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Reaction heat calculation

For instance, it has been shown for PEO (oligomer) — PMA (polymer) interaction that the reaction heat calculated per monomer unit does not depend on the DP of the oligomer26). Then the probability of oligomer-polymer association is... [Pg.146]

Below, it is presented the reaction heat calculated for two DOSG reactions that can elucidate the character of the 0-0 bonding in this group. In the triplet state, the distance between the oxygen atoms in the F2Si(0 )(0 ) molecule increases to 2.5 A i.e., the chemical bond between these atoms is disrupted. The G2(MP2) energy of the triplet state proved to be... [Pg.300]

The magnitude of the reaction is an index of the potential of a hazard. The screening tests for the magnitude of a reaction include reaction heat calculation, reaction calorimetry and sealed cell differential scanning scanning calorimetry (SC—DSC). [Pg.18]

Heats of reaction Heats of reaction can be obtained as differences between the beats of formation of the products and those of the starting materials of a reaction. In EROS, heats of reaction arc calculated on the basis of an additivity scheme as presented in Section 7.1. With such an evaluation, reactions under thermodynamic control can be selected preferentially (Figure 10.3-10). [Pg.552]

Enthalpy of reaction and standard entlialpy of reaction are not always employed in engineering reaction/combustioii calculations. The two other terms tliat hai C been used are tlie gross (or liighcr) heating value and tlie net (or lower) heating value. These arc discussed later in this Section. [Pg.118]

The production of ammonia is of historical interest because it represents the first important application of thermodynamics to an industrial process. Considering the synthesis reaction of ammonia from its elements, the calculated reaction heat (AH) and free energy change (AG) at room temperature are approximately -46 and -16.5 KJ/mol, respectively. Although the calculated equilibrium constant = 3.6 X 108 at room temperature is substantially high, no reaction occurs under these conditions, and the rate is practically zero. The ammonia synthesis reaction could be represented as follows ... [Pg.144]

Bomb calorimeter. The heat flow, q, for the reaction is calculated from the temperature change multiplied by the heat capacity of the calorimeter, which is determined in a preliminary experiment... [Pg.202]

Before energy balance is calculated, we need to make mass balance. Figure 9.1 shows the material balance for ethanol and glycerol fermentation. Put simply, mass into the system is equal to mass out of die system. The mass of carbon dioxide is calculated by adding mass of dry cell, mass of glycerol, mass of edianol and mass of water at product stream and then subtracting die sum from die feed stream. As a result, die mass of carbon dioxide is defined. The heat of the reaction is calculated by the following equation ... [Pg.231]

Thermod5mamics is a fundamental engineering science that has many applications to chemical reactor design. Here we give a summary of two important topics determination of heat capacities and heats of reaction for inclusion in energy balances, and determination of free energies of reaction to calculate equihbrium compositions and to aid in the determination of reverse reaction... [Pg.226]

On the other hand, Arnett and his coworkers have reported both the enthalpies of the protonation (AHJ and the hydrogen bond (AHf) for acid-base reactions. They calculated Hj by measuring the association constants for the proton transfer (ionization) in a number of bases by using FSO3H as the acid and determined Ai/j by calorimetric measurements of the heat of dissolution of P-FC6H4OH in various hydrogen bond acceptors, including sulphoxides, in They have also tried to correlate and... [Pg.558]

Figure 5.4-35. Baseline and reaction heat flows calculated during heating and isothermal periods (reprinted with permission from Landau et al. (1994). Copyright (1994) American Chemical Society). Figure 5.4-35. Baseline and reaction heat flows calculated during heating and isothermal periods (reprinted with permission from Landau et al. (1994). Copyright (1994) American Chemical Society).
The temporal reaction heat flow data may be graphically manipulated to reveal the overall second order dependence in a quantitative manner. Reaction heat flow is converted to reaction rate using eq. (1), and the concentration of the limiting substrate 5 may be calculated according to eq. (3). From these calculations we may constract the plot in Figure 50.2b of reaction rate vs. [5]. The reaction is known to be first order in both [5] and [6] these plots reveal the curvature typical of overall second order kinetics. [Pg.449]

The total heat requirement is thus around 599.98 kj, which is about 548.81 kj more than the heat available from the reaction. This calculation, however, does not take into account the inevitable heat losses due to the nonadiabatic conditions in the reactor. An estimate of these heat losses can be made by considering the industrial practice for aluminothermic chromium metal production. The charge is preheated to about 500 °C before loading into the aluminothermic crucible. This operation adds about 96.65 kj (i.e., 48.9 cal deg-1 475) of heat to the system. It, therefore, appears that around 41.84 kj (96.65 kj - 54.81 kj) of heat is lost due to radiation and convection for every mole of chromium sesquioxide reduced to the metal by the aluminothermic process. [Pg.392]

The equipment requirements that we have determined are well within the realm of technical feasibility and practicality. The heat transfer requirements are easily attained in equipment of this size. The fact that some of the heat transfer requirements are positive and others negative indicates that one should probably consider the possibility of at least partial heat exchange between incoming cold feed and the effluent from the second or third reactors. The heat transfer calculations show that the sensible heat necessary to raise the cold feed to a temperature where the reaction rate is appreciable represents a substantial fraction of the energy released by reaction. These calculations also indicate that it would be advisable to investigate... [Pg.359]

