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Energy integration

It is now clear that the suppression of the dehydrogenation step is the most radical step in saving energy. This is possible only if a suitable catalyst may be found to meet the specifications of KA-oil in just one reaction step. This option will be discussed in the next section. [Pg.158]

Three basic features of integrated chemical processes lie at the root of our need to consider the entire plant s control system (1) the effect of material recycle, (2) the effect of energy integration, and (3) the need to account for chemical component inventories. If we did not have to worry about these issues, then we would not have to deal with a complex plantwide control problem. However, there are fundamental reasons why each of these exists in virtually all real processes. [Pg.18]

Increase conversion For chemical processes involving reversible reactions, conversion of reactants to products is limited by thermodynamic equilibrium constraints. Therefore the reactor effluent by necessity contains both reactants and products. Separation and recycle of reactants are essential if the process is to be economically viable. [Pg.18]

Improve economics In most systems it is simply cheaper to build a reactor with incomplete conversion and recycle reactants than it is to reach the necessary conversion level in one reactor or several in series. The simple little process discussed in Sec. 2.6 illustrates this for a binary system with one reaction A B. A reactor followed by a stripping column with recycle is cheaper than one large reactor or three reactors in series. [Pg.18]

Improve yields In reaction systems such as A - B - C, where B is the desired product, the per-pass conversion of A must be kept low to avoid producing too much of the undesirable product C. Therefore [Pg.18]

Provide thermal sink In adiabatic reactors and in reactors where cooling is difficult and exothermic heat effects are large, it is often necessary to feed excess material to the reactor (an excess of one reactant or a product) so that the reactor temperature increase will not be too large. High temperature can potentially create several unpleasant events it can lead to thermal runaways, it can deactivate catalysts, it can cause undesirable side reactions, it can cause mechanical failure of equipment, etc. So the heat of reaction is absorbed by the sensible heat required to raise the temperature of the excess material in the stream flowing through the reactor. [Pg.19]


The core contributions thus require the calculation of integrals that involve basis functions on up to two centres (depending upon whether 0, and 0 are centred on the same nucleus or not). Each element H)) can in turn be obtained as the sum of a kinetic energy Integra and a potential energy integral corresponding to the two terms in the one-electror HcUniltonian. [Pg.77]

Maz ya V.G., Nazarov S.A. (1987) Asymptotics of energy integrals for small perturbations of the boundary near corner and conical points. Trudy Moscow Math. Soc. 50, 79-129 (in Russian). [Pg.382]

Branches of Process inte ation Mass Integration and Energy Integration... [Pg.10]

Balakrishna, S. and Biegler, L.T., 1992b. Targeting strategies for the synthesis and energy integration of non-isothermal reactor networks. Industrial and Engineering Chemistry Research, 31(9), 2152. [Pg.299]

Table 3.1 Energy integrals for the hydrogen moleeule-ion LCAO problem. Reduced units are used throughout, f is the orbital exponent, and Rab the internuelear separation, p = Rab... Table 3.1 Energy integrals for the hydrogen moleeule-ion LCAO problem. Reduced units are used throughout, f is the orbital exponent, and Rab the internuelear separation, p = Rab...
The main advantage of the method with correlation factor, based on Eq. III. 128 or Eq. III. 129, lies in the fact that it may be applied to any many-electron system. The practical calculation of the energy integrals involved may be fairly cumbersome, but the approach is nevertheless straightforward. [Pg.305]

The effective atomic numbers in the radial wave functions cannot be evaluated by minimizing the energy integral, because of neglect of inner shells. In all the calculations reported the effective atomic numbers were given the value 1. [Pg.215]

This discussion is most easily made precise by the use of the energy integral. If p represents an arbitrary normalized wave function for a system, then the integral... [Pg.307]

It is impossible to carry out this program of directly evaluating the energy integral except in the simplest cases but rough energy curves for various electronic structures can often be constructed by semi-empirical methods, and the discussion outlined above carried out with them. Thus information regarding the repulsive forces between ions obtained from the observed properties of ionic crystals can be used for ionic states of mole-... [Pg.308]

We shall illustrate the applicability of the GvdW(S) functional above by considering the case of gas-liquid surface tension for the Lennard-Jones fluid. This will also introduce the variational principle by which equilibrium properties are most efficiently found in a density functional theory. Suppose we assume the profile to be of step function shape, i.e., changing abruptly from liquid to gas density at a plane. In this case the binding energy integrals in Ey can be done analytically and we get for the surface tension [9]... [Pg.101]

In this section the fundamental principles of the pinch technology method for energy integration will be outlined and illustrated with reference to a simple problem. The method and its applications are described fully in a guide published by the Institution of Chemical... [Pg.111]

There is clearly scope for energy integration between these four streams. Two require heating and two cooling and the stream temperatures are such that heat can be transferred from the hot to the cold streams. The task is to find the best arrangement of heat exchangers to achieve the target temperatures. [Pg.112]

