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System balances

Therefore inductive reactance equal to Xp must be introduced into the Y phase to equalize the reactance distribution and make the system balanced (Figure 28.25). [Pg.884]

Note when used for pump system balance, this Zhf must be used as a negative number ( — 0.1863) because it is a pressure loss associated with the fluid flowing. For pipe line sizing, the pressure head on the tank of 5 psig and any elevation difference between tank outlet nozzle and pump suction centerline do not enter into the calculations. [Pg.84]

This does not require the system balance as outlined in A through C above however, wthout first preparing a pressure balance, the designer cannot be confident of... [Pg.95]

The fan will now have a system resistance Curve A-B and operate at Point 2. As an alternate approach to securing a system balance at the point required, the motor speed can be changed by a suitable means. If the fan speed is reduced by 13,000/13,600, the new speed should be (0.889) (600) = 573 rpm. A new fan Curve E-E will go through the desired point conditions. The new horsepower for this operation will be (3.87) (573/600)" = 3.35 hp. [Pg.564]

Design arrangements for reduced-temperature secondary systems (sometimes referred to as injection circuits) include fixed provisions for minimum dilution rates. Conventional system-balancing devices with three-port automatic modulating valves to regulate mixed water temperatures and, hence, heat output are used. Automatic safety controls must prevent excessive temperatures occurring in the coil circuits, as floor fabrics or finishes could be damaged very rapidly. [Pg.408]

Gurr, G. M., Wratten, S. D., Tylianakis, J., Kean, J. and Keller, M. 2005. Providing plant food for natural enemies in farming systems Balancing practicalities and theory. In Plant-Provided Food for Carnivorous Insects A Protective Mutualism and Its Applications (Wackers, F. L., van Rijn, P. C. J. and Bruin, J., eds), pp. 326-347. Cambridge Cambridge University Press. [Pg.283]

Engineering systems mainly involve a single-phase fluid mixture with n components, subject to fluid friction, heat transfer, mass transfer, and a number of / chemical reactions. A local thermodynamic state of the fluid is specified by two intensive parameters, for example, velocity of the fluid and the chemical composition in terms of component mass fractions wr For a unique description of the system, balance equations must be derived for the mass, momentum, energy, and entropy. The balance equations, considered on a per unit volume basis, can be written in terms of the partial time derivative with an observer at rest, and in terms of the substantial derivative with an observer moving along with the fluid. Later, the balance equations are used in the Gibbs relation to determine the rate of entropy production. The balance equations allow us to clearly identify the importance of the local thermodynamic equilibrium postulate in deriving the relationships for entropy production. [Pg.115]

Water soluble, antistatic lubricant for processing relatively clean fibres on the woollen system. Balanced frictional properties give improved fibre control in carding with film slubbings, reduced fibre breakage and more levels yarns. [Pg.30]

Boundary encloses the entire process the system defined by this boundary has as inputs Feed Streams 1,2, and 3 and Product Streams 1,2, and 3. (Convince yourself.) Balances on this system are referred to as overall balances. The stream that connects Units 1 and 2 is internal to this system and so would not enter into overall system balances. [Pg.104]

We can therefore determine n and 3 from overall system balances. We would write a dry air balance first since it only involves one unknown (nj), while total mole and water balances involve both unknowns. Once n has been determined, the second balance yields nj. No more can be done with the overall system, so we move on to other subsystems. [Pg.111]

We next write the two allowed overfill system balances. The questions are, which ones and in what... [Pg.114]

To carry out degree-of-freedom analyses of reactive systems you must first understand the concepts of independent equations, independent species, and independent chemical reactions. We explain these concepts in the next section, following which we outline and illustrate the three approaches to reactive system balance calculations. [Pg.126]

List possible reasons for the differences between the design predictions and the experimental values of the output stream variables and for the failure of the experimental system balance to close. [Pg.152]

