Big Chemical Encyclopedia

Chemical substances, components, reactions, process design ...

Articles Figures Tables About

Closed loop system formulations

Dual-temperature and simple LPHW heating systems typically require 1,000 to 1,300 ppm as N02 (1,500-2,000 ppm as NaN02) when a standard nitrite/borate/TTA formulation is employed. (This is about twice the level required for cold and chilled water closed loop systems.)... [Pg.396]

It is important not to leave the system empty of water for any long period, as rapid surface rusting will take place. As soon as the closed-loop system is declared free of contamination, sufficient corrosion inhibitor is added to provide long-term corrosion protection. The corrosion inhibitor is usually an anodic, passivating formulation, typically based on nitrite or tannin (and often in combination with phosphate, silicate, borate, or molybdate, etc.). Finally, after confirmation that the entire system is adequately treated (which usually requires the inhibited water in the system to be recirculated for a further 16 to 24 hours), the system is signed off and handed over. [Pg.335]

Off-line de-oiling formulation for heat exchanger or closed-loop system... [Pg.343]

The complete formulation of the closed loop system optimization using a PID controller is as follows... [Pg.43]

Consider, for example, a typical stable system, y(i) = (fcle 7(l -I- kis)) u(s), which is known exactly except for an uncertainty in kl. It is required that the control bring the system from a given initial condition to target steady state at some arbitrary time in the future in the absence of disturbances. Each possible input sequence, u(k), achieves this for one and only one value of k. The validation problem formulation above will therefore indicate that no controller exists satisfying this problem specification. In fact, any PI controller giving a stable closed-loop system will achieve the performance specified. [Pg.323]

Clean, segregated plastics arising from industrial operations (including the ultimate disposal of motor car components) should be recycled in a closed loop system into the primary application. Some packaging, notably film wrap, that can be easily collected in bulk from industrial waste may be economically resourced in the same way. Clean PVC waste can be effectively reprocessed in this way provided the nature of the plasticiser/stabiliser formulation is known. This will be discussed in detail in the following sections. [Pg.4]

Kim, S. S., and Haug, E. J., Recursive Formulation for Flexible Multibody Dynamics Part II, Closed-Loop Systems, Computer Methods in Applied Mechanics and Engineering, Vol. 74, No. 3, 1989, pp. 251-269. [Pg.95]

Kim S.S., Haug E.J., A Recursive Formulation for Flexible Multibody Dynamics, Part II Closed Loop Systems, Comput. Methods Appl. Mech. Engrg. 74 (1989), 251-269. [Pg.584]

Nitrite formulations are employed for both hot and cold water closed loops (and also occasionally for open cooling systems). Unfortunately, nitrite is easily oxidized to nitrate and is very susceptible to microbiological attack (by Nitrobacter agilis and other microorganisms). Nevertheless, it is a good low-cost passivating inhibitor. [Pg.395]

Azoles provide effective corrosion inhibition primarily by chemisorption of the molecule on the metal substrate. Several different types of azoles are available for incorporation into formulations used for the corrosion inhibition of closed loop LPHW heating and low MU requirement, LP steam heating systems. [Pg.400]

NOTE Strongly alkaline, closed loop LPHW system formulations, such as nitrite/borates, typically include an azole product at about 4 to 5% (50% solution). Lower alkalinity products (often the molybdates) have significantly less, perhaps only 0.5%. For comparison, open cooling water and chilled water system formulations typically contain about 2 to 3 % (50% solution) azole. [Pg.401]

Both of these formulations are suitable for closed loop, steel HW heating circuits and low MU, LP steam heating systems. [Pg.403]

Tannin reserve to be maintained at 100 to 150 ppm, other parameters as per standard recommendations. The tannin-based closed-loop formula, also shown, is designed for use at 1,500 to 2,000 ppm product in the system, which provides approximately 180 to 240 ppm tannin reserve. Various modifications to these formulations exist for example, 0.5 to 1.0% diethylhydroxylamine (DEHA) may be added to improve passivation when used in simple HW heating systems. [Pg.410]

