Behaviour of Scrobicularia plana (Da Costa) in water of various salinities

Valve movements, heart and pumping rates have been recorded from Scrobicularia plana (Da Costa) when transferred stepwise from natural sea water to sea water of S = 30% (termed 100%) and then to 80, 60, 40, and 20% sea water, and after direct transfer from 100 to 20% Scrobicularia exhibits short periods of pumping alternating with short ventilatory pauses down to 40% sea water. These are termed activity cycles and contrast with periods of complete quiescence each ≈ 4–12 h long. The heart rate of animals in these salinities is fairly constant during activity cycles. When transferred to 20% sea water, either directly or gradually, short pumping phases alternate with long ventilatory pauses during the initial 72 h. At the same time the heart rate shows wide variation during activity cycles.On transference from 100 to 60% sea water, the valves opened and valve activity pattern returned to normal within 30 min and within 6 h of transfer from 60 into 40% SW. Transfer to 20%, whether stepwise or directly, resulted in valves remaining closed initially for ≈ 10 or 34 h, respectively before opening gradually to expose the mantle margin. The valve adductions were then of reduced frequency and extent.     

Steady-state analysis of self-heated thermistors using finite elements

The purpose of this work is to validate, using numerical, finite element methods, the thermal assumptions made in the analytical analysis of a coupled thermistor probe-tissue model upon which a thermal conductivity measurement scheme has been based. Analytic, closed form temperature profiles generated by the self-heated thermistors can be found if three simplifying assumptions are made: the thermistor is spherical; heat is generated in all regions of the bead; and heat is generated uniformly in the bead. This analytic solution is used to derive a linear relationship between tissue thermal conductivity and the ratio of thermistor temperature rise over electrical power required to maintain that temperature rise. This derived, linear relationship is used to determine thermal conductivity from the observed experimental data. However, in reality, the thermistor bead is a prolate spheroid surrounded by a passive shell, and the heating pattern in the bead is highly nonuniform. In the physical system, the exact relationship between the tissue thermal conductivity and parameters measured by the thermistor is not known. The finite element method was used to calculate the steady-state temperature profiles generated by thermistor beads with realistic geometry and heating patterns. The results of the finite element analysis show that the empirical, linear relationship remains valid when all three simplified assumptions are significantly relaxed.     

Flow rate and bead size as critical parameters for immobilized-yeast reactors

The productivity of immobilized yeast cell reactors varies with a number of parameters, including flow, amount and growth rate of yeast, bead size and type of medium. Variation of these parameters has a pronounced effect on reaction rate. This paper presents typical ranges for these productivities and demonstrates the patterns of changes that take place when bead size, flow and reaction medium are varied. Saccharomyces cerevisiae cells were immobilized in calcium alginate beads for the production of ethanol. The productivity of immobilized yeast in a batch reactor (0.2 g ethanol/g yeast · h) was only two-thirds that of free cells suspended at an equivalent cell density (0.3 g ethanol/g yeast · h). Different flow rates and bead sizes were used to ‘optimize’ the productivity. The productivity of 3.34 mm beads at a flow rate of 8.8 litre h^?1(superficial velocity: 0.12 cm s^?1) was 95% higher than that at 1.0 l h^?1. Maximum productivities of 0.34, 0.27, 0.22 g/g yeast· h were obtained (at a flow rate of 8.8 l h^?1) for 9.2% yeast-immobilized beads of 3.34, 4.45 and 5.65 mm in diameter, respectively.     

