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Dual mode switching systems

For a problem such as this, the dual-mode eontrol system deseribed in Fig. 5.17 is extremely effective. The preload is estimated as before, but no correction is required for integration, because reset aetion is not initiated until the error is nearly zero. Full heating ean be applied to within 1 or 2 percent of the set point, far beyond the eapabilities of a 25 pereent proportional band. Yet full cooling need only be applied for a time delay of perhaps a minute to dissipate the energy stored in the jaeket. As pointed out in Fig. 5.18, the switching parameters are easy to adjust and tolerant of maladjustment. [Pg.284]

The spiro carbon is a stereogenic center in spiropyrans, but because of the achiral structure of the open merocyanine form, the photochromic process will always lead to racemization unless additional chiral moieties are present. When a chiral substituent was introduced, remote from the spiro center, it was possible to isolate diastereo-isomers of the spiropyrans, but rapid epimerization at the spiro center occurred.1441 Diastereoselective switching was successful with 28, in which a stereogenic center was present close to the spiro carbon (Scheme 15).[45] Distinct changes in CD absorption at 250 nm were monitored upon irradiation with UV (250 nm) and with visible light (>530 nm) and a diastereomeric ratio of 1.6 1.0 was calculated for the closed form 28. Furthermore, a temperature-dependent CD effect was observed with this system it was attributed to an inversion of the diastereomeric composition at low temperatures. It might be possible to exploit such effects in dual-mode chiral response systems. A diastereoselective ring-closure was also recently observed in a photochromic N6-spirobenzopyran tricarbonyl chromium complex. 451 ... [Pg.142]

Figure 11.36 Schematic diagram of the dual-column extraction system on-line via a Valeo 10-port switching valve with the chiral LC-MS/MS system. The components were as follows PI, a Leap Technologies autosampler with two HPLC pumps delivering mobile phases A and B to the extraction column EC-1 or EC-2 (Waters Oasis HLB 25 gm, 1 x 50 mm) P2, HPLC pump system delivering isocratic elution mobile phase through the extraction column to the chiral analytical column full bold arrows, pathway for mobile phase A (Table) used to load plasma sample onto extraction column dashed arrows, pathway for mobile phase (neither A nor B) used to elute analytes from extraction column to the chiral analytical column F, in-line filter G in-line guard column MS, a triple-quadrupole instrument in MRM mode. Reproduced from Xia, J. Chromatogr. B 788, 317, copyright (2003) with permission from Elsevier. Figure 11.36 Schematic diagram of the dual-column extraction system on-line via a Valeo 10-port switching valve with the chiral LC-MS/MS system. The components were as follows PI, a Leap Technologies autosampler with two HPLC pumps delivering mobile phases A and B to the extraction column EC-1 or EC-2 (Waters Oasis HLB 25 gm, 1 x 50 mm) P2, HPLC pump system delivering isocratic elution mobile phase through the extraction column to the chiral analytical column full bold arrows, pathway for mobile phase A (Table) used to load plasma sample onto extraction column dashed arrows, pathway for mobile phase (neither A nor B) used to elute analytes from extraction column to the chiral analytical column F, in-line filter G in-line guard column MS, a triple-quadrupole instrument in MRM mode. Reproduced from Xia, J. Chromatogr. B 788, 317, copyright (2003) with permission from Elsevier.
The linear controller must, above all, be preloaded to the anticipated process conditions at the new set point. This was found to be advantageous whenever an antiwindup switch is used in the reset circuit. And because reset is normally required with a dual-mode arrangement, the control system must include an antiwindup switch into which the preload setting is introduced. The arrangement of the system for increasing set-point changes is shown in Fig. 5.17. [Pg.142]

A batch chemical reactor is to be brought up to operating temperature with a dual-mode system. Full controller output supplies heat through a hot-water valve, while zero output opens a cold-mater valve fully at 50 percent output, both valves are closed. While full heating is applied, the temperature of the batch rises at, IT/min the time constant of the jacket is estimated at 3 min, and the total dead time of the system is 2 min. The normal load is equivalent to 30 percent, of controller output. Estimate the required values for the three adjustments in the optimal switching program. [Pg.150]


See other pages where Dual mode switching systems is mentioned: [Pg.3403]    [Pg.3403]    [Pg.145]    [Pg.210]    [Pg.1978]    [Pg.129]    [Pg.70]    [Pg.2190]    [Pg.754]    [Pg.679]    [Pg.657]    [Pg.355]    [Pg.67]    [Pg.209]    [Pg.326]    [Pg.330]    [Pg.429]    [Pg.107]    [Pg.357]    [Pg.107]    [Pg.30]    [Pg.34]    [Pg.238]    [Pg.63]    [Pg.138]    [Pg.74]    [Pg.59]    [Pg.44]    [Pg.283]    [Pg.251]   
See also in sourсe #XX -- [ Pg.229 ]




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