Separation of BSA through FAU-type zeolite ceramic composite membrane formed on tubular ceramic support: Optimization of process parameters by hybrid response surface methodology and biobjective genetic algorithm

In this study, Faujasite (FAU) zeolite was coated on low-cost tubular ceramic support as a separating layer through hydrothermal route. The mixture of silicate and aluminate solutions was used to create a zeolitic separation layer on the support. The prepared zeolite ceramic composite membrane was characterized using X-ray powder diffraction (XRD), Fourier transform infrared spectroscopy (FTIR), particle size distribution (PSD), field emission scanning electron microscopy (FESEM), and zeta potential measurements. The porosity of ceramic support (53%) was reduced by the deposition of FAU (43%) zeolite layer. The pore size and water permeability of the membrane were evaluated as 0.179?µm and 1.62?×?10^?7?m³/m²?s?kPa, respectively, which are lower than that of the support (pore size of 0.309?µm and water permeability of 5.93?×?10^?7?m³/m²?s?kPa). The permeate flux and rejection potential of the prepared membrane were evaluated by microfiltration of bovine serum albumin (BSA). To study the influences of three independent variables such as operating pressure (68.94–275.79?kPa), concentration of BSA (100–500?ppm), and solution pH (2–4) on permeate flux and percentage of rejection, the response surface methodology (RSM) was used. The predicted models for permeate flux and rejection were further subjected to biobjective genetic algorithm (GA). The hybrid RSM-GA approach resulted in a maximum permeate flux of 2.66?×?10^?5?m³/m²?s and BSA rejection of 88.02%, at which the optimum conditions were attained as 100?ppm BSA concentration, 2 pH solution, and 275.79?kPa applied pressure. In addition, the separation efficiency was compared with other membranes applied for BSA separation to know the potential of the fabricated FAU zeolite ceramic composite membrane.     

A mechanistic study of in situ chemical cleaning-in-place for a PTFE flat sheet membrane: fouling mitigation and membrane characterization

This study aimed at unfolding the role and mechanisms of chemically enhanced cleaning-in-place (CIP) regimes in fouling control of polytetrafluoroethylene (PTFE) made flat sheet (FS) membrane bio-reactors (MBRs). The trans-membrane pressure (TMP) was successfully maintained below 10 kPa using a daily CIP regime consisting of 100 to 600 mg l^?1 of NaOCl and cake layer resistance control was shown to be critical for effective high-flux MBR operation. In contrast, in the control unit without the CIP, the TMP exceeded 35 kPa at a flux of 40 LMH. The extracellular polymeric substances associated with proteins (EPS_protein) were also controlled effectively with a daily application of the CIP to the fouled membrane. Moreover, the CIP prompted a thinner and looser bio-cake layer on the membrane surface, suggesting that in situ CIP can be a favorable method to control FS membrane fouling at high-flux MBR operation.     

New insights into membrane fouling in a submerged anaerobic membrane bioreactor based on characterization of cake sludge and bulk sludge

A laboratory-scale submerged anaerobic membrane bioreactor (SAnMBR) treating thermomechanical pulping whitewater was operated for over 7 months to investigate and compare the characteristics of cake sludge and bulk sludge during stable state operation period. Serial analysis showed that cake sludge had a smaller particle size distribution (PSD), much higher specific filtration resistance (1.34 × 10¹⁴ m/kg), 1.5 times higher bound EPS and significantly different microbial community as compared with bulk sludge. Further analysis indicated that small flocs, bound EPS and inorganic materials play important role in cake formation process. The formed cake layer was found to have a heterogeneous structure. The results obtained in this study indicated that cake formation process started from attachment of small flocs and/or specific bacterial clusters which colonize the surface of the membrane and provide enhanced conditions that allow for cake formation to progress.     