Airflow characteristics in a baboon nasal passage cast

Airflow patterns in the nasal passages influence the distribution of air-pollutant-induced lesions in the airway mucosa. Little is known about airflow characteristics of the complex nasopharyngeal airway of humans and experimental animals. Airflow characteristics in the nasopharyngeal airways of an adult male baboon (13.9 kg body wt) were investigated with thermistor probes and the findings compared with flow visualization, using a cinephotographic technique. A clear, acrylic, hollow cast of a baboon nose was made, and thermistor probes were inserted to record air velocity in the cast lumen using a wind tunnel to propel air through the cast. An identical cast was studied by passing water through the cast, with pulses of dye to reveal flow, and cinephotography was used for determination of flow velocities and flow patterns. Flow rates adjusted on the basis of a Reynolds conversion showed good correlations between the two methods, whereas cinephotography revealed areas of turbulence and vortex-like flow not detected by thermistor probes. These results suggest that water flow may provide useful information in complex airways where airflow cannot be determined by other methods.     

Hydrodynamic advantages in the free‐living spiriferinide brachiopod Pachycyrtella omanensis: functional insight into adaptation to high‐energy flow environments

Immobile benthic organisms lacking attachment or cementation mechanisms are considered to be best adapted to quiet bottom environments. Since the free‐living Lower Permian spiriferinide brachiopod Pachycyrtella omanensis inhabited a sandy substrate with high‐energy water flow, flume experiments were performed to show the possible hydrodynamic advantages of shell morphology in postural stability and generation of feeding flows. Modelling indicates that a vertical position, with the commissure plane perpendicular to the seabed, was the most unstable, although it is considered to have been its original life position. On the other hand, the passive flow inside the model in vertical position exhibited vortex movement with constant degree of inhalent flow and exhalent flow, conferring advantages on the effective filtration of food particles using a spiral lophophore. The intensity and movement of the passive flow for feeding could have been adjusted through changes in the angle of opening of the valves. As the shoreface habitat was affected by oscillatory flows, a small‐sized animal could have undergone a high risk of burial, while an increase in size would have led to easier removal from the sandy bottom. To avoid both physical risks, Pachycyrtella developed a thick shell with a high rate of growth, specifically increasing the weight of the ventral umbo without altering its morphofunction to generate passive feeding flows. Biomechanics, functional morphology, opportunistic species, Pachycyrtella, Spiriferinida, suspension feeder.     

Optimization of poly(β-hydroxybutyric acid) recovery from Alcaligenes latus: combined mechanical and chemical treatments

Recovery of the intracellular bioplastic poly(β-hydroxybutyric acid) or PHB from fed-batch cultured Alcaligenes latus, ATCC 29713, was examined using combinations of chemical and mechanical treatments to disrupt the cells. Chemical pretreatments used sodium chloride and sodium hydroxide. For salt pretreatment the cells were exposed to NaCl (8?kg?m^?3) and heat (60?°C, 1 h), cooled to 4?°C, and mechanically disrupted. For alkaline treatments, the cells were exposed to sodium hydroxide (0.025–0.8 kg?NaOH per kg biomass) and mechanically disrupted at ambient temperature. A combined treatment with sodium chloride (8 kg m^?3), heat (60?°C, 1 h), and alkaline pH shock (pH 11.5, 1?min) was also tested. Mechanical disruption employed a continuous flow bead mill (2,800 rpm agitation speed, 90?ml?min^?1 slurry flow rate, 512 m mean bead diameter, bead loadings of 80% or 85% of chamber volume). Disruption was quantified by protein release. Over most of the disruption period, the release of PHB was approximately proportional to protein release. Regardless of the pretreatment or bead load, the disruption obeyed first order kinetics; hence, the rate of protein release was directly proportional to the amount of unreleased protein. Relative to untreated biomass, pretreatment always produced earlier protein release during milling. Pretreatment with a minimum of 0.12?kg NaOH per kg biomass was necessary to enable complete disruption within three passes (85% bead load). Untreated biomass required more than twice as many passes. Irrespective of the chemical pretreatment, the bead loading strongly influenced the disruption rate which was higher at the higher loading. Alkaline hydrolysis associated PHB loss was observed, but it could be limited to insignificant levels by immediate neutralization of disrupted homogenates.     

