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Processability behaviors

The advantage of static decoupling is that less process information is required namely, only steady-state gains. Nonlinear decouplers can be used when the process behavior is nonlinear. [Pg.737]

A key feature of MFC is that future process behavior is predicted using a dynamic model and available measurements. The controller outputs are calculated so as to minimize the difference between the predicted process response and the desired response. At each sampling instant, the control calculations are repeated and the predictions updated based on current measurements. In typical industrial applications, the set point and target values for the MFC calculations are updated using on-hne optimization based on a steady-state model of the process. Constraints on the controlled and manipulated variables can be routinely included in both the MFC and optimization calculations. The extensive MFC literature includes survey articles (Garcia, Frett, and Morari, Automatica, 25, 335, 1989 Richalet, Automatica, 29, 1251, 1993) and books (Frett and Garcia, Fundamental Process Control, Butterworths, Stoneham, Massachusetts, 1988 Soeterboek, Predictive Control—A Unified Approach, Frentice Hall, Englewood Cliffs, New Jersey, 1991). [Pg.739]

According to the end use application, PEs are processed by various techniques, which include injection moulding, blow moulding, rotomoulding, and film extrusion. However, since the bulk of the processed material is used as film in the area of packaging, the discussion in this chapter focuses mainly on processing behavior and the ultimate properties of tubular blown film. [Pg.278]

PEs, as other polymers, exhibit nonlinear behavior in their viscous and elastic properties under practical processing conditions, i.e., at high-shear stresses. The MFI value is, therefore, of little importance in polymer processing as it is determined at a fixed low-shear rate and does not provide information on melt elasticity [38,39]. In order to understand the processing behavior of polymers, studies on melt viscosity are done in the high-shear rate range viz. 100-1000 s . Additionally, it is important to measure the elastic property of a polymer under similar conditions to achieve consistent product quality in terms of residual stress and/or dimensional accuracy of the processed product. [Pg.280]

Rheological and processability behaviors were studied in a Monsanto processability tester (MPT), which is an automatic high-pressure capillary viscometer. The entire barrel and capillary are electrically heated with a microprocessor-based temperature controller [14], The... [Pg.442]

AND ASSEMBLING and Chapter 8, PROCESSING BEHAVIORS and PROCESSING AND PROPERTY). [Pg.179]

Specific family or group of plastics (polyethylene, polyvinyl chlorides, etc.) are compounded or alloyed to provide different properties and/or processing behaviors. Thus a plastic listed in Fig. 5-6 could have different heat resistance properties. [Pg.319]

Designing with plastics based on material process behaviors", Donald V. Rosato, Marlene G. Rosato, and Dominick V. Rosato, Kluwer Academic Publishers (2000). [Pg.610]

Designing with plastics based on material process behaviors , Donald V. Rosato, Marlene G. Rosato, and Dominick V. Rosato, Kluwer Academic Publishers (2000). This book provides a simplified and practical approach to designing plastic products that fundamentally relates to the load, temperature, time, and environment subjected to a product. It will provide the basic behaviors in what to consider when designing plastic products to meet performance and cost requirements. Important aspects are presented such as understanding the advantages of different shapes and how they influence designs. [Pg.612]

Ghosh, A. and De, S.K. Dependence of Physical Properties and Processing Behavior of Blends of Silicone Rubber and Fluorombber on Blend Morphology. Rubber Chem. Technol. 77(5), 856-872, November/December 2004. [Pg.348]

With respect to stream rheological effects in rubber processing, and despite all the restrictions discussed above, it seems nevertheless that the key information is how the nonlinear viscoelasticity is related to the processing behavior of mbber compounds. Such information can be deduced from the appropriate test procedure with the RPA, providing one considers the capabilities of the instmment to provide nonlinear viscoelastic data. [Pg.823]

Mineral oils also known as extender oils comprise of a wide range of minimum 1000 different chemical components (Figure 32.6) and are used extensively for reduction of compound costs and improved processing behaviors.They are also used as plastisizers for improved low temperature properties and improved rubber elasticity. Basically they are a mixture of aromatic, naphthanic, paraffinic, and polycyclic aromatic (PCA) materials. Mostly, 75% of extender oils are used in the tread, subtread, and shoulder 10%-15% in the sidewall approximately 5% in the inner Uner and less than 10% in the remaining parts for a typical PCR tire. In total, one passanger tire can contain up to 700 g of oil. [Pg.924]

