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primary controller. They overcome variable pressure drop, valve friction, and nonlinear valve characteristics. But if the measurement is in the differential form, its nonlinearity becomes part of the primary loop, because flow is being delivered to the process while flow squared is set by the primary controller. The nonlinearity of the differential meter was recognized earlier as a problem in a flow loop. But using a differential meter in the secondary loop of a difficult thermal or composition process is asking for trouble. Suppose the process is linear with respect to flow, as in Example 3.6. The output of the primary controller manipulates differential pressure, however, which varies as flow squared: rdlc pdf 417 PDF417 Barcode Creating Library for RDLC Reports | Generate ...
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Barcode Control SDK supports generating Data Matrix, QR Code, PDF - 417 barcodes in RDLC Local Report using VB and C# class library both in ASP.NET and ... Loop gain now varies inversely with flow (which is much worse than varying directly with flow, because it can approach infinity). And since many processes are started up or operated for extended periods at low flow, the problem is serious. If the primary controller is not placed in manual, the loop will limit-cycle around zero flow. The best solution is to insert a square-root extractor in the flow-measurement line to linearize the secondary loop. The problem of variable dead time was discussed in Chap. 2. This problem was resolved by using an equal-percentage control valve. If a flow loop were placed around the valve, however, its characteristic would be lost. Furthermore, if the flow loop were of the differential type, its nonlinearity would be in the wrong direction, making the primary-loop gain vary inversely as the square of flow. These factors deserve careful consideration before deciding on a cascade flow loop. Because flow loops resonate in the l- to lo-set range, they are safe to use in cascade with temperature or composition, but not ordinarily with liquid or gas pressure or other flow loops. Liquid level is only cascaded to flow in applications involving boiling liquids or condensing vapors, where the natural period of the primary loop is long compared to the flow loop. i =1 We can expand it to 12/n 3 + 22/n 3 + 32/n 3 + + n 2/n 3 + which simplifies to (12 + 22 + 32 + + n 2 + )/n 3 As n grows endlessly larger, we have Lim (12 + 22 + 32 + + n 2)/n 3
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