Comparison between a moving bed membrane bioreactor and a conventional membrane bioreactor on membrane fouling

A membrane bioreactor filled with carriers instead of activated sludge named a moving bed membrane bioreactor (MBMBR) was investigated to minimize the effect of suspended solids on membrane fouling. The MBMBR and a conventional membrane bioreactor (CMBR) were operated in parallel for about two months. Unexpectedly, the rate of membrane fouling in MBMBR was about three times of that in CMBR. MBMBR showed a higher cake layer resistance than CMBR due to plenty of filamentous bacteria inhabited in suspended solids in MBMBR. Protein and polysaccharide contents of soluble EPS in MBMBR were obviously larger than those in CMBR. It could be speculated that the overgrowth of filamentous bacteria in MBMBR resulted in severe cake layer and induced a large quantity of EPS, which deteriorated the membrane fouling.     

Characterizing membrane foulants in MBR with addition of polyferric chloride to enhance phosphorus removal

The effect of polymeric ferric chloride (PFC) addition on phosphorus removal and membrane fouling were investigated in an anoxic/oxic submerged membrane bioreactor. The total phosphorus concentration in effluent averaged at 0.26 mg/L with PFC addition of 10-15 mg/L, while the rate of membrane fouling increased 1.6 times over the control MBR (without PFC addition). Three-dimensional excitation-emission matrix fluorescence spectroscopy and Gel Filtration Chromatography analysis indicated that soluble microbial byproduct-like materials and large molecules (M(W)>100 kDa) were one of the main contributors of biofouling. Fourier transform infrared spectrum confirmed that the major components of the cake layer were proteins and polysaccharides materials. Scanning electron microscopy demonstrated that membrane surfaces were covered with compact gel layer formed by organic substances and Energy Dispersive X-ray analysis indicated that ferric metals were the most important inorganic pollutants. Consequently, soluble organic substances and dose of PFC should be controlled to minimize membrane fouling.     

Study on the toxic effect of lead(II) ion on <Emphasis Type="Italic">Escherichia coli</Emphasis>

The toxic effects of lead(II) have been studied in Escherichia coli cells. Using microcalorimetric analysis, it was shown that E. coli growth was inhibited in the presence of Pb²⁺ resulting from damage to the cell membrane and that Pb²⁺ takes part in the metabolism of cells. Treatment with lysozyme confirms damage to the cell’s outer membrane. Similarities between the ionic radii and charge/radius ratio cause Pb(II) to replace Ca(II) at the binding sites of lipopolysacharides, leading to rupture of protecting areas on the cell’s surface. Consequently, the protection and functionality of outer membrane is lost, thus becoming the basis for the biological effect of Pb²⁺ on E. coli.     

Membrane fouling in a membrane bioreactor (MBR): sludge cake formation and fouling characteristics

A submerged membrane bioreactor (MBR) with a working volume of 1.4 L and a hollow fiber microfiltration membrane was used to treat a contaminated raw water supply at a short hydraulic retention time (HRT) of approximately 1 h. Filtration flux tests were conducted regularly on the membrane to determine various fouling resistances, and confocal laser scanning microscopy (CLSM) and scanning electron microscopy (SEM) were employed to characterize the biofouling development and sludge cake formation on the membrane. The experimental results demonstrate that the MBR is highly effective in drinking water treatment for the removal of organic pollutants, ammonia, and UV absorbance. During the MBR operation, the fouling materials were not uniformly distributed on the entire surface of all of the membrane fibers. The membrane was covered partially by a static sludge cake that could not be removed by the shear force of aeration, and partially by a thin sludge film that was frequently washed away by aeration turbulence. The filtration resistance coefficients were 308.4 x 10(11) m(-1) on average for the sludge cake, 32.5 x 10(11) m(-1) on average for the dynamic sludge film, and increased from 10.5 x 10(11) to 59.7 x 10(11) m(-1) for the membrane pore fouling after 10 weeks of MBR operation at a filtration flux of 0.5 m3/m2 x d. Polysaccharides and other biopolymers were found to accumulate on the membrane, and hence decreased membrane permeability. More important, the adsorption of biopolymers on the membrane modified its surface property and led to easier biomass attachment and tighter sludge cake deposition, which resulted in a progressive sludge cake growth and serious membrane fouling. The sludge cake coverage on the membrane can be minimized by the separation, with adequate space, of the membrane filters, to which sufficient aeration turbulence can then be applied.     

