Large-scale preparation of clove essential oil and eugenol-loaded liposomes using a membrane contactor and a pilot plant

Based on our previous study where optimal conditions were defined to encapsulate clove essential oil (CEO) into liposomes at laboratory scale, we scaled-up the preparation of CEO and eugenol (Eug)-loaded liposomes using a membrane contactor (600?mL) and a pilot plant (3?L) based on the principle of ethanol injection method, both equipped with a Shirasu Porous Glass membrane for injection of the organic phase into the aqueous phase. Homogenous, stable, nanometric-sized and multilamellar liposomes with high phospholipid, Eug loading rates and encapsulation efficiency of CEO components were obtained. Saturation of phospholipids and drug concentration in the organic phase may control the liposome stability. Liposomes loaded with other hydrophobic volatile compounds could be prepared at large scale using the ethanol injection method and a membrane for injection.     

Ethanol injection method for hydrophilic and lipophilic drug-loaded liposome preparation

In this article, a hydrophobic (beclomethasone dipropionate; BDP) and a hydrophilic (cytarabine; Ara-C) drugs have been encapsulated in liposomes in order to be administered via the pulmonary route. For this aim, a liposome preparation method, which is easy to scale up, the ethanol injection method, has been selected. The effects of critical process and formulation parameters have been investigated. The drug-loaded liposomes were prepared and characterized in terms of size, zeta potential, encapsulation efficiency, release study, cell uptake, and aerodynamic behavior. Small multilamellar vesicles, with sizes ranging from about 80 to 170?nm, were successfully obtained. Results indicated a significant influence of phospholipid and cholesterol amounts on liposome size and encapsulation efficiency. The higher encapsulation efficiencies were about 100% for the hydrophobic drug (BDP) and about 16% for the hydrophilic one (Ara-C). The in vitro release study showed a prolonged release profile for BDP, in contrast with Ara-C, which was released more rapidly. The cell-uptake test revealed that fluorescent liposomes have been well internalized into the cytoplasm of SW-1573 human lung carcinoma cells, confirming the possibility to use liposomes for lung cell targeting. Nebulized Ara-C and BDP liposomes presented aerodynamic diameters compatible with deep lung deposition. In conclusion, the elaborated liposomes seem to be promising carriers for both Ara-C and BDP pulmonary delivery.     

A method of calculating the liposome membrane permeability using dialysis method

A correct mode of calculating liposome membrane permeability determined with dialysis is proposed. The liposome membrane permeability is calculated with regard for the ion passage through two diffusion barriers: liposomal membrane and cellophane membrane. The asymmetrical ion distribution under equilibrium conditions is shown. The asymmetry is due to the formation of unstirred layers near the membrane. The equilibrium ion concentration in unstirred layers and the measured average bulk concentration in solution are different. The formula for calculating liposome membrane permeability that takes the mentioned factors into account is suggested.     

A scalable membrane gradostat reactor for enzyme production using Phanerochaete chrysosporium

This is the first demonstration of process scale-up of a membrane gradostat reactor for continuous enzyme production using Phanerochaete chrysosporium ME446. The fungus was immobilised by reverse filtration on to externally unskinned, ultrafiltration capillary membranes and then nutrient gradients were induced across the biofilm. A 10-fold scale-up from a single capillary bioreactor to a 2.4 l multi-capillary unit resulted in a 7-fold increase in enzyme productivity with a peak at 209 U l^–1 d^–1. Subsequent scale effects on the spore distribution, continuous manganese peroxidase production profile and biofilm development are discussed.     

A new simple preparation method for NaK-ATPase-rich membrane fragments

A method for the isolation of highly active membrane bound NaK-ATPase without detergents in quantity from the electric organ of the electric eel (Electrophorus electricus) is described. This method consists of the homogenation of electric organ with an isotonic solution containing sucrose, histidine, EDTA, and arginine, and of the separation of the higher active membrane fraction from the microsomal fraction by density gradient centrifugation. The enzyme has a specific activity of about 20 μmol Pi/min/mg at 37°C, and 13 μmol Pi/min/mg at 30°C. Although it is not as pure as the detergent-treated enzyme preparation based on the level of phosphorylated protein, ouabain binding, or sodium dodecyl sulfate-polyacrylamide gel electrophoresis, its enzyme activity is comparable to that of the purified enzymes. This preparation is very stable and is able to change its medium by Sephadex chromatography without any loss of enzyme activity and protein content. This preparation is also expected to keep the original characteristics as well as the enzyme in the tissue.     

