Effect of temperature on plant elongation and cell wall extensibility

Lockhart equation was derived for explaining plant cell expansion where both cell wall extension and water uptake must occur concomitantly. Its fundamental contribution was to express turgor pressure explicitly in terms of osmosis and wall mechanics. Here we present a new equation in which pressure is determined by temperature. It also accounts for the role of osmosis and consequently the role of water uptake in growing cell. By adopting literature data, we also attempt to report theoretically the close relation between plant elongation and cell wall extensibility. This is accomplished by the modified equation of growth solved for various temperatures in case of two different species. The results enable to interpret empirical data in terms of our model and fully confirm its applicability to the investigation of the problem of plant cell extensibility in function of environmental temperature. Moreover, by separating elastic effects from growth process we specified the characteristic temperature common for both processes which corresponds to the resonance energy of biochemical reactions as well as to the rapid softening of the elastic modes toward the high temperature end where we encountered viscoelastic and/or plastic behavior as dominating. By introducing analytical formulae connected with growth and elastic properties of the cell wall, we conclude with the statement how these both processes contribute quantitatively to the resonance-like shape of the elongation curve. In addition, the tension versus temperature "phase diagram" for a living plant cell is presented.     

The Gibbs-Duhem equation in membrane transport

It is argued that the Gibbs-Duhem equation alone cannot be used for deriving conclusions about the pressure gradient in membrane permeation. Statements regarding spatial variation of pressure in conjunction with chemical potential gradients of the components can legitimately be drawn from an equation that results from a combination of the G-D equation and the mechanical equilibrium equation. The derived equation has been applied here for explaining the mechanics of osmosis. In a further application, the frictional model has been improved here because the driving force also includes the membrane-solute potential interaction, thus allowing the solute partition coefficient to appear in the calculations naturally. By recognizing that because of the membrane-solution interaction, external forces of both potential and frictional character are present, the dissipation function is shown to depend explicitly on the centre-of-mass velocity. Thus the reference velocity for diffusive fluxes cannot be chosen arbitrarily, making Prigogine's theorem invalid in this approach to describing membrane permeation.     

True Anomalous Osmosis in Multi-Solute Model Membrane Systems

The transport of liquid across charged porous membranes separating two electrolytic solutions of different composition consists of both a normal and an anomalous osmotic component. Anomalous osmosis does not occur with electroneutral membranes. Thus, with membranes which can be charged and discharged reversibly, normal osmosis can be measured with the membrane in the electroneutral state, and normal together with anomalous osmosis with the membrane in a charged state, the difference between these two effects being the true anomalous osmosis. Data are presented on the osmotic effects across an oxyhemoglobin membrane in the uncharged state at pH 6.75 and in two charged states, positive at pH 4.0 and negative at pH 10.0, in multi-solute systems with 0.2 and 0.4 osmolar solutions of a variety of electrolytes and of glucose against solutions of other solutes of the same, one-half, and twice these osmolarities. In the simpler systems the magnitude of the true anomalous osmosis can be predicted semiquantitatively by reference to appropriate single-solute systems. In isoosmolar systems with two electrolytic solutions the anomalous osmotic flow rates may reach 300 µl./cm.² hr. and more; systems with electrolytic solutions against solutions of glucose can produce twice this rate. These fluxes are of the same order of magnitude as the liquid transport rates across such living structures as the mucosa of dog gall bladder, ileum, and urinary bladder.     

The general fluid circuit theory of active chloride absorption

The original fluid circuit theory used to explain active intestinal absorption of chloride is modified to include diffusion and secretion of chloride and osmosis. The general differential equation developed is integrated in a particular case. The definition, “effective concentration of chloride in the fluid passing into the intestinal lumen,” leads to simplified general expressions.     

