Influence of CuSO4 spectral filters,daminozide, and exogenous gibberellic acid on growth ofDendranthema Xgrandiflorum (Ramat.) Kitamura ‘bright golden anne’

The response of chrysanthemum plants to gibberellic acid (GA₃) and daminozide, grown under 6% CuSO₄ and water (control) spectral filters, was evaluated to determine the involvement of gibberellins in regulation of plant height under CuSO₄ filters. The CuSO₄ filter increased the red (R)/farred (FR), and blue (B)/R ratio (R=600–700 nm; FR =700–800 nm; B=400–500 nm) of transmitted light. PPF under 6% CuSO₄ filter was reduced by about 34% compared to PPF under water filter which averaged about 750 μM·m^?2·s^?1. Control plants were shaded with Saran Wrap to ensure equal PPF as in the CuSO₄ chamber. GA₃ application increased plant height under both the control and CuSO₄ filter, but the height increase under the CuSO₄ filter was about 20% greater than that under the control filter. Daminozide treatment reduced plant height under the control and CuSO₄ filter, but the height reduction in control plants was slightly greater than under the CuSO₄ filter. The height reduction caused by daminozide was prevented by GA₃ application in plants grown under the control or CuSO₄ filter. The results suggest that GA₃ may be partially involved in height reduction under CuSO₄ filters.     

Mechanism of tetrodotoxin block and resistance in sodium channels

Tetrodotoxin (TTX) has been used for many decades to characterize the structure and function of biological ion channels. Yet, the precise mechanism by which TTX blocks voltage-gated sodium (Na_V) channels is not fully understood. Here molecular dynamics simulations are used to elucidate how TTX blocks mammalian voltage-gated sodium (Nav) channels and why it fails to be effective for the bacterial sodium channel, Na_VAb. We find that, in Na_VAb, a sodium ion competes with TTX for the binding site at the extracellular end of the filter, thus reducing the blocking efficacy of TTX. Using a model of the skeletal muscle channel, Na_V1.4, we show that the conduction properties of the channel observed experimentally are faithfully reproduced. We find that TTX occludes the entrance of Na_V1.4 by forming a network of hydrogen-bonds at the outer lumen of the selectivity filter. The guanidine group of TTX adopts a lateral orientation, rather than pointing into the filter as proposed previously. The acidic residues just above the selectivity filter are important in stabilizing the hydrogen-bond network between TTX and Na_V1.4. The effect of two single mutations of a critical tyrosine residue in the filter of Na_V1.4 on TTX binding observed experimentally is reproduced using computational mutagenesis.     

Assessment of iodine‐treated filter media for removal and inactivation of MS2 bacteriophage aerosols

Aims: To investigate the performance of an iodine‐releasing filter medium for use as a protective device against airborne pathogens. Methods and Results: The filter’s physical and viable removal efficiencies (VRE) were investigated with challenges of MS2 bacteriophage aerosols, and the infectivity of MS2 collected on the filter was analysed. To test a proposed inactivation mechanism, media containing thiosulfate or bovine serum albumin (BSA) were put in impingers to quench and consume I₂ released from the filter. In direct plating experiments, treated filters presented significantly higher VREs than did untreated filters; however, collection in excess BSA decreased VRE by half and in thiosulfate the apparent VRE decreased drastically. No significant difference in infectivity of retained viruses on treated and untreated filters was observed at the same environmental condition. Conclusions: Evidence presented herein for competition by dissolved I₂ in infectivity assays supports a mechanism of induced displacement and capture of I_2. It also requires that dissociation of iodine from the filter and capture of iodine by MS2 aerosols as they pass through the filter be factored in the design of the assessment methodology. The filter’s strong retention capability minimizes reaerosolization but also makes it difficult to discriminate the antimicrobial effect at the surface. Significance and Impact of the Study: This study shows the direct plating assay method to be sensitive to interference by iodine‐releasing materials. This requires reevaluation of earlier reports of VRE measurements.     

Efficiency of Commercial Air Filters Against Marek's Disease Virus

In a series of 10 replicate trials with susceptible chickens as indicators of the presence of virus in the air, filter B₁ (Dri Pak, American Air Filter Co.), which has a dust spot rating of 93 to 97%, and filter C (Astrocel), with a dioctyl phathalate aerosol rating of over 99%, completely removed Marek''s disease virus (MDV) from highly contaminated air. However, air passed through filter B₂ (Duracel), with a dust spot rating of 34 to 45%, remained infectious. Thus, an air filter with a dust spot rating of over 93% will effectively remove MDV from the air. The smallest infectious particles in the air are estimated to be greater than 0.3 μm in diameter.     