Treatment of heavy metal-polluted wastewaters using the biofilms of a multistage rotating biological contactor

The ability of the biofilms of a three-stage rotating biological contactor (RBC) to treat wastewater contaminated with cadmium, copper and zinc was investigated. The system successfully removed the metals, in the order Cu > Zn > Cd with removal capacities of approximately 73, 42 and 33% respectively. Analysis of the contribution of each reactor indicated that metal removal was not uniform, with Reactor 1 showing a much higher removal capacity than Reactors 2 and 3. Energy dispersive X-ray spectroscopy (EDS) revealed the presence of all three metals on the surface of the biofilms in all three reactors. Closer inspection of the biofilms, in terms of biomass and biofilm thickness, revealed that the low metal removal in Reactors 2 and 3 was probably attributable to poor biofilm development in these two reactors compared to that in Reactor 1. The poor biofilm development was substantiated by low chemical oxygen demand (COD) removal in the latter two reactors.     

Membrane bioreactor with a porous hydrophobic membrane as a gas-liquid contactor for waste gas treatment

A novel type of bioreactor for waste gas treatment has been designed. The reactor contains a microporous hydrophobic membrane to create a large interface between the waste gas and the aqueous phase. To test the new reactor, propene was chosen because of its high air/water partition coefficient, which causes a low water concentration and hampers its removal from air. Propene transfer from air to a suspension of propene-utilizing Xanthobacter Py2 cells in the membrane bioreactor proved to be controlled by mass transfer in the liquid phase. The resistance of the membrane was negligible. Simulated propene transfer rates agreed well with the experimental data. A stable biofilm of Xanthobacter Py2 developed on the membrane during prolonged operation. The propene flux into the biofilm was 1 x 10(-6) mol m(-2) s(-1) at a propene concentration of 9.3 x 10(-2) mol m(-3) in the gas phase. (c) 1995 John Wiley & Sons, Inc.     

Bioaugmentation of a rotating biological contactor for degradation of 2-fluorophenol

The performance of a laboratory scale rotating biological contactor (RBC) towards shock loadings of 2-fluorophenol (2-FP) was investigated. During a period of ca. 2 months organic shock loadings of 25 mg L?1 of 2-FP were applied to the RBC. As no biodegradation of 2-FP was observed, bioaugmentation of the RBC with a 2-FP degrading strain was carried out and, along ca. 6 months, organic shock loadings within a range of 25-200 mg L?1 of 2-FP were applied. Complete biodegradation of 50 mg L?1 of 2-FP was observed during operation of the reactor. The RBC showed to be robust towards starvation periods, as after ca. 1month of non-supply of the target compound, the reactor resumed 2-FP degradation. The inoculated strain was retained within the biofilm in the disks, as the 2-FP degrading strain was recovered from the biofilm by the end of the experiment, thus bioaugmentation was successfully achieved.     

Development of a supported emulsion liquid membrane system for propionic acid separation in a microgravity environment

Perstractive fermentation is a good way to increase the productivity of bioreactors. UsingPropionibacteria as the model system, the feasibility of using supported emulsion liquid membrane (SELM) for perstractive fermentation is assessed in this study. Five industrial solvents were considered as the solvent for preparing the SELM. The more polar a solvent is, the higher the partition coefficient. However, toxicity of a solvent also increases with its polarity. CO-1055 (industrial decanol/octanol blend) has the highest partition coefficient toward propionic acid among the solvents that has no molecular toxicity towardPropionibacteria. A preliminary extraction study was conducted using tetradecane as solvent in a hydrophobic hollow fiber contactor. The result confirmed that SELM eliminates the equilibrium limitation of conventional liquid-liquid extraction, and allows the use of a non-toxic solvent with low partition coefficient.     