Microfiltration of yeast suspensions with self-cleaning spiral vortices: possibilities for a new membrane module design

A novel method of producing controlled vortices was used to reduce both concentration polarization and membrane fouling during microfiltration of Saccharomyces cerevisiae broth suspensions. The method involves flow around a curved channel at a sufficient rate so as to produce centrifugal instabilities (called Dean vortices). These vortices depolarize the build-up of suspended particles such as yeast cells at the membrane-solution interface and allow for increased membrane permeation rates. Various operating conditions under which such vortices effectively reduced cake build-up of suspended particles such as yeast cells at the membrane-solution interface and allow for increased membrane permeation rates. Various operating conditions under which such vortices effectively reduced cake build-up during microfiltration of 0 to 0.55 dry wt% yeast broth were investigated. Flux improvements of over 60% for 0.25 dry wt% yeast broth for flow with over that without Dean vortices were observed. This beneficial effect increased with increasing retentate flow rate and increasing transmembrane pressure and decreased with increasing concentration of suspended matter. Similar behavior was observed whether the cells were viable of killed. the improvement in flux in the presence over that in the absence of vortices correlated well with centrifugal force or azimuthal velocity squared. The relative cake resistances increased with reservoir yeast concentration. These values with vortices increased from 62% to 75% of that without vortices with increasing yeast concentration. The ratio of the cake thicknesses in the limiting case (at high feed concentration) was 3.25. These results suggest that self-cleaning spiral vortices could be effective in maintaining good and steady microfiltration performance with cell suspensions other than those tested. (c) 1995 John Wiley & Sons, Inc.     

Mitochondrial and cytosolic calcium in rat hearts under high-K(+) cardioplegia and pyruvate: mechano-energetic performance

High-K(+)-cardioplegia (CPG) and pyruvate (Pyr) are used as cardioprotective agents. Considering that mitochondria play a critical role in cardiac dysfunction, we investigated the effect of CPG on mitochondrial Ca(2+) uptake and sarcorreticular (SR) calcium handling. Cytosolic and mitochondrial Ca(2+), as well as mitochondrial membrane potential (ΔΨm) were assessed in rat cardiomyocytes by confocal microscopy. Mechano-calorimetrical correlation was studied in perfused hearts. CPG did not modify JC-1 (ΔΨm), but transiently increased, by up to 1.8 times, the Fura-2 (intracellular Ca concentration, [Ca(2+)]i) and Rhod-2 (mitochondrial free Ca concentration [Ca(2+)]m) fluorescence of resting cells, with exponential decays. The addition of 5?μmol·L(-1) thapsigargin (Tpg) increased the Rhod-2 fluorescence in a group of cells without any effect on the Fura-2 signal. In rat hearts perfused with CPG, 1?μmol·L(-1) Tpg decreased resting heat rate (ΔH(r):?-0.44?± 0.07?mW·g(-1)), while the addition of 5?μmol·L(-1) KB-R7943 increased resting pressure (ΔrLVP by?+5.26?± 1.10?mm Hg; 1?mm Hg?= 133.322 Pa). The addition of 10?mmol·L(-1) Pyr to CPG increased H(r) (+3.30?± 0.24?mW·g(-1)) and ΔrLVP (+2.2?± 0.4?mm Hg), which are effects potentiated by KB-R7943. The results suggest that under CPG, (i) there was an increase in [Ca(2+)]i and [Ca(2+)]m (without changing ΔΨm) that decayed by exothermic removal mechanisms; (ii) mitochondrial Ca(2+) uptake contributed to the removal of cytosolic Ca(2+), in a process that was potentiated by inhibition of sarco-endoplasmic reticulum Ca(2+)-ATPase (SERCA), and reduced by KB-R7943; (iii) under these conditions, SERCA represents the main energetic consumer; (iv) Pyr increased the energetic performance of hearts,mainly by inducing mitochondrial metabolism.     