Role of Ion Distribution and Energy Barriers for Concerted Motion of Subunits in Selectivity Filter Gating of a K+ Channel

Most potassium channels have two main gate locations, hosting an inner gate at the cytosolic entrance and a filter gate in the selectivity filter; the function of these gates is in many channels coupled. To obtain exclusive insights into the molecular mechanisms that determine opening and closing of the filter gate, we use a combination of single-channel recordings and gating analysis in the minimal viral channel Kcv_NTS. This channel has no inner gate, and its fast closing at negative voltages can therefore be entirely assigned to the filter gate. We find that mutations of S42 in the pore helix severely slow down closing of this filter gate, an effect which is not correlated with hydrogen bond formation by the amino acid at this position. Hence, different from KcsA, which contains the critical E71 in the equivalent position forming a salt bridge, the coupling between selectivity filter and surrounding structures for filter gating must in Kcv_NTS rely on different modes of interaction. Quantitative analysis of concatemers carrying different numbers of S42T mutations reveals that each subunit contributes the same amount of ～ 0.4 kcal/mol to the energy barrier for filter closure indicating a concerted action of the subunits. Since the mutations have neither an influence on the unitary current nor on the voltage dependency of the gate, the data stress that the high subunit cooperativity is mediated through conformational changes rather than through changes in the ion occupation in the selectivity filter.     

A complex of various enzymes concerned with DNA synthesis in Yoshida sarcoma

When the postmicrosomal supernatant from Yoshida sarcoma was filtered through a Sartorius membrane filter (0.1 μ pore size), incorporation of ¹⁴C-thymidine into DNA was observed in the filter. The filter was found to contain over 80 % of the total DNA polymerase and thymidine kinase activities and 50 % of the total TMP kinase activity present in the postmicrosomal supernatant, while 100 % of the lactic dehydrogenase was found in the filtrate. When MgCl₂ was added to the postmicrosomal supernatant from Yoshida sarcoma, formation of the complex increased, maximal complex formation being observed with 1.0×10^?2M MgCl₂.     

Microbial biogeography across a full-scale wastewater treatment plant transect: evidence for immigration between coupled processes

Wastewater treatment plants use a variety of bioreactor types and configurations to remove organic matter and nutrients. Little is known regarding the effects of different configurations and within-plant immigration on microbial community dynamics. Previously, we found that the structure of ammonia-oxidizing bacterial (AOB) communities in a full-scale dispersed growth activated sludge bioreactor correlated strongly with levels of NO₂ ^? entering the reactor from an upstream trickling filter. Here, to further examine this puzzling association, we profile within-plant microbial biogeography (spatial variation) and test the hypothesis that substantial microbial immigration occurs along a transect (raw influent, trickling filter biofilm, trickling filter effluent, and activated sludge) at the same full-scale wastewater treatment plant. AOB amoA gene abundance increased >30-fold between influent and trickling filter effluent concomitant with NO₂ ^? production, indicating unexpected growth and activity of AOB within the trickling filter. Nitrosomonas europaea was the dominant AOB phylotype in trickling filter biofilm and effluent, while a distinct “Nitrosomonas-like” lineage dominated in activated sludge. Prior time series indicated that this “Nitrosomonas-like” lineage was dominant when NO₂ ^? levels in the trickling filter effluent (i.e., activated sludge influent) were low, while N. europaea became dominant in the activated sludge when NO₂ ^? levels were high. This is consistent with the hypothesis that NO₂ ^? production may cooccur with biofilm sloughing, releasing N. europaea from the trickling filter into the activated sludge bioreactor. Phylogenetic microarray (PhyloChip) analyses revealed significant spatial variation in taxonomic diversity, including a large excess of methanogens in the trickling filter relative to activated sludge and attenuation of Enterobacteriaceae across the transect, and demonstrated transport of a highly diverse microbial community via the trickling filter effluent to the activated sludge bioreactor. Our results provide compelling evidence that substantial immigration between coupled process units occurs and may exert significant influence over microbial community dynamics within staged bioreactors.     

