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Query: UMLS:C0085631 (agitation)
 12,064 document(s) hit in 31,850,051 MEDLINE articles (0.00 seconds)

A bacterial strain named GA1 which can produce bioflocculant with high flocculating activity was isolated from soil. The strain was identified as Paenibacillus polymyxa according to its morphological, physiological and biochemical characters, as well as 16S rDNA sequence (GenBank Accession number: DQ166375) similarity comparison. The results indicated that sucrose and yeast extract were the optimal carbon and nitrogen sources for bioflocculant production. Furthermore, the mass ratio of sucrose to yeast extract and the optimal sucrose concentration were ascertained. The optimum component proportion of medium (g/L) is sucrose 40.0, yeast extract 4.0, K2HPO4 5.0, KH2PO4 2.0, NaCl 0.1, MgSO4 0.2. The culture conditions including initial pH, temperature, agitation rate and inoculation quantity of strain GA1 were ascertained. Based on the relation of bacterium growth and bioflocculant production, grading culture was applied to bioflocculant production of GA1. The experimental result show that grading culture can keep high bioflocculant yield as well as shorten time of flocculant production.
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PMID:[Culture medium and grading culture technics for bioflocculant production by Paenibacillus polymyxa GA1]. 1688 27

It is widely accepted that it is possible to successfully cryopreserve human ovarian tissue by direct plunging into liquid nitrogen using permeable cryoprotectants only, without disaccharides. This study aimed to search for and test a new method for in-vitro culture of vitrified tissue. Ovarian biopsies were obtained during operative laparoscopy. Pieces of ovarian tissue were vitrified and warmed. After warming, tissue pieces were randomly distributed into three groups for further culture: in 2 ml of culture medium which was regularly renewed (group 1), in 30 ml of culture medium without agitation (group 2) and in 30 ml of culture medium with agitation (group 3). During the 2-week and 6-week culture, the growth of follicles within the vitrified-warmed ovarian tissue pieces was investigated. After 2 weeks of culture, mean numbers of non-degenerated follicles per mm(2) of tissue were 1.5, 1.7 and 4.5 for groups 1, 2 and 3 respectively (groups 1 and 2 versus group 3, P < 0.05). Agitation during culture of ovarian tissue is beneficial, and can be used as a prognostic tool for future warming and autotransplantation of ovarian tissue.
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PMID:Effective method for in-vitro culture of cryopreserved human ovarian tissue. 1689 38

Moringa oleifera pods Lamarck (Drumstick or Horseradish) is a multipurpose medium or small size tree from sub-Himalayan regions of north-west India and indigenous to many parts of Asia, Africa, South America, and in the Pacific and Caribbean Islands. Its pods (MOP) have been employed as an inexpensive and effective sorbent for the removal of organics, i.e., benzene, toluene, ethylbenzene and cumene (BTEC) from aqueous solutions using HPLC method. Effect of different parameters, i.e., sorbent dose 0.05-0.8g, 25cm(-3) agitation time 5-120min, pH 1-10, temperature 283-308K and concentration of sorbate (1.3-13)x10(-3), (1.1-11)x10(-3), (0.9-9)x10(-3), (0.8-8)x10(-3)moldm(-3), on the sorption potential of MOP for BTEC have been investigated. The pore area and average pore diameter of the MOP by BET method using nitrogen as a standard are calculated to be 28.06+/-0.8m(2)g(-1) and 86.2+/-1.3nm respectively. Freundlich, Langumir and Dubinin-Radushkevich (D-R) sorption isotherms were employed to evaluate the sorption capacity of MOP. Sorption capacities of BTEC onto MOP have been found to be 46+/-10, 84+/-9, 101+/-4, 106+/-32mmolg(-1) by Freundlich, 8+/-0.1, 9+/-0.1, 10+/-0.3, 9+/-0.1mmolg(-1) by Langumir and 15+/-1, 21+/-1, 23+/-2, 22+/-3mmolg(-1) by D-R isotherms respectively, from BTEC solutions at 303K. While the mean energy of sorption process 9.6+/-0.3, 9.2+/-0.2, 9.3+/-0.3, 9.5+/-0.4kJmol(-1) for BTEC is calculated by D-R isotherm only. Rate constant of BTEC onto MOP 0.033+/-0.003, 0.030+/-0.002, 0.029+/-0.002, 0.027+/-0.002min(-1) at solution concentration of 1.3x10(-3), 1.1x10(-3), 0.9x10(-3) and 0.8x10(-3)moldm(-3) and at 303K have been calculated by employing Lagergren equation. Thermodynamic parameters DeltaH -8+/-0.4, -10+/-0.6, -11+/-0.7, -11+/-0.7kJmol(-1), DeltaS -22+/-2, -26+/-2, -27+/-2, -29+/-3Jmol(-1)K(-1) and DeltaG(303K) -0.9+/-0.2, -1.9+/-0.2, -2.3+/-0.1 and -2.6+/-0.2kJmol(-1) were also estimated for BTEC respectively at temperatures 283-308K. The negative values of DeltaH, DeltaS and DeltaG suggest exothermic, stable (with no structural changes at solid-liquid interface) and spontaneous nature of sorption process under optimized conditions. MOP has been used extensively to accrue and then to preconcentrate benzene, toluene and ethylbenzene in wastewater sample.
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PMID:Sorption potential of Moringa oleifera pods for the removal of organic pollutants from aqueous solutions. 1693 Aug 26