Characterization of a liposome-based artificial skin membrane for in vitro permeation studies using Franz diffusion cell device

A prerequisite for successful transdermal or dermal drug therapy is the drug ability to penetration through the skin, especially stratum corneum (SC). The most acceptable technique for measuring skin permeation in vitro is the application of both the Franz diffusion cell device and the skin model. In the skin model, a liposome-based artificial skin membrane (LASM) consisting of tight layers of liposomes immobilized on a filter was prepared and characterized. Using porcine ear skin, rat skin and Strat-M? artificial membrane as control, the LASM was then evaluated in permeation studies with five active compounds: ferulic acid, paeoniflorin, albiflorin, tetrahydrocolumbamine, and tetrahydropalmatine. The scanning electron microscope images demonstrated complete filling of the membrane pores with lipids and the formation of a continuous liposomal coating. The contents of egg phosphatidylcholine (EPC) and cholesterol in LASM were measured to be 12.08?±?0.18 and 4.41?±?0.04?mg/cm², respectively. Moreover, revealed by the measurement of electrical resistance, the LASM remains intact for at least 12?h with the incubation of 20% ethanol. The results of permeation studies demonstrated a good correlation (r^2?=?0.9743, r?=?0.9871) of P_app values between the drugs’ permeation through LASM and porcine ear skin. In addition, by ATR-FTIR analysis, a slighter shift of CH₂ stretching frequency between LASM and porcine ear skin was observed compared with the shift between Strat-M? membrane and porcine ear skin. In summary, for the first time, the LASM has been proved to be a valuable alternative to porcine ear skin in permeation studies using Franz diffusion cell device.     

Impact of sludge retention time on MBR fouling: role of extracellular polymeric substances determined through membrane autopsy

The impact of sludge retention time (SRT) on the biofouling of a membrane bioreactor (MBR) by extracellular polymeric substances (EPS) was investigated. The MBR was operated at 60 and 20 d SRT. The gel layer (recovered through optimized membrane autopsy methods) and the cake layer were analyzed for their content and profile of EPS proteins and polysaccharides. The change to a shorter SRT led to decreased membrane filterability, concomitant with a higher expression of EPS proteins in the cake layer, which were identified as being mainly related with biosynthesis and stress functions. The gel layer was more substantial in internal fibers, with polysaccharides being the major component in this layer. With the decrease in SRT (and filterability decrease), the overall polysaccharide content and sugar variety increased. In conclusion, SRT impacted not only on the quantity but also the composition of EPS molecules, and both were shown to be important in biofouling.     

Three Ca2+-binding proteins from porcine liver and intestine differ immunologically and physicochemically and are distinct in Ca2+ affinities

Intestinal brush-border-derived membrane vesicles contain, after demembranation in the presence of Ca2+, a subset of polypeptides that are specifically solubilized by the addition of Ca2+ chelators. As described previously, this fractionation scheme leads to the enrichment of two major proteins (I and II), one of which has been shown to be identical to the cellular p36K target of Rous sarcoma virus-encoded tyrosine-specific protein kinase (Gerke, V., and Weber, K., (1984) EMBO J. 3, 227-233). We have applied a similar protocol to membrane vesicles from porcine liver and purified a third Ca2+-binding protein (III). All three proteins had wide tissue distributions, and were absent from brain, red blood cells, and cardiac and skeletal muscle. Relative amounts varied between tissues, with protein I low in liver and protein III very low in intestine. Despite their similar extractability the three proteins (I, II, and III) are clearly distinct as far as immunological, biochemical, and physicochemical properties are concerned. They also show characteristic differences in their affinities for Ca2+ ions. The association constants of Ca2+ binding for proteins I and III have been estimated by means of indirect methods to be 10(4) M-1 (protein I) and 10(6) M-1 (protein III), while the direct Hummel-Dreyer method reveals Ca2+ binding to protein II, characterized by an association constant of 0.4 X 10(5) M-1 in the absence and 0.2 X 10(5) M-1 in the presence of 2 mM MgCl2. Conformational changes upon binding Ca2+ are described for protein II using circular dichroism, fluorescence emission, and UV difference spectra. These alterations could be attributed to an increased exposure of tyrosine and tryptophan residues to a more aqueous environment, and led to increased hydrophobicity of protein II that would explain the observed Ca2+-dependent interaction with hydrophobic matrices like phenyl-Sepharose.     