The New Energy and Industrial Technology Development Organization (NEDO), 1993. Final Report for the Project of Super-Heat Pump and Energy Integrated System, September 1993 (in Japanese). [Pg.390]

Current state-of-the-art technology for the production of MIBK involves one-step liquid phase processes in trickle bed reactors at 100-160°C and 1 to 10 MPa utilizing various multifunctional catalysts including Pd, Pt, Ni or Cu supported on, metal oxides, cation exchange resins, modified ZSM5 and other zeolites with lull energy integration (2,3,4). However, the MIBK... [Pg.261]

At this point it might be helpful to summarize what has been done so far in terms of effective potentials. To obtain the QFH correction, we started with an exact path integral expression and obtained the effective potential by making a first-order cumulant expansion of the Boltzmann factor and analytically performing all of the Gaussian kinetic energy integrals. Once the first-order cumulant approximation is made, the rest of the derivation is exact up to (11.26). A second-order expansion of the potential then leads to the QFH approximation. [Pg.406]

Balakrishna, S. and L. T. Biegler. Targeting Strategies for the Synthesis and Energy Integration of Nonisothermal Reactor Networks. Ind Eng Chem Res 31 2152-2164 (1992). [Pg.514]

However, because the energy spectrum is discrete, both before and after chemisorption, AEa does not take the form of the energy-integral (4.99), but is instead evaluated via finite sums (4.86) of the energies, i.e.,... [Pg.132]

The partition function can be written as the product of K, the kinetic energy integral, and Z, the configurational integral,... [Pg.84]

In all cases considered, differences in free energy for a given material in two different states or derivatives of the free energy are calculated and the contributions of the kinetic energy integrals to these quantities will exactly cancel. Since the results are not altered by its omission, for the sake of brevity, we shall not consider the kinetic energy integral. [Pg.84]


See other pages where Energy integration is mentioned: [Pg.208]    [Pg.252]    [Pg.252]    [Pg.202]    [Pg.252]    [Pg.252]    [Pg.252]    [Pg.276]    [Pg.222]    [Pg.10]    [Pg.10]    [Pg.294]    [Pg.282]    [Pg.304]    [Pg.141]    [Pg.214]    [Pg.215]    [Pg.317]    [Pg.158]    [Pg.228]    [Pg.499]    [Pg.111]    [Pg.112]    [Pg.379]    [Pg.234]    [Pg.155]    [Pg.237]   
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See also in sourсe #XX -- [ Pg.10 ]

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See also in sourсe #XX -- [ Pg.177 ]

See also in sourсe #XX -- [ Pg.247 ]

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Coal powered energy plants, integrated

Coal powered energy plants, integrated gasification combined cycle

Configurational integral energy

Coulomb integral, alpha reference energy

Coulomb integrals potential energy surfaces

Dilution, free energy integral

Electron integrated overall energies

Energy equation integral

Energy integration distillation

Energy integration optimization

Energy integration reactor networks

Energy integration software

Energy integration superstructure

Energy integration, definition

Energy representation thermodynamic integration methods

Energy spectrum integral

Energy-integrated distillation

Engineering Intensified Process Systems for Renewable Energy Integration

Entropy and Free Energy Differences by Calorimetric Thermodynamic Integration

Excess integral molar free energy

Exchange energy integral

Free energy integral molar

Free energy methods thermodynamic integration

Free energy perturbation and thermodynamic integration methods

Free energy thermodynamic integration

Free-energy calculations Gibbs-Duhem integration

Free-energy calculations thermodynamic integration

Fundamental Kinetic-Energy Integral

Gibbs energy integral

Heat-exchanger network synthesis energy integration

Hydrogen Fueling Sustainability of Energy Systems, Regional Integration, and Development The Sahara Wind Project

Integral balance energy

Integral electron kinetic energy

Integral encounter theory reversible energy transfer

Integral energy

Integral energy

Integral equations Internal energy

Integral free energy

Integral potential energy

Integrals Coulomb energy

Integrals dispersion energy

Integrals polarization energy

Integrate Health, energy sources

Integrated energy

Integrated energy

Integrated systems energy plantations

Integration of Hydrogen Energy Technologies in Autonomous Power Systems

Integration of primary energy sources with

Kinetic energy integrals

Kinetic-energy integrals integral evaluation

Modeling systems energy integration

Molecular integral evaluation kinetic-energy integrals

Nuclear energy Integral Fast Reactor

Path integral free-energy perturbation and

Path integral free-energy perturbation and umbrella sampling

Potential energy surface overlap integrals

Process energy integration/heat

Process integration maximum energy recovery

Process optimization integrated energy

Process synthesis energy integration

Process systems with energy integration

Reactor network synthesis energy integration

Relative integral molar free energy

Renewable energy integration

Site energy distribution integral

Surface integrals proportional to the energy

Targeting energy integration

The PDT and Thermodynamic Integration for Exact Quantum Free Energy Changes

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