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ASSUMED PRODUCTS

As was noted in Chapters II and IV, the available enthalpy for a given propellant combination is determined primarily by the product species which are formed in the combustion of the propellants. The failure to include a significant product specie [Pg.128]

The identification of probable combustion product species for all but the most exotic propellant combinations has been well established. In conjunction with machine calculations which consider large numbers of possible product species, the likelihood of Introducing error into equilibrium performance calculations through omission of significant product species is small. With the completion of the JANAF Thermochemical Tables (18) which currently contain some 800 possible species and continues to be expanded, the task of taking all possible significant product species into consideration is well defined, although not necessarily simple. The problem of identification of probable species has been reduced to the identification of possible species which for most propellant combination is a routine task. [Pg.131]


For a single-product plant the calculation of equipment sizes is straightforward. First the limiting cycle time ti is determined using Eqn. (7.4-14) or Gantt charts. The batch size is then evaluated for an assumed production capacity Q and available production time H ... [Pg.477]

As discussed in previous sections, however, the routes from methanol to more complex species are not well mapped out, and those reactions that have been utilized by modelers may not have the assumed products. [Pg.39]

A quite different approach to the detonation product state has been to treat it as solidlike. Jones and Miller6 performed equilibrium calculations on TNT with this idea in mind. They used an equation in which the volume was a virial expansion in the pressure. Other solidlike equations are cited in Ref. 2, but these have mostly been used for computing the state parameters with an assumed product state. The modified Kistia-kowsky-Wilson equation of interest to us liere appears to be one of several possible compromises between the hard-sphere molecule approach and the solid state approach. [Pg.2]

It is apparent that Cr(C2C>4)3 3, m-Cr(OH2)2(0204)2 , and Cr(0H2)4C2044 react smoothly with cerium(IV) in acidic-sulfate media, 1 mole of oxalate being oxidized for each 2 moles of cerium(IV) consumed. The observations made are consistent with the view that the three reactions proceed, at least initially, according to the stoichiometries represented by the respective Reactions 3,1, and 2. The initial absorbances of reactant solutions (values obtained by extrapolation of measured absorbances to zero time) agree well with the values calculated, on the basis of Beer s law, from the absorptivity coefficients of the components. Further, as the reactions in 1.83Af sulfuric acid proceed, the absorbances of the solutions move toward the values expected for the assumed products at rates which demonstrate the reactions are first order in cerium(IV) and complex—see, for example, Figure 2. We thus find no indication that reaction intermediates contribute measurably to the absorbances of reactant solutions, or that reaction conditions cause the rapid equilibration of any of the oxalato complexes with other species... [Pg.240]

The fatty acid composition of these milk products with different lipid levels can be calculated if the lipid level is known. Assuming product 1 is listed in this table and product 2 is the same product with a different lipid level ... [Pg.355]

As an example of a simple limit calculation, assume product A is manufactured and the equipment is subsequently cleaned before manufacturing other products. Assuming that product A will ultimately be used as an oral tablet and that the smallest therapeutic dose is 100 mg, a safety factor of 1/1000 is applied. This means that the next product could safely contain not more than... [Pg.529]

There are two ways to improve the accuracy in order to obtain solutions to almost any degree of accuracy. The first is via the so-called self-consistent field-Hartree-Fock (SCF-HF) method, which is a method based on the variational principle that gives the optimal one-electron wave functions of the Slater determinant. Electron correlation is, however, still neglected (due to the assumed product of one-electron wave functions). In order to obtain highly accurate results, this approximation must also be eliminated.6 This is done via the so-called configuration interaction (Cl) method. The Cl method is again a variational calculation that involves several Slater determinants. [Pg.47]

Other possible variables, such as the combustion or initial temperature, assumed products, thermodynamic data, and induction enthalpy, while not generally available as design parameters, do affect predicted and/or delivered performance. [Pg.119]

It assumes product and reactants have the same molar volume. [Pg.175]

Spectroscopic evidence on D SO) in the diatomic molecule leads to 4 00 or 5 18 eV. Herzberg 217 favours the lower, Gaydon the higher. The result depends on the assumed products of a predissociation. [Pg.218]

Z)(G10) in the diatomic molecule depends upon the spectroscopic observation of bands almost to a convergence limit of 4 70 eV. Depending on the assumed products, Z)(G10) =63 5 or 60 9 kcal220. 3Q5, Gaydonprefers the higher. [Pg.218]

Herzberg2i7 gives 2 73 or 3 45 eV, depending on assumed products at convergence limit. Gaydon prefers the lower value. [Pg.222]

An interesting feature of the assumed products 4.203 and 4.204 is that they contain what are formally cyclic-conjugated, 20 Tc-electron pathways. Nonetheless, the recorded H NMR spectra served to reveal resonances that were shifted to a... [Pg.244]

A natural gas contains 85% methane and 15% ethane by volume. The heats of combustion of methane and ethane at 25 C and 1 atm with water vapor as the assumed product are given below ... [Pg.465]

The thorium requirement per country may be compared with the assumed production in each country, shown in Fig. 5.59. It is determined by assuming that the world production of thorium matches the world requirements, and that each country produces in proportion to its total thorium resources, as estimated in Fig. 5.51. [Pg.307]

