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101.
Hein Jürgen Brede 《Zeitschrift für Physik A Hadrons and Nuclei》1972,254(4):375-384
The reactions32S(n, α)29Si and40Ca(n, α)37Ar were studied with 13.9 MeV neutrons using two different counter telescopes. Absolute differential cross sections were measured for the transitions to the ground states of29Si and37Ar and to the 1.27+2.03+2.42 MeV levels of29Si. The angular distribution of the ground states interpreted in terms of a simple pick-up-reaction-model were compared with a DWBA-calculation using the code DWUCK. 相似文献
102.
High-density carriers were produced in germanium using the fundamental (1.06 μm) and second harmonic (0.53 μm) output of a Q-switched glass:Nd3+ laser. Differences in the plasma reflectivity at 10.6 μm are attributed to different amounts of lattice heating. In particular, the more substantial damping of the plasma resonance associated with the 0.53 μm excitation is attributed to a higher electron-phonon collision frequency. The results are discussed with respect to diagnostics of photogenerated semiconductor plasmas and the effeciency of semiconductor switches. 相似文献
103.
104.
.Prof. Dr. Ing. D. Hein .Dipl.-Ing. W. Kastner .Dipl.-Ing. W. Köhler .Dipl.-Ing. W. Krätzer 《Heat and Mass Transfer》1982,16(4):251-257
Zusammenfassung Werden in einem beheizten Verdampferrohr die Randbedingungen so geändert, daß sich der Ort der Siedekrise in Strömungsrichtung verschiebt, so kann dies vorübergehend zu einer starken Reduktion des Wärmeübergangskoeffizienten im Post-Dryout-Gebiet führen. Es werden die an einem Hochdruckkreislauf gewonnenen zeitlichen Verläufe der Wandtemperaturen analysiert, wie sie bei Absenkung des System-druckes bzw. der Enthalpie der Strömung am Eintritt in das Versuchsrohr auftreten. Anhand der Siedekurve werden die beobachteten Wandtemperaturverläufe interpretiert. Durch Nachrechnung der Experimente mit einem dynamischen Rechen-programm lassen sich die unterschiedlichen Effekte, die während der Transiente auftreten, separieren.
Formelzeichen h Sättigungsenthalpie des Wassers - p Druck - p c kritischer Druck - Q Wärmestrom - q Wärmestromdichte - q1, q2 Wärmestromdichte für Rohrabschnitt l bzw. 2 - t Zeit - x wirklicher Dampfmassenanteil - ¯x bilanzmäßiger Dampfmassenanteil Herrn Prof. Dr.-Ing. U. Grigull zum 70. Geburtstag gewidmet 相似文献
Heat transfer in post-dryout region during transients
A change in the boundary conditions in a heated evaporator tube (moving the location of the boiling crisis downstream) could lead to a strong reduction in the heat transfer coefficient in the Post-Dryout region. The analyzed wall temperature data were obtained in a high pressure test loop by reducing the system pressure, or the enthalpy at the test section inlet. The wall temperature time histories were interpreted using the boiling curve. The various effects occurring during the transient could be separated by recalculating the tests with a dynamic simulation computer program.
Formelzeichen h Sättigungsenthalpie des Wassers - p Druck - p c kritischer Druck - Q Wärmestrom - q Wärmestromdichte - q1, q2 Wärmestromdichte für Rohrabschnitt l bzw. 2 - t Zeit - x wirklicher Dampfmassenanteil - ¯x bilanzmäßiger Dampfmassenanteil Herrn Prof. Dr.-Ing. U. Grigull zum 70. Geburtstag gewidmet 相似文献
105.
106.
Paul R. Hein 《Journal of polymer science. Part A, Polymer chemistry》1973,11(1):163-173
A ziegler-type catalyst system consisting of tungsten hexachloride and alkyl or aryl tin compounds was found to polymerize cyclopentene and other cyclic olefins through a ring-opening mechanism. This catalyst system also polymerized α-olefins such as ethylene and 1-octene. An attempt was made to copolymerize cyclopentene and ethylene. Other catalyst systems were also employed for ring-opening polymerizations with limited success. 相似文献
107.