Distribution and Rate of Microbial Processes in an Ammonia-Loaded Air Filter Biofilm

The in situ activity and distribution of heterotrophic and nitrifying bacteria and their potential interactions were investigated in a full-scale, two-section, trickling filter designed for biological degradation of volatile organics and NH₃ in ventilation air from pig farms. The filter biofilm was investigated by microsensor analysis, fluorescence in situ hybridization, quantitative PCR, and batch incubation activity measurements. In situ aerobic activity showed a significant decrease through the filter, while the distribution of ammonia-oxidizing bacteria (AOB) was highly skewed toward the filter outlet. Nitrite oxidation was not detected during most of the experimental period, and the AOB activity therefore resulted in NO₂⁻, accumulation, with concentrations often exceeding 100 mM at the filter inlet. The restriction of AOB to the outlet section of the filter was explained by both competition with heterotrophic bacteria for O₂ and inhibition by the protonated form of NO₂⁻, HNO₂. Product inhibition of AOB growth could explain why this type of filter tends to emit air with a rather constant NH₃ concentration irrespective of variations in inlet concentration and airflow.Emissions of NH₃, odorous organic gasses, and dust from pig facilities cause significant problems for neighbors and the surrounding natural environment. In Denmark, swine production accounts for 34% of the total atmospheric NH₃ emission, of which 50% originates from pig house emissions (19). Furthermore, multiple volatile and very odorous organic compounds are emitted with animal house exhaust air and constitute a severe nuisance in residential areas (16, 31). While biofilters based on wood chips, compost, and peat have proven efficient in removing complex mixtures of volatile organic compounds (VOC) from piggery exhaust air, biotrickling filters have been shown to be efficient in both odor and NH₃ removal (30). In these filters, airborne VOC and NH₃ are taken up by an irrigated biofilm and oxidized by organoheterotrophic and nitrifying bacteria, respectively, resulting in the production of CO₂, NO₂⁻ or NO₃⁻, and microbial biomass (43). The nitrification process, which comprises the two-step oxidation of NH₃ via NO₂⁻ to NO₃⁻, is catalyzed by ammonia-oxidizing bacteria (AOB) and ammonia-oxidizing archaea and by nitrite-oxidizing bacteria (NOB), respectively (22, 23). However, in many biotrickling filters, NOB activity seems to be absent, resulting in NO₂⁻ being the end product of nitrification (29).Waste products often accumulate in biotrickling filters, as the water is recycled many times to minimize wastewater discharge. In particular, NO₂⁻ may accumulate to concentrations above 100 mM (29), resulting in high levels of free nitrous acid (FNA, or HNO₂), which is inhibitory to many microorganisms (2, 40, 50). As a result of an overall countercurrent air-water flow, FNA, VOC, and NH₃ concentrations are expected to decrease from the filter air inlet toward the outlet, potentially promoting a gradient of microbial processes and species distribution through the filter.Also, on a smaller scale, physical and chemical heterogeneity results in microgradients of substrates and O₂ within the biofilm that may affect the spatial distribution and rate of microbial processes. While considerable research effort has been given to the physicochemical aspects of filter optimization (11, 44), very little is known about the distribution, activity, and potential interactions of bacterial processes in the biofilm. Problems frequently arise, such as highly variable odor reduction, failed NH₃ removal, and filter clogging due to excess biofilm growth and slime excretion. Improved insight into the dynamics of the microbial activities may help control the biological processes in order to optimize and stabilize filter performance.In this study, the in situ activity and distribution of organoheterotrophic bacteria and AOB and the identity and NH₃ oxidation potential of the AOB were investigated in a two-section, full-scale biological air filter treating waste gas from a pig facility. Biofilms in different filter sections along a gradient of decreasing VOC and NH₃ load and NO₂⁻ accumulation were characterized. The goal was to attain a basic understanding of the microbial processes and thus filter function.     

Nickel removal from nickel plating waste water using a biologically active moving-bed sand filter

Efficient removal of dissolved nickel was observed in a biologically active moving-bed `MERESAFIN' sand filter treating rinsing water from an electroless nickel plating plant. Although nickel is fully soluble in this waste water, its passage through the sand filter promoted rapid removal of approximately 1 mg Ni/l. The speciation of Ni in the waste water was modelled; the most probable precipitates forming under the conditions in the filter were predicted using PHREEQC. Analyses of the Ni-containing biosludge using chemical, electron microscopical and X-ray spectroscopic techniques confirmed crystallisation of nickel phosphate as arupite (Ni₃(PO₄)₂.8H₂O), together with hydroxyapatite within the bacterial biofilm on the filter sand grains. Biosorption contributed less than 1% of the overall sequestered nickel. Metabolising bacteria are essential for the process; the definitive role of specific components of the mixed population is undefined but the increase in pH promoted by metabolic activity of some microbial components is likely to promote nickel desolubilisation by others.     