A new method for fish chromosome preparation

A new method for the preparation of fish chromosomes from abdominal cavity fluid has been developed. Cells were collected from fish abdominal cavity fluid after an in vivo PHA treatment, and cultured for a short time in medium with colchicine. After 30 min hypotonic treatment for marine fish and 35 min for freshwater fish, slides were prepared by the conventional air-drying method. The advantages ofthe method are: (1) it is technically simple; (2) it produces a reasonably high mitotic index; (3) chromosome spreading is good (4) there is very little cell breakage. Using this method, the chromosomes ofrainbow trout (2n=62); cod (2n=4546) and plaice (2n=46,47 and 48) were investigated.     

Preparation of stimulus responsive multiple emulsions by membrane emulsification using con a as biochemical sensor

In this work, a novel strategy for the controlled fabrication of biomolecular stimulus responsive water-in-oil-in-water (W/O/W) multiple emulsion using the membrane emulsification process was investigated. The emulsions interface was functionalized with a biomolecule able to function as a receptor for a target compound. The interaction between the biomolecular receptor and target stimulus activated the release of bioactive molecules contained within the structured emulsion. A glucose sensitive emulsion was investigated as a model study case. Concanavalin A (Con A) was used as the biomolecular glucose sensor. Various physicochemical strategies for stimulus responsive materials formulation are available in literature, but the preparation of biomolecule-responsive emulsions has been explored for the first time in this paper. The development of novel drug delivery systems requires advanced and highly precise techniques to obtain their particular properties and targeting requirements. The present study has proven the flexibility and suitability of membrane emulsification for the preparation of stable and functional multiple emulsions containing Con A as interfacial biomolecular receptor able to activate the release of a bioactive molecule as a consequence of interaction with the glucose target molecule. The influence of emulsion interfacial composition and membrane emulsification operating conditions on droplets stability and functional properties have been investigated. The release of the bioactive molecule as a function of glucose stimulus and its concentration has been demonstrated.     

一种适合于烟粉虱产卵的新型人工膜系统

介绍一种适合烟粉虱Bemisia tabaci(Gennadius)产卵的新型人工膜系统。该系统由一个透明的塑料盒,底直径30mm,顶口直径40mm,深35mm,其上覆盖1层或2层Parafilm M膜,与产卵的成虫相接触的1层厚度为5~8μm,2层膜中间或单层膜上加试验所需的试剂。将膜装置放于不透光的容器上,其上覆盖黄色玻璃纸,以吸引烟粉虱产卵。该装置可用于烟粉虱的人工产卵,观察卵的发育及研究相关的生理机制。     

Size‐dependent interaction of cells and hemoglobin–albumin based oxygen carriers prepared using the SPG membrane emulsification technique

Hemoglobin‐based oxygen carriers (HBOCs) of various sizes have been developed so far, but their optimum size has not been clarified yet. Here, we examined the effect of HBOCs size on their interaction with cells using Shirasu porous glass (SPG) membrane emulsification technique, which enables precise tuning of particle size. Microspheres composed of bovine hemoglobin (bHb) and bovine serum albumin (BSA) was fabricated with the average diameters of 1.2–18.3 μm and the coefficient of variation of below 13%. Cellular uptake of the microspheres by RAW264.7 was observed at a diameter below 5 μm; however, uptake of the microspheres by HepG2 and HUVEC were not observed at any diameter. No enhancement of the generation of reactive oxygen species in the cytoplasm was detected at diameters above 9.8 μm in the three cell lines, due to their low cellular uptake. In addition, cytotoxicity of the microspheres decreased with increasing microsphere diameter in the three cell lines and microspheres of 18.3 μm showed good cellular compatibility regardless of the oxyhemoglobin percentage. Since cytotoxicity is a crucial factor in their applications, our systemic investigation would provide a new insight into the design of HBOCs. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:1676–1684, 2015     

A new method for monitoring nitric oxide production using Teflon membrane microdialysis

