976 resultados para Steam-pipes
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Receipt from Rolph Smith Lithographers by Steam Power and Co. of Toronto for a name plate, Aug. 23, 1886.
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Receipt from John Burrow, Steam and Gas Fitter and Plumber, St. Catharines for work done, March 31, 1887.
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Receipt from Chatfield and Neelon, St. Catharines for various fittings and pipes, May 13, 1887.
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Receipt from George Lloyd, dealer in stoves and ranges, St. Catharines for range and pipes, July 1, 1887.
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Flyer for the Georgian Bay, Ontario Steam Show, 1983.
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Broadside, 47 cm. x 31 cm. with a coloured picture of a case engine and tender [steam engine] printed by Meyer-Rotier of Milwaukee. On the back is a sketch of a building. This has a stamp on the back which indicates that this is an exhibit in the High Court of Justice in Coburg in the case of Bigelow vs. Powers et al. This item has been torn down the middle and taped. This does not affect the text nor picture, Oct. 11, 1909.
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UANL
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UANL
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UANL
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Este libro es la presentación de un programa de la FAD: el PIPES o Plan Integral de Prevención Escolar. Se trata de un plan general de intervención educativo-escolar para la prevención del consumo de drogas que intenta, a través de la implicación y el compromiso de la comunidad escolar, poner en marcha programas preventivos dirigidos a los alumn@s, con la finalidad de que consigan estilos de vida más saludables y sean capaces de manejar mejor las presiones hacia los consumos. Es un programa integral, abierto y flexible que expone numerosas estrategias debido al amplio abanico de destinatarios: toda la comunidad escolar.
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AEA Technology has provided an assessment of the probability of α-mode containment failure for the Sizewell B PWR. After a preliminary review of the methodologies available it was decided to use the probabilistic approach described in the paper, based on an extension of the methodology developed by Theofanous et al. (Nucl. Sci. Eng. 97 (1987) 259–325). The input to the assessment is 12 probability distributions; the bases for the quantification of these distributions are discussed. The α-mode assessment performed for the Sizewell B PWR has demonstrated the practicality of the event-tree method with input data represented by probability distributions. The assessment itself has drawn attention to a number of topics, which may be plant and sequence dependent, and has indicated the importance of melt relocation scenarios. The α-mode failure probability following an accident that leads to core melt relocation to the lower head for the Sizewell B PWR has been assessed as a few parts in 10 000, on the basis of current information. This assessment has been the first to consider elevated pressures (6 MPa and 15 MPa) besides atmospheric pressure, but the results suggest only a modest sensitivity to system pressure.
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A neural network was used to map three PID operating regions for a two-input two-output steam generator system. The network was used in stand alone feedforward operation to control the whole operating range of the process, after being trained from the PID controllers corresponding to each control region. The network inputs are the plant error signals, their integral, their derivative and a 4-error delay train.
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Rheology of milk foams generated by steam injection was studied during the transient destabilization process using steady flow and dynamic oscillatory techniques: yield stress (τ_y) values were obtained from a stress ramp (0.2 to 25 Pa) and from strain amplitude sweep (0.001 to 3 at 1 Hz of frequency); elastic (G') and viscous (G") moduli were measured by frequency sweep (0.1 to 150 Hz at 0.05 of strain); and the apparent viscosity (η_a) was obtained from the flow curves generated from the stress ramp. The effect of plate roughness and the sweep time on τ_y was also assessed. Yield stress was found to increase with plate roughness whereas it decreased with the sweep time. The values of yield stress and moduli—G' and G"—increased during foam destabilization as a consequence of the changes in foam properties, especially the gas volume fraction, φ, and bubble size, R_32 (Sauter mean bubble radius). Thus, a relationship between τ_y, φ, R_32, and σ (surface tension) was established. The changes in the apparent viscosity, η, showed that the foams behaved like a shear thinning fluid beyond the yield point, fitting the modified Cross model with the relaxation time parameter (λ) also depending on the gas volume fraction. Overall, it was concluded that the viscoelastic behavior of the foam below the yield point and liquid-like behavior thereafter both vary during destabilization due to changes in the foam characteristics.