通气状况、某些呼吸中间产物和抑制剂对甘蔗幼叶原生质体酶解释离的影响

甘蔗幼叶原生质体酶解释离期间呼吸速率逐渐降低。通气良好者原生质体产量高,但各处理原生质体存活率差异不大。以无机盐为稳压剂者,苹果酸、α-酮戊二酸、丙酮酸钠、琥珀酸钠、柠檬酸钠等呼吸中间产物均能提高原生质体产量,尤以琥珀酸钠和丙酮酸钠效果最好。而以糖醇为稳压剂者,苹果酸、α-酮戊二酸、丙酮酸钠和琥珀酸钠等有促进作用,柠檬酸钠却有严重抑制效应,产物几全部为具壁细胞。 呼吸抑制剂如碘乙酸、氟化钠、丙二酸、叠氮化钠和2,4-二硝基酚等对原生质体产量和存活率均有抑制作用。随抑制剂浓度增加,呼吸受抑制越甚,原生质体产量和存活率的降低也越甚。琥珀酸能消除丙二酸对呼吸的抑制,并减轻丙二酸对原生质体释离的不利影响。 用酶法从具壁细胞中分离原生质体是既受细胞的代谢水平所调控,又受组成酶液的稳压剂的组分所影响。其原因需进一步研究。     

Intracellular Mobilization of Ca2+ and Inhibition of Cytoplasmic Streaming Induced by Transcellular Osmosis in Internodal Cells of Nitella flexilis

When transcellular osmosis was induced in internodal cells ofNitella flexilis that had been rendered inexcitable by treatmentwith KCl or EGTA, the rate of cytoplasmic streaming was reducedand the membrane was depolarized. In both KCl- and EGTA-treatedcells, the endoosmosis induced a significant increase in theconcentration of Ca²⁺ in the cytoplasm, which was demonstratedby monitoring the emission of light from aequorin that had beeninjected into the cytoplasm. When transcellular osmosis was induced in tonoplast-free cells,in which the intracellular Ca²⁺ concentration had been stabilizedat a very low level by treatment with the Ca²⁺-chelating agentEGTA, no change in the rate of cytoplasmic streaming on theendoosmosis side was observed. Hydration of the cytoplasm in the absence of endoosmosis wasinduced by direct introduction of a hypotonic medium into thevacuole by intracellular perfusion. The results mimicked theinhibition of streaming induced by transcellular osmosis. During transcellular osmosis, chloroplasts on the endoosmosisside swelled as a result of dilution of the cell sap. Swellingof chloroplasts was demonstrated to be unrelated to the inhibitionof streaming, since streaming was retarded at sites from whichchloroplasts had been removed. It is suggested that hydration of the cytoplasm triggers themobilization of Ca²⁺ from internal stores and causes an increasein the level of cytoplasmic Ca²⁺ that is responsible for theinhibition of streaming. Possible mechanisms for the osmosis-inducedincreases in the level of Ca²⁺ in the cytoplasm are discussed. (Received January 11, 1993; Accepted November 8, 1993)     

The contributions of normal and anomalous osmosis to the osmotic effects arising across charged membranes with solutions of electrolytes

The osmotic effect arising across a porous membrane separating the solution of an electrolyte from water (or a more dilute solution) is ordinarily due to both normal osmosis, as it occurs also with non-electrolytes, and to "anomalous" osmosis. It is shown that the normal osmotic component cannot be measured quantitatively by the conventional comparison with a non-electrolytic reference solute. Anomalous osmosis does not occur with electroneutral membranes. Accordingly, with membranes which can be charged and discharged reversibly (without changes in geometrical structure), such as many proteinized membranes, the osmotic effects caused by an electrolyte can be measured both when only normal osmosis arises (with the membrane in the electroneutral state) and when normal as well as anomalous osmosis occurs (with the membrane in a charged state). The difference between these two effects is the true anomalous osmosis. Data are presented on the osmotic effects across an oxyhemoglobin membrane in the uncharged state at pH 6.75 and in two charged states, positive at pH 4.0 and negative at pH 10.0, with solutions of a variety of electrolytes using a concentration ratio of 2:1 over a wide range of concentrations. The rates of the movement of liquid across the membrane against an inconsequentially small hydrostatic head are recorded instead of, as conventional, the physiologically less significant pressure rises after a standard time.     

