| 摘要 |
<p>An ensemble of acoustic steelpan musical instruments, being an innovation which significantly improves upon traditional acoustic steelpan prior art. Said improvements include an extension of note range across the assemblage of G-Pans, a substantial reduction in the number of steelpans required to effectively cover the steelpan musical range, the use of a compound design whereby individual component parts of the instrument, specifically the playing surface, chime, rear attachment, or skirt and the playing stick or mallet, are optimized for thier specific function, the application of a variety of techniques for eliminating or reducing, non-musical sympathetic vibrations and the inclusion of a variety of mechanical and acoustic resonator designs, to enhance optimally, the sound projection of the aforementioned instrument. An ensemble of acoustic steelpan musical instruments, being an innovation which significantly improves upon traditional acoustic steelpan prior art. Said improvements include an extension of note range across the assemblage of G-Pans, a substantial reduction in the number of steelpans required to effectively cover the steelpan musical range, the use of a compound design whereby individual component parts of the instrument, specifically the playing surface, chime, rear attachment, or skirt and the playing stick or mallet, are optimized for thier specific function, the application of a variety of techniques for eliminating or reducing, non-musical sympathetic vibrations and the inclusion of a variety of mechanical and acoustic resonator designs, to enhance optimally, the sound projection of the aforementioned instrument. The invention concerns a method of diphenylamine production from aniline by a continuous procedure in liquid phase catalysed by thermolabile compounds of fluorine with boron which convert under conditions of diphenylamine formation from aniline to NH4BF4. NH4BF4 crystals arising in the reaction medium of the reactor are maintained in uplift during a time,which is at least so long as the dwell time of aniline in the reactor. The maintaining in uplift is ensured by circulation stirring of the reaction mixture with a stirrer of minimum volume-rate of 0.1-multiple ofthe reaction mixture volume per hourand it is realized by mechanical stirring providing turbulent axial-radial flow of the reaction mixture in the reactor. An input overheated water steam is supplied countercurrentlyto the catalyst into the reactor withpressure higher than the sum of saturated vapour tension of the reaction mixture at the working temperature and hydrostatic pressure of the reaction mixture. Aninput reactant aniline is supplied into the reactor countercurrently to the catalyst input with such speed which ensures at least the same residence time of the catalyst in uplift as is the residence time of aniline in the reactor.</p> |