Surface potential on the periplasmic side of the photosynthetic membrane of Rhodopseudomonas sphaeroides

Membrane surface potential on the periplasmic side of the photosynthetic membrane was estimated in cells, spheroplasts and chromatophores of Rhodopseudomonas sphaeroides. When the membrane potential (potential difference between bulk aqueous phases) was kept constant in the presence of carbonylcyanide m-chlorophenylhydrazone, addition of salt to a suspension of cells or spheroplasts induced a red shift in the carotenoid absorption spectrum which indicated a change in the intramembrane electrical field. The spectral shift is explained by a rise in electrical potential at the outside surface of the photosynthetic membrane due to a decrease in extent of the negative surface potential.The spectral shift occurred in the direction opposite to that in chromatophores, indicating that the sidedness of the membrane of cells or spheroplasts is opposite to that of chromatophores. The dependences of the extent of the potential change on concentration and valence of cations of salts agreed with the Gouy-Chapman relationship on the electrical diffuse double layer. The charge density on the periplasmic surface of the photosynthetic membrane was estimated to be ?2.9 · 10^?3 elementary charge per Ų, while that on the cytoplasmic side surface was calculated as ?1.9 · 10^?3 elementary charge per Ų (Matsuura, K., Masamoto, K., Itoh, S. and Nishimura, M. (1979) Biochim. Biophys. Acta 547, 91–102). Surface potential on the periplasmic side of the photosynthetic membrane was estimated to be about ?50 mV at pH 7.8 in the presence of 0.1 M monovalent salt.     

Ca2+ responses to thyrotropin-releasing hormone and angiotensin II: the role of plasma membrane integrity and effect of G11alpha protein overexpression on homologous and heterologous desensitization

The molecular mechanisms involved in GPCR-initiated signaling cascades where the two receptors share the same signaling cascade, such as thyrotropin-releasing hormone (TRH) and angiotensin II (ANG II), are still far from being understood. Here, we analyzed hormone-induced Ca(2+) responses and the process of desensitization in HEK-293 cells, which express endogenous ANG II receptors. These cells were transfected to express exogenously high levels of TRH receptors (clone E2) or both TRH receptors and G(11)alpha protein (clone E2M11). We observed that the characteristics of the Ca(2+) response, as well as the process of desensitization, were both strongly dependent on receptor number and G(11)alpha protein level. Whereas treatment of E2 cells with TRH or ANG II led to significant desensitization of the Ca(2+) response to subsequent addition of either hormone, the response was not desensitized in E2M11 cells expressing high levels of G(11)alpha. In addition, stimulation of both cell lines with THR elicited a clear heterologous desensitization to subsequent stimulation with ANG II. On the other hand, ANG II did not affect a subsequent response to TRH. ANG II-mediated signal transduction was strongly dependent on plasma membrane integrity modified by cholesterol depletion, but signaling through TRH receptors was altered only slightly under these conditions. It may be concluded that the level of expression of G-protein-coupled receptors and their cognate G-proteins strongly influences not only the magnitude of the Ca(2+) response but also the process of desensitization and resistance to subsequent hormone addition.     

Mechanistic modeling of the loss of protein sieving due to internal and external fouling of microfilters