Prosthetic heart valves: waveform comparisons and average value disposition for pulsatile flow in vitro

With the development of the in vitro testing of heart valves, the standardization of the test methods becomes increasingly important and they should also be improved continuously. This paper discusses the problems of waveform comparison and average value dispositions. In the pulsatile model driven by pneumatics, the pressures before and after the valve, and the flow through it, are measured as three one-dimensional variates. The mean values are calculated according to the FDA and the ISO. A comparison and analysis of experimental waveforms indicate that, for basically the same ranges of pressures and flow rate, the flow curves of different types of valve are clearly different. The mean values and the waveforms in the time domain should be taken into consideration synthetically so that the pusatile characteristics of the valve can be more completely reflected. Using numerical filtering methods to treat the waveforms allows for better comparisons between the measured results taken from the different devices. By means of the constellation graphical method for treating mean values as multivariates, it is feasible to classify the valves and to judge their qualities under conditions of pulsatile flow.     

Cavitation phenomena in mechanical heart valves: the role of squeeze flow velocity and contact area on cavitation initiation between two impinging rods

In this study, the closing dynamics of two impinging rods were experimentally analyzed to simulate the cavitation phenomena associated with mechanical heart valve closure. The purpose of this study was to investigate the cavitation phenomena with respect to squeeze flow between two impinging surfaces and the parameter that influences cavitation inception. High-speed flow imaging was employed to visualize and identify regions of cavitation. The images obtained favored squeeze flow as an important mechanism in cavitation inception. A correlation study of the effects of impact velocities, contact areas and squeeze flow velocity on cavitation inception showed that increasing impact velocities results in an increase in the risk of cavitation. It was also shown that for similar impact velocities, regions near the point of impact were found to cavitate later for those with smaller contact areas. It was found that the decrease in contact areas and squeeze flow velocities would delay the onset and reduce the intensity of cavitation. It is also interesting to note that the squeeze flow velocity alone does not provide an indication if cavitation inception will occur. This is corroborated by the wide range of published critical squeeze flow velocity required for cavitation inception. It should be noted that the temporal acceleration of fluid, often neglected in the literature, can also play an important role on cavitation inception for unsteady flow phenomenon. This is especially true in mechanical heart valves, where for the same leaflet closing velocity, valves with a seat stop were observed to cavitate earlier. Based on these results, important inferences may be made to the design of mechanical heart valves with regards to cavitation inception.     

Local thermodilution: a reliable technique for estimating renal blood flow in the rabbit

1. A thermistor probe designed for determination of renal blood flow in rabbits, consisted of a fast-responding bead thermistor and an injection port which was also used to measure renal venous pressure between injections. 2. By an in vitro calibration system, actual measured flow (Qa) correlates well with the thermodilution calculated flow (Qc), where Qc = 0.99 Qa + 4.9 (r = 0.97, n = 42). 3. The renal blood flow (RBF) as determined by the thermodilution technique in 3 control groups was 53 +/- 3 (8), 60 +/- 6 (8), and 62 +/- 3 (3) ml/min/kidney or about 9% of the cardiac output. 4. Hypovolemia (-10%) reduced RBF by 19% from the control value, whereas, hypervolemia (+10%) did not alter RBF. 5. Smoke-induced apnea resulted in hypertension (+30%) and bradycardia (-39%), and was associated with changes in RBF (-55%) and renal vascular resistance (+183%). 6. We conclude that the local thermodilution technique is a relatively easy and reliable method for estimating RBF in rabbits.     

Giant scallop feeding and growth responses to flow

The relationship between ambient seawater flow velocity and growth of the giant scallop Placopecten magellanicus Gmelin is shown to be a reverse ramp function with growth inhibition at flow velocities of > 10–20 cm · s⁻¹. The mechanism of inhibition involves a reduction in ration as velocities around the scallop increase. In ambient flows which are sufficient to cause overloading of the scallop gill, the feeding/filtration rate is reduced by an unknown mechanism, possibly involving the mantle edge closing or a gill bypass mechanism operating. In ambient flows where the pressure at the exhalant opening exceeds the inhalant plus the pressure head created by the gill, as when the scallop is placed dorsal edge to the flow, the tendency for flow reversal is resisted by a similar mechanism involving a reduction in feeding/filtration rate.     