Heating aluminium powder with carbon tetrachloride, chloromethane or carbon tetrachloride-chloroform mixtures in closed systems to 152°C may cause an explosion, particularly if traces of aluminium chloride are present [1], A mixture of carbon tetrachloride and aluminium powder exploded dining ball-milling [2], and it was later shown that heavy impact would detonate the mixture [3], Mixtures with fluorotrichloroethane and with trichlorotrifluoroethane will flash or spark on heavy impact [4], A virtually unvented aluminium tank containing a 4 1 2 mixture of o-dichlorobenzene, 1,2-dichloroethane and 1,2-dichloropropane exploded violently 7 days after filling. This was attributed to formation of aluminium chloride which catalysed further accelerating attack on the aluminium tank [5], An analysis of the likely course of the Friedel-Crafts reaction and calculation of the likely heat release (29.1 kJ/mol) has been published [26],... [Pg.32]

The enthalpy released or absorbed in a process can be described by Equation 6 for constant volume conditions and an isobaric process. While determining the safety subindex Irm the heat release of the main reaction is calculated for the total reaction mass (i.e. both the reactants and diluents are included) to take account the heat capacity of the system which absorbs part of the energy released ... [Pg.64]

The subindex Irs of the heat of side reactions is determined in the similar way as the subindex Irm for the main reaction. The heat release for each possible side reactions is calculated according to Equation 6 for the full reaction mass including diluents. The same safety scores that were used for the main reaction are utilized also for the side reations (Table 9). The greatest heat of reaction value of all side reactions is used for determining the value of the Irs. [Pg.65]

The heats of main and side reactions are calculated by Equation 6 for the whole liquid inventory. For the main reaction the heat is about 300 J/g. The formation of propionic acid gives the maximum heat of side reaction which is about 1000 J/g. The most dangerous chemical in this process is carbon monoxide which appears in the reaction section. As a construction material stainless steel and Hastelloy are both needed. Hastelloy gives the score value 2. Most dangerous chemical interaction may appear between methanol and hydriodic acid in the reaction section resulting heat formation and even a fire, which gives the score 4. [Pg.94]

The various solution methods were applied to a set of measurements taken at different reactor conditions. Table 5 gives the data used for the reconciliation. The value corresponding to the specific heat is an effective specific heat, calculated from rigorous simulations using the Phenics package, and takes into account the heat of reaction. [Pg.254]

Phosphorus trifluoride has been used as a reactant gas in calorimetry to act as a fluorine acceptor rather than donor. The heats of formation of xenon fluorides have been calculated from the reaction heats (137) ... [Pg.19]

Because the heat of formation of NH2C12+ is not known, this chemical shift cannot be calculated from available thermodynamic data. However, quantum mechanical methods have been used to estimate the energy of this and similar reactions. These calculations are attractive for at least three reasons ... [Pg.158]

In many reactions, AH and AG are similar in magnitude (see B1, for example). This fact is used to estimate the caloric content of foods. In living organisms, nutrients are usually oxidized by oxygen to CO2 and H2O (see p. 112). The maximum amount of chemical work supplied by a particular foodstuff (i. e., the AG for the oxidation of the utilizable constituents) can be estimated by burning a weighed amount in a calorimeter in an oxygen atmosphere. The heat of the reaction increases the water temperature in the calorimeter. The reaction heat can then be calculated from the temperature difference AT. [Pg.20]

This means that if it is desired to calculate the effective work potential of an explosive, it is necessary to calculate.or assume the water-gas reaction constant of the detonation products behind the reaction zone, calculate the heat liberated by the decomposition reaction at this equilibrium (Qc) and calculate.the pressure developed on the basis of the gaseous products. A simple approximation of this value can be arrived at by multiplying the heat value Qc by the volume of gas formed at the maximum temperature but expressed as volume at standard temperature and pressure (Vc)... [Pg.730]

In an explosive reaction, heat and gases are liberated. The volume of gas V and the heat of explosion Q can both be calculated independently but these values can be combined to give the value for the explosive power as shown in Equation 5.12. [Pg.90]

O-Nitration is an exothermic reaction. Approximate calculations which have been made (Kagawa [70] Calvet and Dhers-Pession [71]) on the basis of esterifying methyl alcohol and cellulose indicate that the esterification of one hydroxyl group is accompanied by the development of 2 0.2 kcal of heat (see pp. 46, 147). [Pg.20]


See other pages where Reaction heat calculation is mentioned: [Pg.216]    [Pg.385]    [Pg.558]    [Pg.229]    [Pg.31]    [Pg.381]    [Pg.7]    [Pg.348]    [Pg.103]    [Pg.192]    [Pg.467]    [Pg.374]    [Pg.216]    [Pg.32]    [Pg.90]    [Pg.96]    [Pg.219]    [Pg.189]    [Pg.236]    [Pg.37]    [Pg.12]    [Pg.77]    [Pg.200]    [Pg.627]    [Pg.137]   
See also in sourсe #XX -- [ Pg.89 , Pg.90 , Pg.91 ]




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