The measurement of nitric oxide (NO) by electron spin resonance (ESR) is complicated by potentially toxic spin-trapping agents, which may affect the NO-producing cells per se and/or cause artifacts and systemic side effects. These problems can be addressed by preventing direct interaction between the agent and the biological system. In the present study, we utilized Teflon as a barrier between the spin trap and the living cell, since the material is permeable to gas only. Our aim was to investigate if NO could diffuse across the membrane in sufficient amounts to be trapped and quantified by ESR. We used standard microdialysis equipment and specially designed dialysis probes, or tubing, with Teflon membranes. Sodium nitroprusside was used as a NO donor and Fe-N-dithiocarboxysarcosine (Fe(DTCS)2) as a spin trap. NO readily diffuses through Teflon and could be quantified in concentrations considerably below 50 nM in a reproducible and accurate manner. In cell cultures of activated murine macrophages, NO synthesis from iNOS could be monitored and we noted a huge increase in NO concentration by superoxide dismutase. We conclude that spin trapping of NO by Fe(DTCS)2 across Teflon membranes is an attractive approach for quantifying and monitoring nitric oxide production without interfering with cell viability.     

A novel method for isolation of membrane proteins: a baculovirus surface display system

We have developed a novel baculovirus surface display (BVSD) system for the isolation of membrane proteins. We expressed a reporter gene that encoded hemagglutinin gene fused in frame with the signal peptide and transmembrane domain of the baculovirus gp64 protein, which is displayed on the surface of BmNPV virions. The expression of this fusion protein on the virion envelope allowed us to develop two methods for isolating membrane proteins. In the first method, we isolated proteins directly from the envelope of budding BmNPV virions. In the second method, we isolated proteins from cellular membranes that had disintegrated due to viral egress. We isolated 6756 proteins. Of these, 1883 have sequence similarities to membrane proteins and 1550 proteins are homologous to known membrane proteins. This study indicates that membrane proteins can be effectively isolated using our BVSD system. Using an analogous method, membrane proteins can be isolated from other eukaryotic organisms, including human beings, by employing a host cell-specific budding virus.     

High oxygen transfer rate in a new aeration system using hollow fiber membrane

A new type of bubble aeration column called a hollow fiber membrane (HFM) aeration column was proposed, which was featured in the use of hollow fiber membranes and gave a high bubble density in the column. The value of k(L)a was increased by modifying the membrane surface for making the pore size smaller. The Sauter mean diameter of bubbles (D(vs)) was 2.0 +/- 0.1 mm in the range of the superficial gas velocity from 0.02 m s(-1) to 0.065 m s(-1), while that obtained for the bubbles near the membrane was 811 mum at the superficial gas velocity of 4.0 x 10(-4) m s(-1). The difference was ascribed to the effect of coalescence of bubbles. The value of K(L)a increased in proportion to the superficial gas velocity up to 0.02 m s(-1), and was almost constant above 0.03 m s(-1). The maximum value of k(L)a, 2.5 s(-1), was higher than those of the other aeration columns reported previously. The pneumatic power consumption per unit liquid volume (P(v)) for obtaining the same k(L)a was the smallest in the HFM aeration columns. P(v), for obtaining the same interfacial area of bubbles per liquid volume, was also lower than those for other types of aeration columns. It was suggested from the measurement of bubble diameter that the larger interfacial area generated in the HFM aeration column ascribes to the larger gas holdup than the smaller D(vs). (c) 1992 John Wiley & Sons, Inc.     

A new method for enzyme membrane preparation based on polyurethane technology: Electrode modification for sensor development

The new method developed for enzyme membrane preparation is based on cross-linking poly (vinyl alcohol) (PVAL) with triisocyanate (TIC) in the presence of enzyme. Dimethylsulfoxide (DMSO) was the only solvent found to dissolve PVAL, TIC and enzyme at room temperature, without completely denaturing the latter. The rate of gelation to form the desired network membrane can be controlled by the amount of solvent used. All the enzymes tested (alkaline phosphatase and alcohol, cholesterol and glucose oxidases) dissolved in DMSO and retained sufficient activity for use in electrochemical sensors. Membranes were formed on both graphite and platinized graphite electrodes. The resulting prototype sensors were examined with regard to feasibility of preparation, adhesion of the gels to the electrode surfaces, swelling properties of the gels in DMSO and aqueous buffers, and their electrochemical properties.