Volume flows and pressure changes during an action potential in cells ofChara australis

Summary Methods have been used for monitoring either volume flows or pressure changes, simultaneously with membrane potentials, in giant algal cells ofChara australis during an action potential. The volume flows were measured from the movement of a mercury bead in a capillary tube recorded by a photo-transducer. The pressure changes were measured by monitoring the deflection of a thin wedge, resting transversely across a cell, and using the same photo-transducer, the deflection of the wedge being directly related to the cell's turgor pressure. The average maximum rate of volume flow per unit area during an action potential was 0.88±0.11 nliter·sec^–1·cm^–2 in the direction of an outflow from the cell (total volume outflow being about 3 nliter·cm^–2 per action potential). Similarly, the maximum rate of change of pressure was 19.6±3.8×10^–3 atm·sec^–1 (peak change being 19.3±2.9×10^–3 atm equivalent to 14.7±2.2 mm Hg). The volume flow and pressure changes followed the vacuolar potential quite closely, the peak rate of volume flow lagging behind the peak of the action potential by 0.17±0.08 sec and the peak rate of pressure change leading it by 0.09±0.07 sec.     

Behaviour controls post-settlement dispersal by the juvenile bivalves Austrovenus stutchburyi and Macomona liliana

Post-settlement dispersal is a key process affecting the population dynamics of many soft sediment benthic invertebrates. Despite its importance, few studies have quantified those factors that influence juvenile dispersal. In a laboratory flume, we examined the effects of three flow velocities and two substrate types on the dispersal of two common intertidal bivalves: the deposit-feeding wedge shell Macomona liliana and the suspension-feeding cockle Austrovenus stutchburyi. Juveniles of three size classes (<2, 2-4 and 4-8 mm shell length) were added to cores of defaunated natural sediment or glass beads. We recorded the number of bivalves remaining in cores versus those recovered downstream either on the flume floor, in bedload traps or in a plankton net at the end of the working section of the flume after 48 h at three freestream velocities (4.8, 11.0 and 16.6 cm s⁻¹). At flow speeds of 4.8 cm s⁻¹, <5% of individuals were recovered outside the cores for both species. At higher flows, the dispersal mode (crawling, bedload or in suspension) and frequency of dispersal differed markedly between species. Austrovenus dispersed primarily by crawling in the low flow treatments. The frequency of dispersal increased substantially (2-6×) between 11.0 and 16.6 cm s⁻¹, and most Austrovenus were found in bedload traps at the highest flow. At the highest flow, twice as many Austrovenus individuals left the glass bead treatment as from the natural sediment. The number of dispersing Macomona also increased with increasing flow from the natural sediment, but numbers dispersing from glass beads were similar for the two higher flows (11.0 and 16.6 cm s⁻¹). Macomona dispersal mode was associated with size; smaller size classes were collected in the bedload traps and the plankton net in approximately equal proportions, while only a small proportion of the largest size class were collected in the plankton net. In contrast to flume dispersal experiments with live bivalves, most dead Austrovenus did not move at the highest flow speed, while most dead Macomona were transported at the highest flow speed. The live-dead comparisons, in conjunction with our primary experimental results, imply that there are active behavioural components to both water column and bedload transport. Our research emphasises that both species actively influence post-settlement transport in response to both substrate type and flow regime, and that bedload transport, often categorised as a passive transport process, is also greatly influenced by active behavioural processes.     