108.
M.S. Hundal 《Journal of sound and vibration》1976,48(2):189-193
The performance of an impact absorber with a linear spring and a quadratic law damper is analyzed. The equation of motion is non-dimensionalized and a closed form solution is obtained. Chosen response variables are presented in terms of a dimensionless parameter, the quadratic damping ratio. The performance is compared with that of an absorber with viscous damper. 相似文献
109.
110.
Dr. J. C. Hein 《Heat and Mass Transfer》1984,18(2):61-67
Analytical solutions for the heat conduction in a plane wall with periodic temperature variations at the wall surface are presented. Series and asymptotic developments of these solutions are deduced. The results are important for the calculation of the heat transfer in rotary kilns or other rotaring units.
Nomenclature a 2 =/ C m2/s thermal diffusivity, Eq. (1) - C J/kg K specific heat - F K initial temperature of the wall, Eq. (4) - F m2 surface of the wall - G Green's function, Eq. (10) - G1 Green's function, Eq. (12) - h m thickness of the wall - H Heaviside function, Eq. (5) - k constant, Eq. (25) - k x constant, Eq. (25) - Q J total energy, Eq. (17) - Q u J total energy from temperatureU, Eq. (18) - Q v J total energy from temperatureV, Eq. (19) - s s–1 Laplace variable - t s time - t 1 s heating time, Eq. (5) - t 2 s period, Eq. (5) - T K temperature of the wall - T i K surface temperature of the wall - T 1 K surface temperature of the wall during the heating time - T 2 K surface temperature of the wall during the cooling time - U K temperature of the wall defined in problem 1 - V, K temperature of the wall defined in problem 2 - x m coordinate - 0 W/m2K overall heat transfer coefficient, Eq. (31) - 10 W/m2 K overall heat transfer coefficient, Eq. (32) - 20 W/m2 K overall heat transfer coefficient, Eq. (33) - Dirac Delta function - s–1/2 parameter, Eq. (6) - W/mK thermal conductivity - kg/m3 specific mass - dimensionless time, Eq. (34) - Riemann Zeta function surfix Laplace transformed variable 相似文献
Die Wärmeleitung in einer ebenen Wand mit periodischen Temperaturänderungen
Zusammenfassung Es werden analytische Lösungen für die Wärmeleitung in einer ebenen Wand mit periodischen Temperaturänderungen an ihrer Oberfläche mitgeteilt. Reihen- und asymptotische Entwicklungen dieser Lösungen werden abgeleitet. Die Ergebnisse sind wichtig für die Berechnung des Wärmetransportes in Drehrohröfen oder ähnlichen Maschinen.
Nomenclature a 2 =/ C m2/s thermal diffusivity, Eq. (1) - C J/kg K specific heat - F K initial temperature of the wall, Eq. (4) - F m2 surface of the wall - G Green's function, Eq. (10) - G1 Green's function, Eq. (12) - h m thickness of the wall - H Heaviside function, Eq. (5) - k constant, Eq. (25) - k x constant, Eq. (25) - Q J total energy, Eq. (17) - Q u J total energy from temperatureU, Eq. (18) - Q v J total energy from temperatureV, Eq. (19) - s s–1 Laplace variable - t s time - t 1 s heating time, Eq. (5) - t 2 s period, Eq. (5) - T K temperature of the wall - T i K surface temperature of the wall - T 1 K surface temperature of the wall during the heating time - T 2 K surface temperature of the wall during the cooling time - U K temperature of the wall defined in problem 1 - V, K temperature of the wall defined in problem 2 - x m coordinate - 0 W/m2K overall heat transfer coefficient, Eq. (31) - 10 W/m2 K overall heat transfer coefficient, Eq. (32) - 20 W/m2 K overall heat transfer coefficient, Eq. (33) - Dirac Delta function - s–1/2 parameter, Eq. (6) - W/mK thermal conductivity - kg/m3 specific mass - dimensionless time, Eq. (34) - Riemann Zeta function surfix Laplace transformed variable 相似文献