The key recognitive skill required to carry out the above tasks is the formation of a mental model of the process operations that fits the current facts about the process and enables the operators to correctly assess process behavior and predict the effects of possible control actions. Correct mental models of process operations have allowed operators to overcome the weakness of lost sensors and conflicting trends, even under the pressure of an emergency (Dvorak, 1987), whereas most of the operational mishandlings are due to an erroneous perception as to what is going on in the process (O Shima, 1983). [Pg.208]

The term, process trend, undoubtedly carries an intuitive meaning about how process behavior changes over time. However, the exact mean-... [Pg.211]

The scope of this book deals primarily with the parameter estimation problem. Our focus will be on the estimation of adjustable parameters in nonlinear models described by algebraic or ordinary differential equations. The models describe processes and thus explain the behavior of the observed data. It is assumed that the structure of the model is known. The best parameters are estimated in order to be used in the model for predictive purposes at other conditions where the model is called to describe process behavior. [Pg.2]

In practice, there may not be sufficient operating experience and resultant data to develop a numeric-symbolic interpreter that can map with certainty to the labels of interest, Cl. Under these circumstances, if sufficient knowledge of process behaviors exists, it is possible to construct a KBS in place of available operating data. But the KBS maps symbolic forms of input data into the symbolic labels of interest and is therefore not sufficient in itself. A KBS depends on intermediate interpretations, ft, that can be generated with certainty from a numeric-symbolic mapper. This is shown in Fig. 4. In these cases, the burden of interpretation becomes distributed between the numeric-symbolic and symbolic-symbolic interpreters. Figure 4 retains the value of input mapping to preprocess data for the numeric-symbolic interpreter. [Pg.44]

To address this situation, a data interpretation system was constructed to monitor and detect changes in the second stage that will significantly affect the product quality. It is here that critical properties are imparted to the process material. Intuitively, if the second stage can be monitored to anticipate shifts in normal process operation or to detect equipment failure, then corrective action can be taken to minimize these effects on the final product. One of the limitations of this approach is that disturbances that may affect the final product may not manifest themselves in the variables used to develop the reference model. The converse is also true—that disturbances in the monitored variables may not affect the final product. However, faced with few choices, the use of a reference model using the process data is a rational approach to monitor and to detect unusual process behavior, to improve process understanding, and to maintain continuous operation. [Pg.84]

This example (Kosanovich et al., 1995) builds on the previous example and illustrates how multivariate statistical techniques can be used in a variety of ways to understand and compare process behavior. The charge to the reactor is an aqueous solution that is first boiled in an evaporator until the water content is reduced to approximately 20% by weight. The evaporator s contents are then discharged into a reactor in which 10 to 20 pounds of polymer residue can be present from the processing of the previous batch. [Pg.86]

Because of the role of precursor structure on film processing behavior (consolidation, densification, crystallization behavior), the reaction pathways are typically biased through the use of the catalyst, which is simply an acid or a base. This steers the reaction toward an electrophilic or nucleophilic attack of the M—OR bond.1,63 Hydrolysis sensitivity of singly or multiply hydrolyzed silicon alkoxides is also influenced by the catalyst, which contributes to the observed variations in oligomer length and structure. Figure 2.3b illustrates... [Pg.42]

Numerous investigators have attempted to control the precursor structure and related solution chemistry effects with varying degrees of success, to influence subsequent processing behavior, such as crystallization tempera-ture.40-42,78,109 110 Particular attention has been given to precursor characteristics such as structural similarity to the desired product and the chemical homogeneity of the precursor species. For multicomponent films, this latter factor is believed to influence the interdiffusional distances associated with the formation of complex crystal structures, such as perovskite compounds. Synthetic approaches have been geared toward the preparation of multimetal species with cation stoichiometry identical to that of the desired crystalline phase.40 42 83 84... [Pg.57]


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See also in sourсe #XX -- [ Pg.442 ]




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