Experiences with a 20 litre industrial bead mill for the disruption of microorganisms

Suspensions of several yeast strains and bacterial species were disrupted in a continuously operating industrial agitator mill of 22.7 litre internal working volume. The influence of agitator speed, flow rate, concentration of microorganisms in the slurry, packing density of glass beads and bead diameter on the disruption process was studied using baker's yeast (Saccharomyces cerevisiae). Cell disintegration was followed by assaying the appearance of protein and the activities of d-glucose-6-phosphate dehydrogenase [d-glucose-6-phosphate:NADP⁺ oxidoreductase, EC 1.1.1.49] and α-d-glucosidase [α-d-glucoside glucohydrolase, EC 3.2.1.20] in the soluble fraction. The best operating conditions for the disintegration of baker's yeast with respect to activity yield appeared to be at a rotational speed of 1100 rev/min, a flow rate of 100 litre h^?1 and a cell concentration of 40% (w/v). The location of the desired enzyme in the cell is of importance for the choice of bead diameter and packing density of the glass beads. Temperature increase and power consumption during disintegration are also strongly influenced by the bead loading in the mill. With optimized parameters, 200 kg baker's yeast can be processed per hour with a degree of disintegration >85%. The disruption process in the mill was found to be very effective for several yeast species tested, e.g. Saccharomyces cerevisiae, Saccharomyces carlsbergensis, and Candida boidinii. The usefulness of the Netzsch LME 20-mill for the disruption of bacteria species was demonstrated with Escherichia coli, Brevibacterium ammoniagenes, Bacillus sphaericus and Lactobacillus confusus. As expected, the mill capacity for bacterial disruption was significantly smaller than for the yeast. Between 10 and 20 kg per h bacteria may be processed, depending on the organism.     

A horizontal bioreactor for ethanol production by immobilized cells

The one-parameter-tanks-in-series model was found to be an adequate model for the characterization of flow dynamics in a horizontal immobilized cell reactor, when blue dextran was used as tracer. Isobutanol proved to be inadequate, because it diffused inside the beads and thus caused tailing in RTD. The CO₂ evolution rate displayed the most pronounced effect on axial liquid dispersion. At high CO₂ production rates and low dilution rates each stage of the reactor behaved like a well-mixed reactor. At lower CO₂ evolution rates the number of tanks (N) related to the reactor increased up to 10. The medium flow rate affects axial dispersion to a minor degree. An increase of the dilution rate from 0.328 to 1.34 h^?1 resulted in a slight rise of N from 3.5 to 5 at high CO₂ production and from 4 to 7 at medium CO₂ production rates. Variation in the bead hold up showed the same characteristic axial mixing behavior as reflected by changing the medium flow rate. The quantitative correlation between axial mixing and the most significant fermentation parameters (dilution rate, CO₂ evolution rate and bead hold up) allow to develop an overall model, which besides kinetic expressions also contains terms related to the flow dynamics of the reactor. In the third part of this communication such a model will be presented and compared with actual fermentation data.     

An integrated laser trap/flow control video microscope for the study of single biomolecules

We have developed an integrated laser trap/flow control video microscope for mechanical manipulation of single biopolymers. The instrument is automated to maximize experimental throughput. A single-beam optical trap capable of trapping micron-scale polystyrene beads in the middle of a 200-microm-deep microchamber is used, making it possible to insert a micropipette inside this chamber to hold a second bead by suction. Together, these beads function as easily exchangeable surfaces between which macromolecules of interest can be attached. A computer-controlled flow system is used to exchange the liquid in the chamber and to establish a flow rate with high precision. The flow and the optical trap can be used to exert forces on the beads, the displacements of which can be measured either by video microscopy or by laser deflection. To test the performance of this instrument, individual biotinylated DNA molecules were assembled between two streptavidin beads, and the DNA elasticity was characterized using both laser trap and flow forces. DNA extension under varying forces was measured by video microscopy. The combination of the flow system and video microscopy is a versatile design that is particularly useful for the study of systems susceptible to laser-induced damage. This capability was demonstrated by following the translocation of transcribing RNA polymerase up to 650 s.     