Experimental assessment of the influence of beam hardening filters on image quality and patient dose in volumetric 64-slice X-ray CT scanners

Beam hardening filters have long been employed in X-ray Computed Tomography (CT) to preferentially absorb soft and low-energy X-rays having no or little contribution to image formation, thus allowing the reduction of patient dose and beam hardening artefacts. In this work, we studied the influence of additional copper (Cu) and aluminium (Al) flat filters on patient dose and image quality and seek an optimum filter thickness for the GE LightSpeed VCT 64-slice CT scanner using experimental phantom measurements. Different thicknesses of Cu and Al filters (0.5–1.6 mm Cu, 0.5–4 mm Al) were installed on the scanner’s collimator. A planar phantom consisting of 13 slabs of Cu having different thicknesses was designed and scanned to assess the impact of beam filtration on contrast in the intensity domain (CT detector’s output). To assess image contrast and image noise, a cylindrical phantom consisting of a polyethylene cylinder having 16 holes filled with different concentrations of K₂HPO₄ solution mimicking different tissue types was used. The GE performance and the standard head CT dose index (CTDI) phantoms were also used to assess image resolution characterized by the modulation transfer function (MTF) and patient dose defined by the weighted CTDI. A 100 mm pencil ionization chamber was used for CTDI measurement. Finally, an optimum filter thickness was determined from an objective figure of merit (FOM) metric. The results show that the contrast is somewhat compromised with filter thickness in both the planar and cylindrical phantoms. The contrast of the K₂HPO₄ solutions in the cylindrical phantom was degraded by up to 10% for a 0.68 mm Cu filter and 6% for a 4.14 mm Al filter. It was shown that additional filters increase image noise which impaired the detectability of low density K₂HPO₄ solutions. It was found that with a 0.48 mm Cu filter the 50% MTF value is shifted by about 0.77 lp/cm compared to the case where the filter is not used. An added Cu filter with approximately 0.5 mm thickness accounts for 50% reduction in radiation-absorbed dose as measured by the weighted CTDI. The FOM results indicate that with an additional filter of 0.5 mm Cu or minimum 4 mm Al, a good compromise between image quality and patient dose is achieved for CT images acquired at tube voltages of 120 and 140 kVp. The results seem to indicate that an optimum filter for high kVp acquisitions, routinely used in cardiovascular imaging, should be 0.5 mm copper or 4 mm aluminium minimum.     

Shaker-IR K+ channel gating in heavy water: Role of structural water molecules in inactivation

It has been reported earlier that the slow (C-type) inactivated conformation in K_v channels is stabilized by a multipoint hydrogen-bond network behind the selectivity filter. Furthermore, MD simulations revealed that structural water molecules are also involved in the formation of this network locking the selectivity filter in its inactive conformation. We found that the application of an extracellular, but not intracellular, solution based on heavy water (D₂O) dramatically slowed entry into the slow inactivated state in Shaker-IR mutants (T449A, T449A/I470A, and T449K/I470C, displaying a wide range of inactivation kinetics), consistent with the proposed effect of the dynamics of structural water molecules on the conformational stability of the selectivity filter. Alternative hypotheses capable of explaining the observed effects of D₂O were examined. Increased viscosity of the external solution mimicked by the addition of glycerol had a negligible effect on the rate of inactivation. In addition, the inactivation time constants of K⁺ currents in the outward and the inward directions in asymmetric solutions were not affected by a H₂O/D₂O exchange, negating an indirect effect of D₂O on the rate of K⁺ rehydration. The elimination of the nonspecific effects of D₂O on our macroscopic current measurements supports the hypothesis that the rate of structural water exchange at the region behind the selectivity filter determines the rate of slow inactivation, as proposed by molecular modeling.     