Recycle is a common feature of chemical processes. Its most common use is to send unused raw materials emerging from a process unit back to the unit. Overall system balances are usually (but not always) convenient starting points for analyzing process with recycle. A purge stream is withdrawn from a process when a species enters in the process feed and is completely recycled. If this species were not removed in the purge, it would keep accumulating in the process system and eventually lead to shutdown. [Pg.154]

Starting with the open system balance equation, derive the steady-state mechanical energy balance equation (Equation 7.7-2) for an incompressible fluid and simplify the equation further to derive the Bernoulli equation. List all the assumptions made in the derivation of the latter equation. [Pg.315]

The general form of the mechanical energy balance can be derived starting with the open-system balance and a second equation expressing the law of conservation of momentum, a derivation beyond the scope of this book. This section presents a simplified form for a single incompressible liquid flowing into and out of a process system at steady state. [Pg.333]

The first law of thermodynamics for an open system at steady state resembles the closed-system balance ... [Pg.338]

Solve the system balance equations, working around the cycle from unit to unit until the tear stream variables are recalculated. [Pg.515]

Ototoxicity is defined as affects on the organs of the inner ear. Oto means ear. The organs of the inner ear supply two key functions to the body hearing and balance. Chemicals that cause ototoxicity can affect the cochlea (hearing) or the vestibular system (balance). Ototoxicity of the cochlea or the Organ of Corti may also be termed cochleotoxicity. Ototoxicity of the vestibular system may also be termed... [Pg.1899]


See other pages where System balances is mentioned: [Pg.882]    [Pg.153]    [Pg.154]    [Pg.679]    [Pg.117]    [Pg.361]    [Pg.42]    [Pg.85]    [Pg.186]    [Pg.64]    [Pg.158]    [Pg.238]    [Pg.282]    [Pg.171]    [Pg.288]    [Pg.519]    [Pg.411]    [Pg.101]    [Pg.240]    [Pg.253]    [Pg.541]    [Pg.8]    [Pg.117]    [Pg.627]    [Pg.168]    [Pg.169]   
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Balance for Deposition in a Flow System

Balance for Open Systems

Balance model systems

Balance of system

Balance-of-plant systems

Balance-of-systems cost

Balanced system

Balanced system

Balances independent, nonreactive system

Balances independent, reactive system

Balancing of Gasification Systems

Balancing the Runner System in Multi-Cavity Injection Molds

Binary systems mass balance

Complex system energy balance

Complex systems material balance equations

Component balances flow system

Cooling tower system balance

Distributed Balancing System

Energy Balance for Closed Systems

Energy Balances on Closed Systems

Energy Balances on Open Systems at Steady State

Energy balance closed systems

Energy balance for a closed system

Energy balance steady-flow systems

Energy,balance for an open system

Entropy balance for open systems

Fuel system material balance

Fundamentals of Material Balance (Nonreactive Systems)

General heat balance equation of a calorimetric system

Generalized Mass Balance for Two Phase Systems

Hierarchical balancing system

Hydrodynamically balanced systems

Hydrophilic-lipophilic balance system

Implementation of a company-wide balancing system

Mass and Energy Balances for Open Systems

Mass balance nonisothermal system

Material Balance Equations for Reactive Systems (Steady-State and Continuous Operation)

Material and Energy Balance in Open Systems Under Steady-State Conditions

Molar balance in open and closed systems with chemical reaction

Open systems energy balances

Open-System Energy Balances on Process Equipment

Oxidation-Reduction Balances of the Earth System

Radiation balance of the Earth-atmosphere system

Reaction Invariant Balances in a System of Units

Reactor/heat exchanger systems balances

Renal system balance

Requirements on the Industrial Balancing System

Structure of the Balancing System IBS

Surfactants balance) system

System of mass balance equations

The General Balance Equations for Distributed Systems

The whole system of balance equations

Three-phase systems mass-balance equation

Total energy balance, closed system

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