salt aqueous two‐phase system (ATPS) cannot effectively adjust the polarity of the system, but binary small molecule alcohol‐salt ATPS can adjust the polarity and improve the extraction efficiency of antibiotics. In this work, a binary ATPS based on ethanol +2‐propanol + (NH₄)₂SO₄ system was formed and applied to the separation and purification of TC in real water samples. The influence factors on partition behaviors of TC were discussed, including the types and the concentration of phase salts, the volume ratio of alcohol, the pH value, extraction temperature, and the standing time. The response surface methodology was used to determine the best experimental conditions for multi‐factor experiments. Under this optimal condition, the extraction efficiency of TC reached 95.7%. This new method is considered to have significant application in the divorce of antibiotics.     

Fermentability of the hemicellulose‐derived sugars from steam‐exploded softwood (douglas fir)

Steam explosion ofDouglas fir wood chips under low‐severity conditions (log Ro = 3.08 corresponding to 175°C, 7.5 min, and 4.5% SO₂) resulted in the recovery of around 87% of the original hemicellulose component in the water‐soluble stream. More than 80% of the recovered hemicellulose was in a monomeric form. As the pretreatment severity increased from 3.08 to 3.76, hemicellulose recovery dropped to 43% of the original hemicellulose found in Douglas fir chips while the concentration of glucose originating from cellulose hydrolysis increased along with the concentration of sugar degradation products such as furfural and hydroxymethylfurfural. Despite containing a higher concentration of hexose monomers (mainly glucose originating from cellulose degradation), the water‐soluble fraction prepared under high‐severity conditions (log Ro = 3.73 corresponding to 215°C, 2.38 min, and 2.38% SO₂) was not readily fermented. Only the two hydrolyzates obtained at low and medium (195°C, 4.5 min, and 4.5% SO₂) severities were fermented to ethanol using a spent sulfur liquor adapted strain of Saccharomyces cerevisiae. High ethanol yields were obtained for these two hydrolyzates with 0.44 g of ethanol produced per gram of hexose utilized (86% of theoretical). However, the best results of hemicellulose recovery and fermentability were obtained for the low‐severity water‐soluble fraction which was fermented significantly faster than the fraction obtained after medium‐severity treatment probably because it contained higher amounts of fermentation inhibitors. © 1999 John Wiley & Sons, Inc. Biotechnol Bioeng 64: 284–289, 1999.     

A three‐phase excess post‐exercise oxygen consumption in Atlantic salmon Salmo salar and its response to exercise training

The recovery of oxygen uptake to the standard metabolic rate (SMR) following exhaustive chasing exercise in Atlantic salmon Salmo salar parr occurred in three phases (rapid, plateau and slow). The initial recovery phase lasted 0·7 h and contributed 16% to the total excess post‐exercise oxygen consumption (EPOC). It was followed by a longer plateau phase that contributed 53% to the total EPOC. The slow recovery phase that completed recovery of SMR, which has not been reported previously, made a 31% contribution to the total EPOC. The plasticity of EPOC was demonstrated in exercise‐trained fish. Exercise training increased EPOC by 39% when compared with control fish (mean ± S.E., 877·7 ± 73·1 v . 629·2 ± 53·4 mg O₂ kg^?1, d.f. = 9, P <  0·05), with the duration of the plateau phase increasing by 38% (4·7 ± 0·58 v . 3·4 ± 0·16 h, d.f. = 9, P <  0·05) and the contribution of the slow phase to the total EPOC increasing by 80% (173·9 ± 23·9 v . 312·5 ± 50·4 mg O₂ kg^?1, d.f. = 9, P  < 0·05). As a result, the combination of the plateau and slow phases of exercise‐trained fish increased by 47% compared with control fish (756·6 ± 71·4 v . 513·6 ± 43·1 mg O₂ kg^?1; d.f. = 9, P  = 0·01). To substantiate the hypothesis that the plateau and slow recovery phase of EPOC was related to general metabolic recovery following exhaustive exercise, the time‐course for recovery of SMR was compared with previously published metabolite recovery profiles. The final phase of metabolic recovery was temporally associated with the final phases of gluconeogenesis, lactate oxidation and muscle intracellular pH regulation. Therefore, the plasticity of the latter phase of EPOC agreed with the known effects of exercise training in fishes.     