Water is one of the most widely used raw materials in the manufacture of aqueous paint formulations. But as well as being used in production it can have a number of other uses, e.g. cooling and cleaning. Because of the cost of "new" water and disposal of contaminated water most manufactures have introduced closed loop or recycling systems. [Pg.70]

Polysilicates, incorporated in various formulations that may include P-P04 or molybdate and phosphonates/TTA/polymer, have found application for smaller, light duty, open cooling systems and closed-loop circuits, especially where naturally soft or ion-exchange-softened makeup waters have been used. The reported effectiveness of such programs has been mixed. [Pg.151]

Stochastic objective function. The preceding MPC formulation assumes that future process outputs are deterministic over the finite optimization horizon. For a more realistic representation of future process outputs, one may consider a probabilistic (stochastic) prediction for y[/c + i k] and formulate an objective function that contains the expectation of appropriate functionals. For example, if y[k + i k] is probabilistic, then the expectation of the functional in Eq. (4) could be used. This formulation, known as open-loop optimal feedback, does not take into account the fact that additional information would be available at future time points k + i and assumes that the system will essentially run in open-loop fashion over the optimization horizon. An alternative, producing a closed-loop optimal feedback law relies... [Pg.140]

Kaplan and Norton (2008) state that strategy develops and management is a closed-loop process where each part of the system influences aU other parts. They proposed the framework shown in Fig. 7.11 to integrate strategy formulation and planning with operational execution. [Pg.168]

The most important and challenging problems in active and passive stmctural control systems are the formulation and solution of optimal control and nonlinear constrained optimization needed to develop appropriate closed loop feedback control algorithms and the optimal placement, which is the central focus of this book. State-of-the-art techniques for optimal design of passive and active control systems are described in detail in various chapters written by researchers aroimd the world. I welcome this new book for offering a very good overview of the current developments in the field. [Pg.410]

While the main thrust of these analyses are to provide a plant that exhibits satisfactory closed-loop performance, the assumptions regarding the control system vary considerably across the various methods proposed. The open-loop indicators are largely based on factors that limit achievable closed-loop performance independent of controller type, whereas most of the optimization based integrated design formulations assume a specific controller type such as multiloop PI, LQG and so forth. While this is not considered to be a problem per se, it is important that the implications of these assumptions are clear so that appropriate deductions may be drawn. This chapter attempts to at least in part address this issue. [Pg.240]

For linear systems, the closed-loop mapping from the external inputs to outputs of interest may be formulated directly. We recognize first that for a truncated transfer function approximation of the form. [Pg.247]

The inclusion of the state space realization of Q within an optimization formulation will be outlined here. In order to illustrate some of the details of the formulation, a specific problem will be considered variations to address other scenarios such as determination of a closed-loop performance limit for a fixed design, follow in a straightforward manner. In so doing, the variables and constraints within the general problem formulation (PI) in Section 3 will be separated into groupings that represent the various components of the overall system. [Pg.252]


See other pages where Closed loop system formulations is mentioned: [Pg.398]    [Pg.75]    [Pg.62]    [Pg.41]    [Pg.2129]    [Pg.41]    [Pg.461]    [Pg.3]    [Pg.91]    [Pg.320]    [Pg.8]    [Pg.246]    [Pg.64]    [Pg.65]    [Pg.530]    [Pg.569]    [Pg.722]    [Pg.15]    [Pg.635]    [Pg.139]    [Pg.136]    [Pg.438]    [Pg.2289]    [Pg.126]    [Pg.172]    [Pg.243]    [Pg.249]    [Pg.606]    [Pg.293]    [Pg.136]   
See also in sourсe #XX -- [ Pg.176 ]




SEARCH



Closed loop

Closed loop systems

Closing loops

Formulation system

© 2024 chempedia.info