Convective heat transfer characteristics of toothed leaves

Summary Model leaves were used to test the hypothesis that serrate leaves have more convective heat loss than entire leaves of the same average size. Convection coefficients were positively correlated with size of teeth, supporting the hypothesis. Experimental results were in close agreement with theoretical predictions, which assumed an inverse correlation between depth of serration and effective leaf dimension.Abbreviations A total surface area of model (cm²) - D characteristic dimension of model (cm) - h convection coefficient (cal cm^-2 min^{-1 o}K^-1) - I radiant energy flux (cal cm^-2 min^-1) - Q radiant energy absorbed by leaf (cal min^-1) - q_c convective heat transfer (cal min^-1) - q_e evaporative heat loss (cal min^-1) - q_k conductive heat loss (cal min^-1) - q_r radiative heat loss (cal min^-1) - T_a air temperature (^oK) - T₁ model temperature (^oK) - V wind speed (m s^-1) - emissivity - Stefan-Boltzmann constant (8.130x10^-11 cal min^-1 cm^{-2 o}K^-4)     

Uptake and transfer factors of137Cs by mushrooms

Summary The¹³⁷Cs content of 118 species (668 samples) of higher fungi collected in the period from August 1984 to October 1989 at three different locations in Styria, Austria, was determined by gamma-spectrometry. The Cs-content of most mushrooms has been increasing since September 1986. In order to find out which factors determine the¹³⁷Cs-contamination of mushrooms and the transfer-value soil to mushroom, the concentration of total and plant-available radiocesium in soils as well as the pH-value, the content of humus, clay, silt, sand, exchangeable cations, the composition of the clay minerals, and the particle size distribution of the soils of two different locations were examined. The higher the¹³⁷Cs contamination of the soil, the thicker the layer of humus and the higher the content of humus, the lower the pH-value, and the lower the amount of essential cations, especially of K⁺, the higher the amount of¹³⁷Cs plant-available will be. Therefore, the contamination of the mushrooms in the coniferous forest of Koralpenblick (1000 m) is higher than in the mixed forest at the Rosenberg around Graz at approx. 500 m height. Of 26 different species of mushrooms measured at both sites, only 61% show the highest TF-values soil to mushrooms also at the Koralpenblick. In the spruce forest at Koralpenblick there are many species of mushrooms with high¹³⁷Cs-contamination which were not found at the Rosenberg. However, the properties of the species to which a mushroom belongs are more important than environmental conditions and soil properties. The transfer values of⁴⁰K stay within narrow bounds, whereas those of¹³⁷Cs differ widely.Dedicated to Prof. Dr. Otto Härtel on the occasion of his 80th birthday     

Compatibility between F-like genetic transfer factors

A study has been made of compatibility among four F-like factors of genetic transfer (pAP22-4, pAP38, pAP39 and pAP41) labeled separately by transpozones Tn1 and Tn9. It has been established that pAP38 transfer factor is compatible with plasmids pAP22-4, pAP39 and pAP412, while pAP41 transfer factor is compatible with plasmids pAP22-4 and pAP38 but is incompatible with plasmid pAP39.     

Oxygen transfer and culture characteristics of self-immobilized Solanum aviculare aggregates

Oxygen transfer characteristics of self-immobilized Solanum aviculare cells were measured using aggregates 3.0 to 12.5 mm in diameter. Apparent specific oxygen uptake rates in the absence of external boundary layers varied from 5.9 x 10(-11) to 8.5 x 10(-7) kg kg(-1) s(-1) dry weight, but did not decline continuously with increasing particle size. The effective diffusivity of oxygen in deactivated aggregates increased with particle diameter, varying from 5.0 x 10(-11) to 1.0 x 10(-9) m(2) s(-1) or between 2% and 40% of the molecular diffusivity in water at the same temperature. Gas spaces detected in the larger aggregates were confined to the central core and were not distributed throughout the tissue to facilitate oxygen transfer. Oxygen consumption rates in the absence of diffusional limitations were estimated using the relationship between the observable Thiele modulus and effectiveness factor for zero-order reaction. The calculated results indicated severe oxygen limitations in the aggregates, but were inconsistent with the observation that relatively large S. aviculare aggregates contained a high fraction of viable cells and were capable ofactive growth and steroidal alkaloid synthesis. This work suggests that oxygen delivery is facilitated in living plant cell aggregates by mechanisms which depend on metabolic activity and which do not function in deactivated cells. (c) 1995 John Wiley & Sons Inc.     

Gas transfer characteristics of a novel membrane bioreactor

We show the design features of a membrane bioreactor based on pulsatile flow across dimpled membranes. Results show an enhanced mass transfer of air of at least five-fold magnitude as compared with flat membranes. An increased working volume form 20 mL to 120 mL reduced the k(L)A at a given Reynolds number because of axial mixing of fluid from the deoxygenated end chamber. The bioreactor was used to supply air to a hybridoma mammalian cell line, and the calculated oxygen uptake showed that high-density cultures could be maintained in a 20mL, single-dimpled cultures could be maintained in a 20 mL, single-dimpled membrane system. Indirect aeration of a 2 L continuous stirred tank reactor, by a double-membrane system, showed that air could be supplied to mammalian cells at cell densities of approximately 4 x 10(6) /mL.     

Mass transfer characteristics of hydrophobic tubing membrane sensors

Summary The total resistance to transfer through a hydrophobic membrane used in the tubing method is due to an external liquid film and to the membrane itself. The global mass transfer coefficient is higher for alcohols than for other tested volatiles. PTFE microporous membranes are recommended.     