Nitrogen and phosphorus cycling in relation to stand age of Ecucalyptus regnans F. Muell

Water movement between a root and the soil depends on the hydraulic conductances of the soil, the root, and the intervening root-soil air gap (L_gap) created as roots shrink during soil drying. To measure L_gap, segments of young cylindrical roots of Agave deserti about 3 mm in diameter were placed concentrically or eccentrically within tubes of moistened filter paper at a known water potential. As the width of the air gap between the filter paper and a concentrically located root was made smaller, measured L_gap increased less than did predicted L_gap based on isothermal conditions. For gaps of the size expected in the soil during water loss from roots (e.g., 10% of the root radius), the underprediction was about 70% and was primarily caused by a lowering of the root surface temperature accompanying water evaporation. As a root segment was eccentrically moved toward the filter paper, the measured L_gap increased. For the most eccentric case of touching the filter paper, the measured L_gap was 2.4-fold greater than for the concentric case, compared with an infinite L_gap predicted if the water potential were constant around the root surface. When a root touched soil with a water potential of -1.0MPa, L_gap estimated using a graphical method increased about 2.3-fold and the overall conductance of the root-soil system increased by 31% compared with the concentric case. For markedly eccentric locations of roots in air gaps, L_gap, which can be the principal conductance initially limiting water loss from roots to a drying soil, can be about 60% of the value predicted for the concentric isothermal case.     

Investigations of boron uptake at the cellular level

The efficiency of recovery of P by iron oxide-impregnated filter paper, as used in the new P_i test for soil phosphorus, was found to depend on the method used for impregnating the paper with iron oxide and could range from as little as 28% to more than 98%. The greatest efficiency of recovery was obtained with filter papers which had been washed with deionised water following iron oxide-impregnation. These filter papers were also found to give the most reproducible results. ei]{gnB E}{fnClothier}     

Growth and development of embryo parts during the germination of caryopses of the wild oat (Avena fatua L.)

Wild oat (Avena fatua L.) caryopses were germinated on moist filter paper and under water in the presence and absence of hydrogen peroxide (H₂O₂). The sequential growth and development of embryo parts were studied. Germination, as indicated by radicle emergence, was least and slowest in caryopses submerged in deoxygenated water. The coleorhiza in such caryopses elongated much earlier than the root, in contrast to the other treatments where the coleorhiza and the root emerged at about the same time. In caryopses incubated on moist filter paper all embryo parts showed considerable growth. In H₂O₂ treated caryopses only the epicotyl showed substantial growth over the experimental period. In all treatments the first mitotic peaks were noticed at the same period. The occurrence of these early nuclear divisions may be due to release of 4 C nuclei from inhibition by the uptake of water during caryopsis imbibition. The mitosis continued in the radicle of the embryo in those caryopses germinating on moist filter paper, indicating occurrence of DNA synthesis. In the other two treatments, however, few divisions were detected. Here the early growth of the root, causing caryopsis germination, was due to cell elongation, especially in the proximal part of the root.     

Two selective filters in the calcium channel of the molluscan neuron somatic membrane

Modification of the calcium channel of the somatic membrane of molluscan neurons under the influence of EDTA and other Ca-binding agents was investigated. The results showed that there are two selective filters in the calcium channel of this membrane. The first is located near the outer pore of the calcium channel and it binds bivalent cations in the order:pK _Ca:pK _Sr:pK _Ba:pK _Mg=6.6:5.5:4.8:4.2. This external filter regulates selectivity of the channel relative to the charge of the cation and it conjecturally contains several carboxyl groups. The second selective filter lies inside the channel and regulates permeability for ions with a single charge. It is suggested that the structure of the inner filter closely resembles that postulated by Hille for the selective filter of the sodium channel, and that it contains one carboxyl group. The results of investigation of the effect of Ca⁺⁺, Cd⁺⁺, and H⁺ on the fast sodium current of the somatic membrane showed that it is not blocked by these ions, but the decrease observed in its amplitude is connected with a change in the membrane surface potential and a corresponding change in the juxtamembranous concentration of carrier ions. On the basis of the experimental results it is postulated that the selective filter of the fast sodium channel of the molluscan neuron somatic membrane does not contain a carboxyl group.A. A. Bogomolets Institute of Physiology, Academy of Sciences of the Ukrainian SSR, Kiev. Translated from Neirofiziologiya, Vol. 15, No. 4, pp. 420–427, July–August, 1983.     

