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Initial and final values

Initial and final values of R (final value based on all data) 51.4% 17.1%... [Pg.236]

Initial and final temperature and feed rate are taken as parameters to be optimized, whereby the other variables are optimized in the same run. Temperature and feed rate between these two points are assumed to be straight lines connecting the initial and final values. The optimal values of variables obtained in the first step are taken as initial guesses for optimization. [Pg.326]

With the Nelder-Mead search, 58 full integrations and 0.6 s computer time on a VAX 6000 computer were needed to get the following result with initial and final values, standard deviation, residual plot and statistical information. [Pg.121]

Three different whey protein products extruded at the cook temperature of 75 °C resulted in varying degrees of melt texturization (Table 5.3). Among the whey proteins, WPC (WPC80) was the least texturized. Whey lactalbumin (WLAC) and WPI were both significantly (p < 0.05) more texturized, but a wider spread of texturization was observed for WPI, the initial and final values were from 28% to 94.8%, and therefore more emphasis was placed on studying WPI (Onwulata et ah, 2006). [Pg.182]

When are the simplified results valid If the work path has buffer regions at its beginning and end during which the work parameter is fixed for a time > Tshort, then the subsystem will have equilibrated at the initial and final values of p in each case. Hence the odd work vanishes because TL 0, and the probability distribution reduces to Boltzmann s. [Pg.57]

Consider a thermodynamic system with an external parameter (or constraint) A that can be used to control the state of the system. When changing the control parameter A a certain amount of work is performed on the system. According to the second law of thermodynamics the average work necessary to do that is smaller than the Helmholtz free energy difference between the two equilibrium states corresponding to the initial and final values of the constraint [33]... [Pg.265]

Entropy, which has the symbol S, is a thermodynamic function that is a measure of the disorder of a system. Entropy, like enthalpy, is a state function. State functions are those quantities whose changed values are determined by their initial and final values. The quantity of entropy of a system depends on the temperature and pressure of the system. The units of entropy are commonly J K1 mole-1. If S has a ° (5°),... [Pg.197]

Measurements include initial and final masses, and initial and final volumes. Calculations may include the difference between the initial and final values. Using the formula mass and the mass in grams, moles may be calculated. Moles may also be calculated from the volume of a solution and its molarity. [Pg.95]

You measure initial and final values, but calculate the change. [Pg.297]

The thermodynamic changes for reversible, free, and intermediate expansions are compared in the first column of Table 5.1. This table emphasizes the difference between an exact differential and an inexact differential. Thus, U and H, which are state functions whose differentials are exact, undergo the same change in each of the three different paths used for the transformation. They are thermodynamic properties. However, the work and heat quantities depend on the particular path chosen, even though the initial and final values of the temperature, pressure, and volume, respectively, are the same in all these cases. Thus, heat and work are not thermodynamic properties rather, they are energies in transfer between system and surroundings. [Pg.88]

Next, enter the following values in the INITIAL AND FINAL VALUES window ... [Pg.523]

Figure 10. Thermal stability of PET. A[rj]ocp means the difference of [rj]ocp between the initial and final value... Figure 10. Thermal stability of PET. A[rj]ocp means the difference of [rj]ocp between the initial and final value...
For the perfectly mixed continuous reactor, the CSTR, the ratio VT/ Fy only represents the mean residence time, /p,av however, it is still possible to compare the performance of the CSTR with the performance of the BR by letting the mean residence time fp av = t. Interestingly, when the reaction rate shows a positive dependence on reactants concentration, the BR is more effective than the CSTR. This is because the batch reactor experiences all the system compositions between initial and final values, whereas the CSTR operates at the final composition, where the reaction rate is smaller (under the above hypotheses). Finally, one can compare the two continuous reactors under steady-state conditions. The CSTR allows a more stable operation because of back-mixing, which however reduces the chemical performance, whereas the PFR is suitable for large heat transfer but suffers from larger friction losses. [Pg.12]

If we integrate a state function (Frame 1), the integral represents the overall change and has a definite value governed solely by the initial and final values of the given property. Thus ... [Pg.10]

In order to perform an integration f y.dx we must be able to define precisely dr (or the initial and final values for the change) i.e. integration is linked to state function properties. [Pg.10]

The energy and mass balances and rate of reaction equations are given in Table 1 together with boundary conditions, nomenclature, and values of the physical properties. Thermal conductivity and thermal diffusivity are assumed to be linear functions of the density (verified by Wong(20) and McClean(14)). The porosity and heat capacity C are linear functions of their initial and final values using the atio, eta, as follows ... [Pg.460]

When depreciation is not used in a prorated-cost sense, various meanings can be attached to the word value. One of these meanings involves appraisal of both initial and final values on the basis of conditions at a certain time. The difference between the estimated cost of new equivalent property and the appraised value of the present asset is known as the appraised depreciation. This concept involves determination of the values of two assets at one date as compared with the engineering-cost concept, which requires determination of the value of one asset at two different times. [Pg.268]

There are a number of different ways in which a heat of reaction may be defined. One of the most general definitions is the following. If a closed system containing a given number of moles Ni of N different species at a given T and p is caused to undergo an isobaric process in which the Ni are changed to prescribed final values and in which the initial and final values of T are the same, then the heat liberated by the system, — — J dQ, is the... [Pg.538]


See other pages where Initial and final values is mentioned: [Pg.460]    [Pg.83]    [Pg.342]    [Pg.687]    [Pg.236]    [Pg.16]    [Pg.41]    [Pg.47]    [Pg.295]    [Pg.256]    [Pg.111]    [Pg.129]    [Pg.60]    [Pg.254]    [Pg.460]    [Pg.600]    [Pg.77]    [Pg.292]    [Pg.11]    [Pg.30]    [Pg.93]    [Pg.36]    [Pg.52]    [Pg.211]    [Pg.168]    [Pg.264]    [Pg.12]    [Pg.92]   


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