Odorant transfer characteristics of white bread during baking

The potent odorants in the crust and crumb of white bread were identified and quantified by gas chromatography-mass spectrometry and gas chromatography/olfactometry. The weight loss ratio of the samples baked at 220 °C was controlled in the range of 0-28%. The odorants were classified into 5 types by the transfer characteristics: i) All amounts of odorant transferred from the crust to external space (type-I). ii) All transferred from the crust to the crumb and external space (type-II). iii) Certain amount remaining in the crust and the rest transferred to the crumb and external space (type-III). iv) All transferred from the crumb to external space (type-IV). v) Certain amount remaining in the crumb and the rest transferred to the crust and external space (type-V). The odorants of type-IV were not apparent after the crust had formed. The results indicate that the crust could be a barrier to prevent the odorants from being transferred to external space.     

Visual transfer characteristics from Mach band measurements

Whenever the eye views a spatially-varying gradient of luminance, the Mach bands arise, causing a subjective distribution different from the luminance distribution of the field of view. This phenomenon has been used for the determination of the contrast-transfer function of the visual system when working under normal viewing conditions, i.e., operating in a region where both luminance and detail size are well above threshold. The Mach bands have been measured by making subjective photometric comparisons and the data have been analyzed under the assumption of linearity of response to input. The hypothesis that the visual system may be treated as an approximately linear link in the imaging chain is satisfied best when the luminances are plotted logarithmically. The possibility of this type of investigation is discussed. The result found is compared with apparent subjective contrast measurements of a sine-wave spatial luminance distribution.     

Location and characteristics of the transfer region of a Bacteroides conjugative transposon and regulation of transfer genes.

Many Bacteroides clinical isolates contain large conjugative transposons, which excise from the genome of a donor and transfer themselves to a recipient by a process that requires cell-to-cell contact. It has been suggested that the transfer intermediate of the conjugative transposons is a covalently closed circle, which is transferred by the same type of rolling circle mechanism used by conjugative plasmids, but the transfer origin of a conjugative transposon has not previously been localized and characterized. We have now identified the transfer origin (oriT) region of one of the Bacteroides conjugative transposons, TcrEmr DOT, and have shown that it is located near the middle of the conjugative transposon. We have also identified a 16-kbp region of the conjugal transposon which is necessary and sufficient for conjugal transfer of the element and which is located near the oriT. This same region proved to be sufficient for mobilization of coresident plasmids and unlinked integrated elements as well as for self-transfer, indicating that all of these activities are mediated by the same transfer system. Previously, we had reported that disruption of a gene, rteC, abolished self-transfer of the element. rteC is one of a set of rte genes that appears to mediate tetracycline induction of transfer activities of the conjugative transposons. On the basis of these and other data, we had proposed that RteC activated expression of transfer genes. We have now found, however, that when the transfer region of TcrEmr DOT was cloned as a plasmid that did not contain rteC and the plasmid (pLYL72) was tested for transfer out of a Bacteroides strain that did not have a copy of rteC in the chromosome, the plasmid was self-transmissible without tetracycline induction. This and other findings suggest that RteC is not an activator transfer genes but is stimulating transfer in some other way.     

Fertility regulation in F-like resistance transfer factors

Mutants of the R factor R100 have been isolated that mediate high-frequency transfer of the R factor during conjugation. Complementation tests revealed two classes of mutants, operator-constitutive and repressor-negative. Some of the latter class were suppressible by amber and ochre suppressors. The results support a simple model of regulation for the control of R-factor-mediated piliation.     

Hydrodynamic and mass transfer characteristics of three-phase gaslift bioreactor systems.

This review focuses on the hydrodynamic and mass transfer characteristics of various three-phase, gaslift fluidized bioreactors. The factors affecting the mixing and volumetric mass transfer coefficient (k(L)a), such as liquid properties, solid particle properties, liquid circulation velocity, superficial gas velocity, bioreactor geometry, are reviewed and discussed. Measurement methods, modeling and empirical correlations are reviewed and compared. To the authors' knowledge, there is no 'generalized' correlation to calculate the volumetric mass transfer coefficient, instead, only 'type-specific' correlations are available in the literature. This is due to the difficulty in modeling the gaslift bioreactor, caused by the variation in geometry, fluid dynamics, and phase interactions. The most important design parameters reported in the literature are: gas hold-up, liquid circulation velocity, 'true' superficial gas velocity, mixing, shear rate, aeration rate and volumetric mass transfer coefficient, k(L)a.     

Production and mass transfer characteristics of non-Newtonian biopolymers for biomedical applications

The market for microbial biopolymers is currently expanding to include several emerging biomedical applications. Specifically, these applications are drug delivery and wound healing. A fundamental understanding of the key fermentation parameters is necessary in order to optimize the production of these biopolymers. Considering that most microbial biopolymer systems exhibit non-Newtonian rheology, oxygen mass transfer can be an important parameter to optimize and control. In this article, we present a critical review of recent advances in rheological and mass transfer characteristics of selected biopolymers of commercial interest in biomedical applications.     

Dimensionless solutions and general characteristics of bioheat transfer during thermal therapy

The derivation and application of the general characteristics of bioheat transfer for medical applications are shown in this paper. Two general bioheat transfer characteristics are derived from solutions of one-dimensional Pennes’ bioheat transfer equation: steady-state thermal penetration depth, which is the deepest depth where the heat effect reaches; and time to reach steady-state, which represents the amount of time necessary for temperature distribution to converge to a steady-state. All results are described by dimensionless form; therefore, these results provide information on temperature distribution in biological tissue for various thermal therapies by transforming to dimension form.