Scavenging of free radicals in gas-phase mainstream cigarette smoke by immobilized catalase at filter level

Catalase is well known as capable of inducing the decomposition of H₂O₂. In this study, a kind of immobilized catalase (entrapped in cross-linked chitosan beads) was dispersed in conventional acetate filter as an antioxidant additive. Quantitative estimation of the free radicals in mainstream cigarette smoke (MCS) was performed to address the effect of this modified filter. It was found that the levels of PBN adduct and NO^?/NO₂^? associated with the gas-phase mainstream cigarette smoke (GPCS) were efficiently decreased by ～40% through catalase filtering. Besides, the modified filter was found to lower the MCS-induced adverse biological effects including lipid peroxidation and mutagenicity. This was proved to be substantially attributed to the catalase-dependent breakdown of NO^?, which was stimulated by some of peroxides (most probably being H₂O₂), the dismutation products of tar particulate matters (TPM). These results highlighted a promising approach to reduce the smoking-associated health risks to passive smokers. Moreover, the mechanisms of catalase filtering may be helpful for the development of appropriate immobilized enzyme systems to be applied for reducing health risks associated with gaseous pollutants.     

Impact of Low Filter Resistances on Subjective and Physiological Responses to Filtering Facepiece Respirators

Ten subjects underwent treadmill exercise at 5.6 km/h over one hour while wearing each of three identical appearing, cup-shaped, prototype filtering facepiece respirators that differed only in their filter resistances (3 mm, 6 mm, and 9 mm H₂O pressure drop). There were no statistically significant differences between filtering facepiece respirators with respect to impact on physiological parameters (i.e., heart rate, respiratory rate, oxygen saturation, transcutaneous carbon dioxide levels, tympanic membrane temperature), pulmonary function variables (i.e., tidal volume, respiratory rate, volume of carbon dioxide production, oxygen consumption, or ventilation), and subjective ratings (i.e., exertion, thermal comfort, inspiratory effort, expiratory effort and overall breathing comfort). The nominal filter resistances of the prototype filtering facepiece respirators correspond to airflow resistances ranging from 2.1 - 6.6 mm H₂O/L/s which are less than, or minimally equivalent to, previously reported values for the normal threshold for detection of inspiratory breathing resistance (6 - 7.6 mm H₂O/L/sec). Therefore, filtering facepiece respirators with filter resistances at, or below, this level may not impact the wearer differently physiologically or subjectively from those with filter resistances only slightly above this threshold at low-moderate work rates over one hour.     

The use of vertical flow constructed wetlands for on-site treatment of domestic wastewater: New Danish guidelines

Official guidelines for the on-site treatment of domestic sewage have recently been published by the Danish Ministry of Environment as a consequence of new treatment requirements for single houses and dwellings in rural areas. This paper summarises the guidelines for vertical constructed wetland systems (planted filter beds) that will fulfil demands of 95% removal of BOD and 90% nitrification. The system can be extended with chemical precipitation of phosphorus with aluminium polychloride in the sedimentation tank to meet requirements of 90% phosphorus removal. The necessary surface area of the filter bed is 3.2 m²/person equivalent and the effective filter depth is 1.0 m. The filter medium must be filtersand with a d₁₀ between 0.25 and 1.2 mm, a d₆₀ between 1 and 4 mm, and a uniformity coefficient (U = d₆₀/d₁₀) less than 3.5. The sewage is, after sedimentation, pulse-loaded onto the surface of the bed using pumping and a network of distribution pipes. The drainage layer in the bottom of the bed is passively aerated through vertical pipes extending into the atmosphere in order to improve oxygen transfer to the bed medium. Half of the nitrified effluent from the filter is recirculated to the first chamber of the sedimentation tank or to the pumping well in order to enhance denitrification and to stabilise the treatment performance of the system. A phosphorus removal system is installed in the sedimentation tank using a small dosing pump. The mixing of chemicals is obtained by a simple airlift pump, which also circulates water in the sedimentation tank. The vertical flow constructed wetland system is an attractive alternative to the common practice of soil infiltration and provides efficient treatment of sewage for discharge into the aquatic environment.     

Models of the structure and gating mechanisms of the pore domain of the NaChBac ion channel

The NaChBac prokaryotic sodium channel appears to be a descendent of an evolutionary link between voltage-gated K_V and Ca_V channels. Like K_V channels, four identical six-transmembrane subunits comprise the NaChBac channel, but its selectivity filter possesses a signature sequence of eukaryotic Ca_V channels. We developed structural models of the NaChBac channel in closed and open conformations, using K⁺-channel crystal structures as initial templates. Our models were also consistent with numerous experimental results and modeling criteria. This study concerns the pore domain. The major differences between our models and K⁺ crystal structures involve the latter portion of the selectivity filter and the bend region in S6 of the open conformation. These NaChBac models may serve as a stepping stone between K⁺ channels of known structure and Na_V, Ca_V, and TRP channels of unknown structure.