Fed‐batch and perfusion cell culture processes used to produce therapeutic proteins can use microfilters for product harvest. In this study, new explicit mathematical models of sieving loss due to internal membrane fouling, external membrane fouling, or a combination of the two were generated. The models accounted for membrane and cake structures and hindered solute transport. Internal membrane fouling was assumed to occur due to the accumulation of foulant on either membrane pore walls (pore‐retention model) or membrane fibers (fiber‐retention model). External cake fouling was assumed to occur either by the growth of a single incompressible cake layer (cake‐growth) or by the accumulation of a number of independent cake layers (cake‐series). The pore‐retention model was combined with either the cake‐series or cake‐growth models to obtain models that describe internal and external fouling occurring either simultaneously or sequentially. The models were tested using well‐documented sieving decline data available in the literature. The sequential pore‐retention followed by cake‐growth model provided a good fit of sieving decline data during beer microfiltration. The cake‐series and cake‐growth models provided good fits of sieving decline data during the microfiltration of a perfusion cell culture. The new models provide insights into the mechanisms of fouling that result in the loss of product sieving. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 33:1323–1333, 2017     

Calcium Status of Yellow Lupin Symbiosomes as a Potential Regulator of Their Nitrogenase Activity: The Role of the Peribacteroid Membrane

The capacity of symbiosomes from yellow lupin root nodules for active Ca²⁺uptake and the sensitivity of their nitrogenase activity to a disturbance of the symbiotic Ca partition were investigated. The experiments carried out on the isolated symbiosomes and the peribacteroid membrane (PBM) vesicles, using Ca²⁺indicators arsenazo III and chlorotetracycline, and the cytochemical Ca visualization with potassium pyroantimonate (PA) provided evidence that an Mg-ATP-energized pump, most likely Mg²⁺-dependent Ca²⁺-ATPase catalyzing the active transport of Ca²⁺from the cytosol of the plant cell into the symbiosomes across the PBM, functions on this membrane. Depleting the symbiosomes of Ca both in vivoandin vitroby treating the intact nodules of yellow lupin root or the purified symbiosomes isolated from the latter with EGTA and Ca²⁺-ionophore A23187 substantially decreased their nitrogenase activity. The inhibitory effect of calcium deficit in the symbiosomes was not reversed by the addition of calcium to the incubation medium containing the plant tissues under study and was even enhanced under these conditions. The nitrogenase activity of the isolated symbiosomes not experiencing calcium deficit was also inhibited by the addition of relatively high concentrations of exogenous calcium to the incubation medium. These results seem to give evidence that the calcium status of nodule symbiosomes from yellow lupin roots controls their nitrogenase activity. The data obtained suggest that both Ca²⁺transport on PBM and the low passive permeability of this membrane for the given cation play the key role in such a control.     

Humic substances and the water calcium content change the toxicity of malachite green

Laboratory experiments were conducted to test interactive effects of calcium (Ca²⁺) content and the presence of humic substance (HS) on malachite green (MAG)‐induced toxicity in fish embryos and larvae by means of a semistatic 144‐h‐embryo‐larval‐test with zebrafish (Danio rerio). Two kinds of reconstituted water samples were used to produce the test media by mixing salts into deionized water resulting in either hard water (↑Ca ? HS), or soft water (↓Ca ? HS). By adding HS two additional test media were produced (↑Ca + HS, ↓Ca + HS). MAG was tested in concentrations of 0.05, 0.10, 0.15, 0.20, 0.25 mg L^?1. The toxicity ranking of MAG (mg L^?1) to embryos based on 96‐h‐LC₅₀ in the different test water samples is: ↑Ca ? HS (0.061) > ↑Ca + HS (0.123) = ↓Ca ? HS (0.12) ≥ ↓Ca + HS (0.134) and on 144‐h‐LC₅₀ to larvae is: ↑Ca ? HS (0.038) > ↑Ca + HS (0.06) > ↓Ca ? HS (0.077) = ↓Ca + HS (0.077). Mortality of all the groups was significantly different (P < 0.05). Increased Ca²⁺ concentrations did not protect zebrafish embryos and larvae from MAG‐induced toxicity. At high Ca²⁺ conditions, the mortality of the embryos as well as of the larvae is reduced in the ↑Ca + HS group relative to the ↑Ca ? HS group. Thus, at high Ca²⁺ conditions the HS does affect the MAG‐induced mortality. The mechanism which causes the higher toxicity of MAG in the presence of higher Ca²⁺ concentrations is poorly understood. A probable explanation could be the stimulation of the calcium‐binding protein calmodulin as well as the calmodulin kinase II in cell membranes in the presence of high Ca²⁺ concentrations.     