The heat of reaction is removed by excess ethylene leaving the reactor as an overhead stream. Ethylene is cooled and recycled to the reactor along with fresh ethylene feed. The reaction is conducted under an oxygen-free, anhydrous environment to prevent deactivation of the catalyst. The reaction is maintained at 80°C in order to minimize the potential isomerization of butene-1 to butene-2. Ethylene conversion is about 20 percent per pass and the assumed product yield from this process are 95 percent butene-1 and 5 percent butene-2. [Pg.517]

Tables 3 and 4 detail raw material and energy inputs to the plywood producing process, as well as product and co-product outputs from the process shown in Table 5 are all emissions to air, water, and ground. Results were generated in SimaPro 5.0.9 version 5 LCA software with the Franklin Database employed for LCI on fuel use, and electricity production burdens assuming production serving the Pacific Northwest region. Data shown in Table 5 are allocated total emissions, which include emissions for the production and delivery of electricity, fuel, and adhesives. Emissions for production of the phenolic adhesive were obtained from Athena . All other inputs and outputs were based on manufacturing plant surveys. Tables 3 and 4 detail raw material and energy inputs to the plywood producing process, as well as product and co-product outputs from the process shown in Table 5 are all emissions to air, water, and ground. Results were generated in SimaPro 5.0.9 version 5 LCA software with the Franklin Database employed for LCI on fuel use, and electricity production burdens assuming production serving the Pacific Northwest region. Data shown in Table 5 are allocated total emissions, which include emissions for the production and delivery of electricity, fuel, and adhesives. Emissions for production of the phenolic adhesive were obtained from Athena . All other inputs and outputs were based on manufacturing plant surveys.
As it happened, the global oil business did not grow nearly as much as Marchetti had predicted in fact, it declined. In late 1998, the total annual dollar volume of the global oil business was reckoned to be in the range of 380-460 billion, assuming production of about 38 billion barrels per day... [Pg.261]

Note. Fidler et al. 1 had attempted to prepare methylenemagnesium bromide and iodide by reaction of the halides with magnesium but found the assumed products to have slight activity towards benzaldehyde. The later Italian workers achieved success by use of the evidently more reactive magnesium amalgam. [Pg.141]

Use of these equations is illustrated for the fission-product decay chain of mass number 92 considered in Sec. 3.2. Assume production of Sr, the first nuclide of the chain, at a constant rate P = 1/h for a period of 3 h (T = 3 h), followed by several hours of radioactive decay with P = 0. The amounts of Sr and Y, calculated by applying Eqs. (2.37) and (2.38), respectively, are shown in Fig. 2.9. The amount of stable Zr during the period of F=0 is obtained from the material-balance equation ... [Pg.42]

For these assumed products, the distillate temperature is obtained from a dewpoint calculation as 11.5°F (-11.4°C) and the bottoms temperature is obtained from a bubble-point calculation as 164.9°F (73.8 C). The dew-point calculation also gives values of (jCi)o, from which values of (y,)i for the top stage of the enricher are obtained from a... [Pg.633]

A recent review of detonation theory is given elsewhere [12]. Models of the phenomenon envisage a detonation wave propagating into unreacted material with a sharp discontinuity in temperature and pressure at the detonation front. A reaction zone of a millimeter or smaller dimensions and yielding the equilibrium quantities of reaction products at high temperature and pressure abuts the up-stream side of the front. Using macroscopic hydrodynamic-thermodynamic theory, the energy released, and an equation of state for the assumed products, detonation velocities, pressures, and temperatures may be calculated in certain cases. [Pg.5]

Understanding our long-term energy needs necessitates a review of reserves and estimates of reserves by fuel type. How long these reserves may last may be considered using a simple measure of reserve size, the reserve-to-production (R P) ratio, or a more complex method, the Hubbert Peak analysis. This analysis assumes production from oil fields basically follows a bell curve, where production increases until the maximum production rate is reached when half the resource has been... [Pg.47]

Irradiation of 3,3,5-trimethyl-2(3fl)-thiophenone leads to the thiete (269) by decarbonylation (Equation (21)) <89AG(E)1499>. It was reali later, however, that the photolytic decarbonylation of such 2-(3. -thiophenones is more complex than initially assumed. Products depend on the substitution pattern as well as on the actual substituents. A detailed mechanistic route has been suggested for the formation of thietes, thiophenes, thiapyrans, etc. from the excited state of the substrate <92CB231l>. [Pg.540]


See other pages where ASSUMED PRODUCTS is mentioned: [Pg.352]    [Pg.357]    [Pg.24]    [Pg.607]    [Pg.128]    [Pg.154]    [Pg.92]    [Pg.35]    [Pg.237]    [Pg.159]    [Pg.473]    [Pg.443]    [Pg.376]    [Pg.352]    [Pg.388]    [Pg.189]    [Pg.124]    [Pg.319]    [Pg.327]    [Pg.393]    [Pg.55]    [Pg.291]    [Pg.79]    [Pg.141]    [Pg.22]   


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