Concentration of ultrafiltered benzylpenicillin broths by reverse osmosis

Concentration of benzylpenicillin filtered broths purified by ultrafiltration and fermented broths clarified by ultrafiltration was carried out by reverse osmosis. This study was done using a reverse osmosis laboratory/pilot installation from Paterson Candy International Ltd. whose module has a tubular configuration and a membrane with a molecular weight cut-off of 100 Dalton (ZF99) made of a polyamide film with a rejection of 99% of NaCl. It was concluded that reverse osmosis is an adequate technique to concentrate benzylpenicillin ultrafiltered broths, leading to low losses of benzylpenicillin in the permeate and high benzylpenicillin recovery for high volumetric concentration factors.     

Aquaporins: Another piece in the osmotic puzzle

Osmolarity not only plays a key role in cellular homeostasis but also challenges cell survival. The molecular understanding of osmosis has not yet been completely achieved, and the discovery of aquaporins as molecular entities involved in water transport has caused osmosis to again become a focus of research. The main questions that need to be answered are the mechanism underlying the osmotic permeability coefficients and the extent to which aquaporins change our understanding of osmosis. Here, attempts to answer these questions are discussed. Critical aspects of the state of the state of knowledge on osmosis, a topic that has been studied since 19th century, are reviewed and integrated with the available information provided by in vivo, in vitro and in silico approaches.     

Anomalous osmosis through a model membrane constructed with potassium polystyrenesulfonate solution

It is reported that anomalous osmosis can be observed through liquid membranes which are made by placing a potassium polystyrenesulfonate solution between two inert cellophane membranes. No anomalous osmosis is observed with pure water instead of polyelectrolyte solution.     

Correlation Between Appearance of Embryogenic Cells and the IAA Levels in Rice Somatic Cell Culture

Changes of endogenous IAA level and IAA action in cultured rice ( Oryza sativa L. ) somatic cells during the period from 7th to 15th day which was the transition from somatic to embryogenic cells were observed. The study was carded out in three experimental systems viz. mature caryopsis and young panicles (2 ~ 5 mm long) of rice cv. "Guangluai 4" under normal osmosis (3% sucrose), mature caryopses from rice cv. "Yanjing 2" or "Guangluai 4" under normal and higher osmosis (5% sucrose or 2.5 % sorbitol). During this period, endogenous IAA contents were greatly increased in young-panicle calli under normal osmosis and mature-caryoptic calli under higher osmosis but decreased in mature-caryoptic calli under normal osmosis. Exogenous IAA could induce the appearance of embryogenic cell from nonembryogenic callus at a lower frequency. And 2,3,5-tri-iodobenzoic acid could increase the frequency of embryogenic cell induction. From these results it could be concluded that accumulation of higher IAA level in the cultured rice cells was essential for induction of embryogenic cell appearance. Since 2,4-D was involved in all induction medium with the same concentration but exerted different effects on embryogenic cell induction, it was suggested that it might act through mediating the endogenous IAA metabolism.     

Transport and kinetics in sandwiched membrane bioreactors.

A bioreactor in which living yeast cells are sandwiched between an ultrafiltration membrane and a reverse osmosis membrane was constructed, and experiments were performed for the conversion of substrate glucose to product ethanol. A set of equations that include both transport through a series of barrier layers and bioreaction rate were developed to predict the performance of the sandwich bioreactor. The above equations were solved by using numerical values for the transport parameter and the bioreaction rate constant, and the results are compared with the experimental data.     

Linear free energy relationship for osmotic water flow through a membrane

A linear free-energy relationship has been found for the osmotic water flux through membranes in a broad variety of systems including electrolytes, organic compounds, intact biological cells and industrial scale filtration. In all cases, broad concentration ranges were found in which the equation In v = In m + β (v. flux (in kg cm⁻² min⁻¹: m. molarity)) was valid. The parameters and β were interpreted in terms of molecular weight, mean ionic radius, enthalpy of solvation. electronic structure and H-bonding propensity. The equation is independent of the membrane material and of the presence of other solutes and precipitates, as long as the latter are incompressible. Its parameters are only slightly dependent upon the temperature. The contributions from different solutes to the osmotic flux are at appreciable concentrations even additive. The relationship permits the prediction of the osmotic water flux and of the rate of filtration of systems of known composition. For simple systems it permits determination of the molecular weight, mean ionic radius, degree of hydration and enthalpy of solvalion. It is suggested that osmosis is primarily due to the shift of hydration equilibria and that guanidine hydrochloride. in a realistic concentration range, forms practically infinite clathrates with water. The properties of the urea and Gdn.HCl systems indicate that these solutes either reversibly change the membrane structure and/or display intrinsic hysteresis.     