A procedure for the determination of eight organophosphate flame retardants and plasticizers in dust samples is presented. Microwave-assisted extraction and gas chromatography (GC) with nitrogen-phosphorus detection (NPD) were used for sample preparation and analytes quantification, respectively. Influence of different variables (type and volume of organic solvent, temperature, time, agitation, etc.) on the yield of the extraction step was evaluated. The most important factor was the type of solvent, with the highest efficiencies corresponding to acetone. Under final conditions 10 mL of this solvent were employed. The extraction was carried out at 130 degrees C and satisfactory yields, similar to those obtained with the Soxhlet technique, were achieved. Due to the high content of organic carbon in dust samples, primary acetone extracts had to be subjected to intensive clean-up. Dilution with ultrapure water followed by concentration on a reversed-phase sorbent and further purification using silica, allowed a significant reduction of co-extracted interferences. Application of the developed methodology to indoor dust from private houses showed important concentrations of several organophosphate esters. The highest levels, up to 19 microg/g, corresponded to tris(butoxyethyl) phosphate; moreover, average values of two chlorinated compounds, used as flame retardants and considered as the most concerning species in the group, exceeded the 1 microg/g level.
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PMID:Microwave-assisted extraction of organophosphate flame retardants and plasticizers from indoor dust samples. 1714 May 88

This study presents an assessment of the kinetic, mass transfer and hydrodynamic parameters of a pilot-scale fixed bed reactor containing immobilized biomass in polyurethane matrices and fed with the effluent of a horizontal-flow fixed bed anaerobic reactor, which was used to treat domestic sewage. It was found that the liquid-solid and intra-particle mass transfer resistances significantly affected the overall oxygen consumption rate and that mechanical agitation could minimize such resistances. The volumetric oxygen transfer coefficient (kLa) values for superficial air velocities between 8.4 cm min(-1) and 57.0 cm min(-1) varied from 20.8 h(-1) to 58.8 h(-1) for tap water, and 16.8 h(-1) to 53.0 h(-1) for the anaerobic pre-treated effluent. The intrinsic oxygen uptake rate was estimated to be 19.9 mgO2 gVSS(-1) h(-1). A first-order kinetic model with residual concentration was considered to adequately represent the COD removal rate, whereas nitrogen conversion was considered to be well represented by a model of pseudo-first-order reaction in series. It was also found that the ammonium conversion to nitrite was the limiting step of the overall nitrogen conversion rate. The hydrodynamic behavior of the reactor was represented by three to four completely mixed reactors in series.
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PMID:Kinetics, mass transfer and hydrodynamics in a packed bed aerobic reactor fed with anaerobically treated domestic sewage. 1714 61

Uniform-sized agarose beads were prepared by membrane emulsification technique in this study. Agarose was dissolved in boiling water (containing 0.9% sodium chloride) and used as water phase. A mixture of liquid paraffin and petroleum ether containing 4 wt% of hexaglycerin penta ester (PO-500) emulsifier was used as oil phase. At 55 degrees C, the water phase permeated through uniform pores of microporous membrane into the oil phase by a pressure of nitrogen gas to form uniform W/O emulsion. Then the emulsion was cooled down to room temperature under gentle agitation to form gel beads. The effect of oil phase, emulsifier, especially temperature on the uniformity of the beads were investigated and interpreted from interfacial tension between water phase and oil phase. Under optimized condition, the coefficient variation (C.V.) showing the size distribution of the beads was under 15%. This was the first report to prepare uniform agarose beads by membrane emulsification, and to investigate the effect of temperature on the size distribution of the droplets and beads. The beads with different size can be prepared by using membranes with different pore size, and the result showed that there was a linear relationship between the average diameter of beads and pore size of the membranes; beads with diameter from 15 to 60 microm were able to obtain in this study.
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PMID:Preparation of uniform-sized agarose beads by microporous membrane emulsification technique. 1736 74