Salt‐enhanced cultivation as a morphology engineering tool for filamentous actinomycetes: Increased production of labyrinthopeptin A1 in Actinomadura namibiensis

Salt‐enhanced cultivation as a morphology engineering tool for the filamentous actinomycete Actinomadura namibiensis was evaluated in 500‐mL shaking flasks (working volume 100 mL) with the aim of increasing the concentration of the pharmaceutically interesting peptide labyrinthopeptin A1. Among the inorganic salts added to a complex production medium, the addition of (NH₄)₂SO₄ led to the highest amount of labyrinthopeptin A1 production. By using 50 mM (NH₄)₂SO₄, the labyrinthopeptin A1 concentration increased up to sevenfold compared to the non‐supplemented control, resulting in 325 mg L^?1 labyrinthopeptin A1 after 10 days of cultivation. The performance of other ammonium‐ and sulfate‐containing salts (e.g., NH₄Cl, K₂SO₄) was much lower than the performance of (NH₄)₂SO₄. A positive correlation between the uptake of glycerol as one of the main carbon sources and nongrowth‐associated labyrinthopeptin productivity was found. The change in the cell morphology of A. namibiensis in conjunction with increased osmolality by the addition of 50 mM (NH₄)₂SO₄, was quantified by image analysis. A. namibiensis always developed a heterogeneous morphology with pellets and loose mycelia present simultaneously. In contrast to the non‐supplemented control, the morphology of (NH₄)₂SO₄‐supplemented cultures was characterized by smaller and circular pellets that were more stable against disintegration in the stationary production phase.     

Highly efficient enzymatic synthesis of an ascorbyl unstaturated fatty acid ester with ecofriendly biomass‐derived 2‐methyltetrahydrofuran as cosolvent

Enzymatic synthesis of ascorbyl undecylenate, an unsaturated fatty acid ester of ascorbic acid, was reported with biomass‐derived 2‐methyltetrahydrofuran (MeTHF) as the cosolvent. Of the immobilized lipases tested, Candida antarctica lipase B (CAL‐B) showed the highest activity for enzymatic synthesis of ascorbyl undecylenate. Effect of reaction media on the enzymatic reaction was studied. The cosolvent mixture, t‐butanol‐MeTHF (1:4, v/v) proved to be the optimal medium, in which not only ascorbic acid had moderate solubility, but also CAL‐B showed a high activity, thus addressing the major problem of the solvent conflict for dissolving substrate and keeping satisfactory enzyme activity. In addition, the enzyme was much more stable in MeTHF and t‐butanol‐MeTHF (1:4) than in previously widely used organic solvents, t‐butanol, 2‐methyl‐2‐butanol, and acetone. The much higher initial reaction rate in this cosolvent mixture may be rationalized by the much lower apparent activation energy of this enzymatic reaction (26.6 vs. 38.1–39.1 kJ/mol) and higher enzyme catalytic efficiency (V_max/K_m, 8.4 vs. 1.3–1.4 h^?1). Ascorbyl undecylenate was obtained with the yields of 84–89% and 6‐regioselectivity of >99% in t‐butanol‐MeTHF (1:4) at supersaturated substrate concentrations (60 and 100 mM) after 5–8 h. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:1005–1011, 2014     

Production of biobutanol from acid-pretreated corncob using Clostridium beijerinckii TISTR 1461: Process optimization studies

Corncob is a potential feedstock in Thailand that can be used for fermentable sugar production through dilute sulfuric acid pretreatment and enzymatic hydrolysis. To recover high amounts of monomeric sugars from corncob, the sulfuric pretreatment conditions were optimized by using response surface methodology with three independent variables: sulfuric acid concentration, temperature, and time. The highest response of total sugars, 48.84 g/L, was found at 122.78°C, 4.65 min, and 2.82% (v/v) H₂SO₄. With these conditions, total sugars from the confirmation experiment were 46.29 g/L, with 5.51% error from the predicted value. The hydrolysate was used as a substrate for acetone–butanol–ethanol fermentation to evaluate its potential for microbial growth. The simultaneous saccharification and fermentation (SSF) showed that C. beijerinckii TISTR 1461 can generate acetone–butanol–ethanol products at 11.64 g/L (5.29 g/L acetone, 6.26 g/L butanol, and 0.09 g/L ethanol) instantly using sugars from the hydrolysed corncob with Novozymes 50013 cellulase enzyme without an overliming process.     

Improved Microbial Production of Colominic Acid,a Homopolymer of N-Acetylneuraminic Acid

A culture medium has been devised for producing colominic acid in improved yields. Major improvements were obtained by using sorbitol as a source of carbon, by adding phosphate in high concentrations, and by supplementing a limited amount of yeast extract. E. coli O 16: Kl: HNM produced approximately 3000 µg/ml of colominic acid on cultivation at 37°C for 46 hr with a liquid medium consisting of sorbitol (2.0%), (NH₄)₂SO₄ (0.5%), K₂HPO₄ (1.4%), MgSO₄·7H₂O (0.05%), and yeast extract (0.05%).

Isolation and purification by deproteinization with ammonium sulfate, precipitation with ethanol, and by column chromatography on anion exchange resins resulted in a pure colominic acid preparation devoid of internal ester linkages.

In producing colominic acid, strains forming S-type colonies were more active than those forming R-type colonies.