Biodegradation of Methyl Orange by alginate-immobilized Aeromonas sp. in a packed bed reactor: external mass transfer modeling

Azo dyes are recalcitrant and xenobiotic nature makes these compounds a challenging task for continuous biodegradation up to satisfactorily levels in large-scale. In the present report, the biodegradation efficiency of alginate immobilized indigenous Aeromonas sp. MNK1 on Methyl Orange (MO) in a packed bed reactor was explored. The experimental results were used to determine the external mass transfer model. Complete MO degradation and COD removal were observed at 0.20 cm bead size and 120 ml/h flow rate at 300 mg/l of initial dye concentration. The degradation of MO decreased with increasing bead sizes and flow rates, which may be attributed to the decrease in surface of the beads and higher flux of MO, respectively. The experimental rate constants (k _ps) for various beads sizes and flow rates were calculated and compared with theoretically obtained rate constants using external film diffusion models. From the experimental data, the external mass transfer effect was correlated with a model J _D = K Re ^?(1 ? n). The model was tested with K value (5.7) and the Colburn factor correlation model for 0.20, 0.40 and 0.60 bead sizes were J _D = 5.7 Re ^?0.15, J _D = 5.7 Re ^?0.36 and J _D = 5.7 Re ^?0.48, respectively. Based on the results, the Colburn factor correlation models were found to predict the experimental data accurately. The proposed model was constructive to design and direct industrial applications in packed bed reactors within acceptable limits.     

鲢幼鱼在不同水流速度下的暴发-滑行行为策略

在水温（18±1）℃的条件下,以全长（11.70±0.57）cm的鲢（Hypophthalmichthys molitrix）幼鱼为研究对象,测定其不同流速（16.5、22.0、27.5、33.0、38.5、44.0、49.5和55.0 cm/s）下的持续游泳时间、调头百分比和暴发-滑行运动数据。结果表明,鲢的平均持续游泳时间先随流速的增加而减小,后随流速的增加而增加。当流速33.0 cm/s时,平均持续时间最短为118.6min,其中各组试验鱼的最大可持续游泳时间均可达到200min。调头百分比随流速的增加迅速减小,当流速≥44.0 cm/s时,不再出现调头行为。暴发-滑行游泳的平均暴发时间随流速的增加呈上升趋势（y=0.03x+2.64,R2=0.92,P<0.05）。平均对地暴发距离均在30-45 cm,没有显著性差异（P>0.05）,平均绝对暴发距离存在极显著性差异,且随流速的增加而增加（y=4.98x-5.63,R2=0.98,P<0.001）。平均对地暴发速度没有显著性差异（平均对地平均速度和最大速度分别在9-12 cm/s、12-16 cm/s,P>0.05）。平均绝对暴发速度与水流速度之间存在线性正相关关系（平均绝对平均暴发速度:y=0.98x+10.74,R2=1.00,P<0.001;平均绝对最大暴发速度:y=1.02x+13.75,R2=0.99,P<0.001）。研究表明鲢在不同的流速下采取的暴发-滑行行为策略不同。     

基于物理模型实验的光倒刺鲃生态行为学研究

建立了基于天然河道的物理模型,通过控制实验研究水环境因子对鱼类行为的影响。文中选取了金沙江下游2.6 km河段建立物理模型,以南方水系的经济鱼类光倒刺鲃为研究对象,进行了鱼的行为对底质和流速的响应实验。分析得出,光倒刺鲃对砂卵石底质的选择明显大于其它底质且差异极其显著(P<0.01),光倒刺鲃2龄幼鱼期的喜好流速范围为0.3-0.6 m/s;研究同时发现水流紊动强度对光倒刺鲃行为具有重要影响。该研究结果可以为光倒刺鲃栖息地模型提供参考。     

A thermistor leaf thermometer

An instrument is described which allows measurements of leaf temperature within about 0.3 C. It consists of a special thermistor probe, a small circuit box, and a standard ammeter. The circuit box can easily be fixed to the meter and contains a battery, which passes 0.3 milliampere through the thermistor, and also contains an integrated circuit amplifier, so that the meter reads 20 C full scale deflection, with ranges adjustable in 10 C steps. Calibration experiments show the superiority of the thermistor leaf thermometer to a thermocouple pressed onto a rubber surface with a resilience resembling that of a leaf.     