Economic evaluation of preconcentration in production of ethanol from dilute sugar solutions

The economic feasibility of preconcentrating dilute sugar solutions prior to fermentation is investigated. Two methods, evaporation and reverse osmosis, are compared. A computer program to determine the optimal preconcentration conditions for glucose solutions of 1.5-16 wt% has been developed. It was used to compute the fractional cost for labor and maintenance, preconcentration, fermentation, and distillation. Preconcentration with evaporation resulted in a higher total cost, compared with no preconcentration, for all cases studied, although a six-effect unit was used. Reverse osmosis was found to be economically feasible for preconcentration to about 5-10 wt % depending on the concentration of the feed.     

Membrane processing of fruit juices and beverages: a review

Membrane technology for the processing of fruit juices and beverages has been applied mainly for clarification using ultrafiltration and microfiltration, and for concentration using reverse osmosis. The effects of product preparation, membrane selection, and operating parameters are important factors influencing filtration rate and product quality. Technological advances related to the development of new membranes, improvement in process engineering, and better understanding of fruit beverage constituents have expanded the range of membrane separation processes. Developments in novel membrane processes, including electrodialysis and pervaporation, increased the array of applications in combination with other technologies for alternate uses in fruit juices and beverages.     

Usefulness of Sau-PCR for molecular epidemiology of nosocomial outbreaks due to Burkholderia cepacia which occurred in a local hospital in Guangzhou, China

The aim of the present study was to determine the source of nosocomial outbreak due to Burkholderia cepacia by molecular techniques. A total of 11 B. cepacia strains were isolated; nine from blood and one from sputum of patients without cystic fibrosis, and one from reverse osmosis water at a local hospital in Guangzhou, China. Analyses of 11 strains by the Sau-PCR assay and pulsed-field gel electrophoresis revealed that nine strains obtained from the blood of outpatients in a hemodialysis unit and one strain from reverse osmosis water had identical DNA profiles, indicating that the reverse osmosis water supply could be a source of infection.     

ON THE CAUSE OF THE INFLUENCE OF IONS ON THE RATE OF DIFFUSION OF WATER THROUGH COLLODION MEMBRANES. I

1. In three previous publications it had been shown that electrolytes influence the rate of diffusion of pure water through a collodion membrane into a solution in three different ways, which can be understood on the assumption of an electrification of the water or the watery phase at the boundary of the membrane; namely, (a) While the watery phase in contact with collodion is generally positively electrified, it happens that, when the membrane has received a treatment with a protein, the presence of hydrogen ions and of simple cations with a valency of three or above (beyond a certain concentration) causes the watery phase of the double layer at the boundary of membrane and solution to be negatively charged. (b) When pure water is separated from a solution by a collodion membrane, the initial rate of diffusion of water into a solution is accelerated by the ion with the opposite sign of charge and retarded by the ion with the same sign of charge as that of the water, both effects increasing with the valency of the ion and a second constitutional quantity of the ion which is still to be defined. (c) The relative influence of the oppositely charged ions, mentioned in (b), is not the same for all concentrations of electrolytes. For lower concentrations the influence of that ion usually prevails which has the opposite sign of charge from that of the watery phase of the double layer; while in higher concentrations the influence of that ion begins to prevail which has the same sign of charge as that of the watery phase of the double layer. For a number of solutions the turning point lies at a molecular concentration of about M/256 or M/512. In concentrations of M/8 or above the influence of the electrical charges of ions mentioned in (b) or (c) seems to become less noticeable or to disappear entirely. 2. It is shown in this paper that in electrical endosmose through a collodion membrane the influence of electrolytes on the rate of transport of liquids is the same as in free osmosis. Since the influence of electrolytes on the rate of transport in electrical endosmose must be ascribed to their influence on the quantity of electrical charge on the unit area of the membrane, we must conclude that the same explanation holds for the influence of electrolytes on the rate of transport of water into a solution through a collodion membrane in the case of free osmosis. 3. We may, therefore, conclude, that when pure water is separated from a solution of an electrolyte by a collodion membrane, the rate of diffusion of water into the solution by free osmosis is accelerated by the ion with the opposite sign of charge as that of the watery phase of the double layer, because this ion increases the quantity of charge on the unit area on the solution side of the membrane; and that the rate of diffusion of water is retarded by the ion with the same sign of charge as that of the watery phase for the reason that this ion diminishes the charge on the solution side of the membrane. When, therefore, the ions of an electrolyte raise the charge on the unit area of the membrane on the solution side above that on the side of pure water, a flow of the oppositely charged liquid must occur through the interstices of the membrane from the side of the water to the side of the solution (positive osmosis). When, however, the ions of an electrolyte lower the charge on the unit area of the solution side of the membrane below that on the pure water side of the membrane, liquid will diffuse from the solution into the pure water (negative osmosis). 4. We must, furthermore, conclude that in lower concentrations of many electrolytes the density of electrification of the double layer increases with an increase in concentration, while in higher concentrations of the same electrolytes it decreases with an increase in concentration. The turning point lies for a number of electrolytes at a molecular concentration of about M/512 or M/256. This explains why in lower concentrations of electrolytes the rate of diffusion of water through a collodion membrane from pure water into solution rises at first rapidly with an increase in concentration while beyond a certain concentration (which in a number of electrolytes is M/512 or M/256) the rate of diffusion of water diminishes with a further increase in concentration.     

