Permeable membrane

The synthetic and plasmid DNAs are mixed and join their sticky ends spontaneously. They are covalently bound together by DNA ligases, when the resulting hybrid plasmid is inserted into bacterial cells. Dilute calcium chloride solutions render the bacterial membranes permeable and allow the passage of ONA into the cells. 

Membrane filtration Membrane module Membrane permeability Membrane process Membrane processes Membrane reactor Membrane roofing Membranes... 

Although microporous membranes are a topic of research interest, all current commercial gas separations are based on the fourth type of mechanism shown in Figure 36, namely diffusion through dense polymer films. Gas transport through dense polymer membranes is governed by equation 8 where is the flux of component /,andare the partial pressure of the component i on either side of the membrane, /is the membrane thickness, and is a constant called the membrane permeability, which is a measure of the membrane s ability to permeate gas. The ability of a membrane to separate two gases, i and is the ratio of their permeabilities,a, called the membrane selectivity (eq. 9). 

Sequential batch diafiltration is a series of dilution—concentration steps. The concentration of membrane-permeable species is... 

Most of the naturally-occurring pyrazine hydroxamic acids appear to be derived from valine, leucine and isoleucine, and biosynthetic studies by MacDonald and coworkers (61JBC(236)512, 62JBC(237)1977, 65JBC(240)1692) indicate that these amino acids are incorporated. However, it would seem that the logical intermediates, viz. the 2,5-dioxopiperazines such as (111) and (112), are not always incorporated. This does not rule out their intermediacy, as there may be problems such as low solubility or membrane permeability which prevent their efficient incorporation. An exception to these results was reported for pulcherrimic acid (113) (65BJ(96)533), which has been shown to be derived from cyclo-L-leu-L-leu which serves as an efficient precursor. 

An important characteristic of pervaporation that distinguishes it from distillation is that it is a rate process, not an equilibrium process. The more permeable component may be the less-volatile component. Perv oration has its greatest iitihty in the resolution of azeotropes, as an acqiinct to distillation. Selecting a membrane permeable to the minor corTiponent is important, since the membrane area required is roughly proportional to the mass of permeate. Thus pervaporation devices for the purification of the ethanol-water azeotrope (95 percent ethanol) are always based on a hydrophihc membrane. 

The factors to consider in the selection of cross-flow filtration include the cross-flow velocity, the driving pressure, the separation characteristics of the membrane (permeability and pore size), size of particulates relative to the membrane pore dimensions, and the hydrodynamic conditions within the flow module. Again, since particle-particle and particle-membrane interactions are key, broth conditioning (ionic strength, pH, etc.) may be necessary to optimize performance. 

Fig. 5-9. Total number of stages and total membrane surfaee area versus membrane seleetivity for the separation of 1 kg s of a raeemie mixture at a membrane permeability of 1.6 x 10 kg m. s, yielding both enantiomers at 95 % purity [55].

Shimomura, O. (1997). Membrane permeability of coelenterazine analogues measured with fish eggs. Biocbem. J. 326 297-298. 

More than 50 endogenous and exogenous inhibitors of the calpains have been described as either transition-state reversible or irreversible inhibitors. The first transition-state inhibitors were the peptide aldehydes (e.g., leupeptin). Using this compound, new ones were synthesized that exhibited improved membrane permeability and calpain specificity (e.g., calpeptin). Other groups of inhibitors have since been discovered a-dicarbonyls (originally developed as serine protease inhibitors), nonpeptide quinolinecarboxamides,... 

Outer Membrane Permeability and Active Efflnx Systems... 

The thermodynamic aspect of osmotic pressure is to be sought in the expenditure of work required to separate solvent from solute. The separation may be carried out in other ways than by osmotic processes thus, if we have a solution of ether in benzene, we can separate the ether through a membrane permeable to it, or we may separate it by fractional distillation, or by freezing out benzene, or lastly by extracting the mixture with water. These different processes will involve the expenditure of work in different ways, but, provided the initial and final states are the same in each case, and all the processes are carried out isothermally and reversibly, the quantities of work are equal. This gives a number of relations between the different properties, such as vapour pressure and freezing-point, to which we now turn our attention. 

The ion pair extraction by flow injection analysis (FIA) has been used to analyze sodium dodecyl sulfate and sodium dodecyl ether (3 EO) sulfate among other anionic surfactants. The solvating agent was methanol and the phase-separating system was designed with a PTFE porous membrane permeable to chloroform but impermeable to the aqueous solution. The method is applicable to concentrations up to 1.25 mM with a detection limit of 15 pM [304]. 

The polymeric products from disordered AG have much smaller molecular weights and reduced tendency to self-associate in solution. Such properties may be desirable in applications requiring membrane permeability. 

TBT and TFT are membrane-active molecules, and their mechanism of action appears to be strongly dependent on organotin(IV) lipophilicity. They function as ionophores and produce hemolysis, release Ca(II) from sarcoplasmic reticulum, alter phosphatodylseiine-induced histamine release, alter mitochondrial membrane permeability and perturb membrane enzymes. Organotin(IV) compounds have been shown to affect cell signaling they activate protein kinase and increase free arachidonic acid through the activation of phospholipase... 

Physiologically Based Phamiacokinetic (PBPK) Model—Comprised of a series of compartments representing organs or tissue groups with realistic weights and blood flows. These models require a variety of physiological information tissue volumes, blood flow rates to tissues, cardiac output, alveolar ventilation rates and, possibly membrane permeabilities. The models also utilize biochemical information such as air/blood partition coefficients, and metabolic parameters. PBPK models are also called biologically based tissue dosimetry models. 

Simon, E.W. (1974). Phospholipids and plant membrane permeability. New Phyto-logist, 73, 377-420. 

B. G. Phospholipid membrane permeability of peptide nucleic acid. FEB. S. Lett. 

Simmons C.G., Pitts A. E., Mayfield L. D., Shay J.W., Corey D.R. Synthesis and membrane permeability of PNA-pep-tide conjugates. Bioorg. Med. Chem. Lett. 1997 7 3001-3006. 

L. B. Kier and C.-K. Cheng, A cellular automata model of membrane permeability. J. Theor. Biol. 1997, 186, 75. 

A dual isotope labeling technique [85] has been used to measure membrane permeability in plant cells, based on the selective permeabiHty of the membranes of living cells to tritiated water and carbon-14 labeled mannitol. Kieran [29] showed that the results of the dual isotope labeling and Evan s Blue staining methods correlated well as indicators of cell viability however, the latter was preferable in terms of reagent cost and ease of analysis. 

Refsgaard HH, Jensen BF, Brockhoff PB, Padkjaer SB, Guldbrandt M and Christensen MS. In silico prediction of membrane permeability from calculated molecular parameters. J Med Chem 2005 48 805-11. 

Irvine JD, Takahashi L, Lockhart K, Cheong J, Tolan JW, Selick HE, et al. MDCK (Madin-Darby canine kidney) cells a tool for membrane permeability screening. J Pharm Sci 1999 88 28-33. 

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