Electrical signs of impulse conduction in spinal motoneurons

An analysis has been made of the electrical responses recorded on the surface and within the substance of the first sacral spinal segment when the contained motoneurons are excited by single and repeated antidromic ventral root volleys. A succession of negative deflections, designated in order of increasing latency m, i, b, d, has been found. Each of those deflections possesses some physiological property or properties to distinguish it from the remainder. Indicated by that fact is the conclusion that the successive deflections represent impulse conduction through successive parts of the motoneurons that differ in behavior, each from the others. Since the spinal cord constitutes a volume conductor the negative deflections are anteceded by a positive deflection at all points except that at which the axonal impulses first enter from the ventral root into the spinal cord. Frequently two or more negative deflections are recorded together in overlapping sequence, but for each deflection a region can be found in which the onset of that deflection marks the transition from prodromal positivity to negativity. Deflection m is characteristic of axonal spikes. Latent period is in keeping with known axonal conduction velocity. Refractory period is brief. The response represented by m is highly resistant to asphyxia. Maximal along the line of ventral root attachment and attenuating sharply therefrom, deflection m can be attributed only to axonal impulse conduction. Deflection i is encountered only within the cord, and is always associated with a deflection b. The i,b complex is recordable at loci immediately dorsal to regions from which m is recorded, and immediately ventral to points from which b is recorded in isolation from i. Except for its great sensitivity to asphyxia, deflection i has properties in common with those of m, but very different from those of b or d. To judge by properties i represents continuing axonal impulse conduction into a region, however, that is readily depolarized by asphyxia. Deflection b possesses a unique configuration in that the ascending limb is sloped progressively to the right indicating a sharp decrease in velocity of the antidromic impulses penetrating the b segment. A second antidromic volley will not conduct from i segment to b segment of the motoneurons unless separated from the first by nearly 1 msec. longer than is necessary for restimulation of axons. This value accords with somatic refractoriness determined by other means. Together with spatial considerations, the fact suggests that b represents antidromic invasion of cell bodies. Deflection d is ubiquitous, but in recordings from regions dorsal and lateral to the ventral horn, wherein an electrode is close to dendrites, but remote from other segments of motoneurons, d is the initial negative deflection. In latency d is variable to a degree that demands that it represent slow conduction through rather elongated structures. When associated with deflection b, deflection d may arise from the peak of b with the only notable discontinuity provided by the characteristically sloped rising phase of b. Deflection d records the occupation by antidromic impulses of the dendrites. Once dendrites have conducted a volley they will not again do so fully for some 120 msec. Embracing the several deflections, recorded impulse negativity in the motoneurons may endure for nearly 5 msec. When the axonal deflection m is recorded with minimal interference from somatic currents, it is followed by a reversal of sign to positivity that endures as long as impulse negativity can be traced elsewhere, demonstrating the existence of current flow from axons to somata as the latter are occupied by impulses. Note is taken of the fact that impulse conduction through motoneurons is followed by an interval, measurable to some 120 msec., during which after-currents flow. These currents denote the existence in parts of the intramedullary motoneurons of after-potentials the courses of which must differ in different parts of the neurons, otherwise nothing would be recorded. The location of sources and sinks is such as to indicate that a major fraction of the current flows between axons and somata. For approximately 45 msec. the direction of flow is from dendrites to axons. Thereafter, and for the remaining measurable duration, flow is from axons to dendrites.