How effective are simulated molecular-level experiments for teaching diffusion and osmosis?

Diffusion and osmosis are central concepts in biology, both at the cellular and organ levels. They are presented several times throughout most introductory biology textbooks (e.g., Freeman, 2002), yet both processes are often difficult for students to understand (Odom, 1995; Zuckerman, 1994; Sanger et al., 2001; and results herein). Students have deep-rooted misconceptions about how diffusion and osmosis work, especially at the molecular level. We hypothesized that this might be in part due to the inability to see and explore these processes at the molecular level. In order to investigate this, we developed new software, OsmoBeaker, which allows students to perform inquiry-based experiments at the molecular level. Here we show that these simulated laboratories do indeed teach diffusion and osmosis and help overcome some, but not all, student misconceptions.     

Osmosis in Cortical Collecting Tubules : A Theoretical and Experimental Analysis of the Osmotic Transient Phenomenon

This paper reports a theoretical analysis of osmotic transients and an experimental evaluation both of rapid time resolution of lumen to bath osmosis and of bidirectional steady-state osmosis in isolated rabbit cortical collecting tubules exposed to antidiuretic hormone (ADH). For the case of a membrane in series with unstirred layers, there may be considerable differences between initial and steady-state osmotic flows (i.e., the osmotic transient phenomenon), because the solute concentrations at the interfaces between membrane and unstirred layers may vary with time. A numerical solution of the equation of continuity provided a means for computing these time-dependent values, and, accordingly, the variation of osmotic flow with time for a given set of parameters including: P_f (cm s^–1), the osmotic water permeability coefficient, the bulk phase solute concentrations, the unstirred layer thickness on either side of the membrane, and the fractional areas available for volume flow in the unstirred layers. The analyses provide a quantitative frame of reference for evaluating osmotic transients observed in epithelia in series with asymmetrical unstirred layers and indicate that, for such epithelia, P_f determinations from steady-state osmotic flows may result in gross underestimates of osmotic water permeability. In earlier studies, we suggested that the discrepancy between the ADH-dependent values of P_f and P_DDw (cm s^–1, diffusional water permeability coefficient) was the consequence of cellular constraints to diffusion. In the present experiments, no transients were detectable 20–30 s after initiating ADH-dependent lumen to bath osmosis; and steady-state ADH-dependent osmotic flows from bath to lumen and lumen to bath were linear and symmetrical. An evaluation of these data in terms of the analytical model indicates: First, cellular constraints to diffusion in cortical collecting tubules could be rationalized in terms of a 25-fold reduction in the area of the cell layer available for water transport, possibly due in part to transcellular shunting of osmotic flow; and second, such cellular constraints resulted in relatively small, approximately 15%, underestimates of P_f.