It was found that the soil-dwelling fungus Rhizoctonia praticola 93A was capable to produce laccase in submerged cultures. Effects of culture conditions on the enzyme biosynthesis in shaken flask and aerated bioreactor cultures were evaluated to improve the yields of the process. Production of extracellular laccase was considerably intensified by the addition of Cu2+ to a carbon-limited and nitrogen-sufficient culture medium (C/N = 0.98). When an optimized medium containing glucose (2 g/l) and L-asparagine (1.5 g/l) was used and enzyme synthesis was stimulated by addition of 5 microM Cu2+ before inoculation, maximal laccase activities obtained in a batch cultivation were, approximately, 1000 nkat/l. Under these conditions, addition to the medium of the aromatic inducer 2,5-xylidine (1 mM) led to a 10-fold increase in laccase activity. Laccase productivity in shaken flask cultures was also enhanced (to more than 4000 nkat/l on day 3) by using a medium with the initial pH of 7.5. Such a high value of the optimal medium pH for laccase production by R. praticola is exceptional among the ligninolytic fungi. In fermenter fungal cultures supplemented with cupric ions, the highest laccase activity (about 4000 nkat/l after 3 days' cultivation) was reached after 24-h incubation using a bioreactor with the aeration rate of 21/min, the agitation speed of 200 rpm, and a constant medium pH of 8.0.
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PMID:Effects of culture conditions on production of extracellular laccase by Rhizoctonia praticola. 1741 68

In filamentous fungi, including the model organism Neurospora crassa, plentiful biological tissue from which RNA can be extracted may be obtained by allowing fungal spores to germinate and form a mycelium in liquid culture. The mycelium constitutes a mosaic of multinuclear, tubular filaments known as hyphae or mycelia. In general, when exposed to air, fungal hyphae quickly start to develop spores, which are often colorful. However, when submerged in liquid under rapid agitation large amounts of vegetatively growing mycelium can be obtained, which can be easily harvested by means of filtration. To preserve the physiological state of the culture, the mycelium is snap-frozen, and then to free its contents, the mycelium is ground under liquid nitrogen to break all hyphal structures. Here a method to extract high-quality total RNA from Neurospora mycelium using TRIzol reagent is described.
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PMID:Isolation of total RNA from Neurospora mycelium. 1741 16

Porous carbon has been prepared from waste antibiotic material by a chemical activation method using K(2)CO(3) as an activating reagent. Carbon was studied systematically by the adsorption of nitrogen and iodine. It was found that the process parameters such as activation temperature and activation time are crucial for preparing high-quality activated carbon. The proper choice of the preparation conditions allows to produce microporous activated carbon with a micropore volume up to 0.492 cm(3)/g and a BET surface area of 1260 m(2)/g. Adsorption of mercury(II) from an aqueous solution on antibiotic carbon was investigated under the varying conditions of agitation time, metal ion concentration and pH. The adsorption capacity of the carbon is 129 mg/g.
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PMID:Use of an activated carbon from antibiotic waste for the removal of Hg(II) from aqueous solution. 1742 4

An indigenous strain Pseudomonas aeruginosa S2 (P. aeruginosa S2), isolated from diesel-contaminated soil, produced extracellular surface-active material identified as rhamnolipid. Due to its excellent surface activity, rhamnolipid is known to be well-suited for stimulating the bioremediation efficiency of oil contaminated sites. To improve production yield of rhamnolipid with P. aeruginosa S2, various carbon and nitrogen sources were screened to select favorable ones leading to better biosurfactant production yield. It was found that using 4% glucose could attain better rhamnolipid yield, while 50 mM NH4NO3 appeared to be the most preferable nitrogen source. Meanwhile, the effect of carbon to nitrogen ratio (C/N ratio) on rhamnolipid yield was also investigated, and the optimal C/N ratio was identified as approximately 11.4. Moreover, response surface methodology (RSM) was applied to optimize the trace element concentration for rhamnolipid production. Results from two-level design indicate that concentrations of MgSO4 and FeSO4 were the most significant factors affecting rhamnolipid production. Using steepest ascent method and RSM analysis, an optimal medium composition was determined, giving a rhamnolipid production yield of 2.37 g/L in 100 h at 37 degrees C and 200 rpm agitation. Scale-up production of rhamnolipid in a well-controlled 5 L jar fermentor using the optimal medium and operating condition (at 37 degrees C and pH 6.8) further elevated the biosurfactant production yield to 5.31 g/L (in 97 h), which is over 2-fold higher than the best results obtained from shake-flask tests.
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PMID:Improved production of biosurfactant with newly isolated Pseudomonas aeruginosa S2. 1746 51


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