Improving the performance of an aerobic membrane bioreactor (MBR) treating pharmaceutical wastewater with powdered activated carbon (PAC) addition

In this study, the effects of organic loading rate (OLR) and the addition of powdered activated carbon (PAC) on the performance and membrane fouling of MBR were conducted to treat real pharmaceutical process wastewater. Over 145 days of operation, the MBR system was operated at OLRs ranging from 1 to 2 kg COD m^?3 day^?1 without sludge wasting. The addition of PAC provided an improvement in the flux, despite an increase in the OLR:PAC ratio. The results demonstrated that the hybrid PAC-MBR system maintained a reduced amount of membrane fouling and steadily increased the removal performance of etodolac. PAC addition reduced the deposition of extracellular polymeric substance and organic matter on the membrane surface and resulted an increase in COD removal even at higher OLRs with low PAC addition. Membrane fouling mechanisms were investigated using combined adsorption fouling models. Modified fouling index values and normalized mass transfer coefficient values indicated that predominant fouling mechanism was cake adsorption.     

Aspects of signal transduction in stimulus exocytosis-coupling in Paramecium

This paper deals with the detailed mechanisms of signal transduction that lead to exocytosis during regulative secretion induced by specific secretagogues in a eukaryotic cell, Paramecium tetraurelia. There are at least three cellular compartments involved in the process: I) the plasma membrane, which contains secretagogue receptors and other transmembrane proteins, II) the cytoplasms, particularly in the region between the cell and secretory vesicle membranes, where molecules may influence interactions of the membranes, and III) the secretory vesicle itself. The ciliated protozoan Paramecium tetraurelia is very well suited for the study of signal transduction events associated with exocytosis because this eukaryotic cell contains thousands of docked secretory vesicles (trichocysts) below the cell membrane which can be induced to release synchronously when triggered with secretagogue. This ensures a high signal-to-noise ratio for events associated with this process. Upon release the trichocyst membrane fuses with the cell membrane and the trichocyst content undergoes a Ca2+-dependent irreversible expansion. Secretory mutants are available which are blocked at different points in the signal transduction pathway. Aspects of the three components mentioned above that will be discussed here include a) the properties of the vesicle content, its pH, and its membrane; b) the role of phosphorylation/dephosphorylation of a cytosolic 63-kilodalton (kDa)Mr protein in membrane fusion; and c) how influx of extracellular Ca2+ required for exocytosis may take place via exocytic Ca2+ channels which may be associated with specific membrane microdomains (fusion rosettes).     

Maintenance of the differentiated type II cell characteristics by culture on an acellular human amnion membrane

We have developed a Culture system for guinea pig alveolar type II cells using an epithelium-denuded human amnion membrane as a substratum. The differentiated morphology was maintained for 3 wk by both air-interface feeding and immersion feeding when type II cells were cultured on the basement membrane side of the amnion with fibroblasts on the opposite side (coculture). Functionally high levels of surfactant protein B (SP-B) and C (SP-C) messenger ribonucleic acids (mRNAs) were expressed even after the 3-wk cultivation and surfactant protein A mRNA was detected on day 10 of the culture. The differentiation was also maintained when fibroblasts were cultured on lower chambers of the culture plates (separate culture). In contrast, culture of type II cells without fibroblasts (monoculture) could not preserve the mature morphology. When the monoculture was supplemented with keratinocyte growth factor or hepatocyte growth factor, a monolayer of rather cuboidal type II cells with apical microvilli was maintained. However, the percent area of lamellar bodies in these cells was significantly less than that in freshly isolated type II cells, and mRNA expressions of SP-B and SP-C were also considerably suppressed. These findings suggest that other growth factors or combinations of these factors are necessary for the maintenance of the differentiated phenotype. As substratum, a permeable collagen membrane or a thin gel layer of Engelbreth-Holm-Swarm mouse sarcoma extracts did not preserve the mature characteristics. This culture system using an acellular human amnion membrane may provide novel models for research in type II cells.