Energy process requirements

The observation of primary reaction products of high activation energy processes requires both high temperatures and short residence times of the pyrolysate in the hot zone. Flash vacuum pyrolysis performed in proximity to the ion source of a mass spectrometer in many cases satisfies these criteria however, the design of the pyrolyser plays an important role in the overall performance of the Py-MS... 

Energy efficiency of the process. If the process requires a furnace or steam boiler to provide a hot utility, then any excessive use of the hot utility will produce excessive utility waste through excessive generation of CO2, NO, SO, particulates, etc. Improved heat recovery will reduce the overall demand for utilities and hence reduce utility waste. 

This thermal ionization process requires fiiament temperatures of about 1000-2000°C. At these temperatures, many substances, such as most organic compounds, are quickiy broken down, so the ions produced are not representative of the structure of the original sample substance placed on the filament. Ionization energies (1) for most organic substances are substantially greater than the filament work function (( )) therefore 1 - ( ) is positive (endothermic) and few positive ions are produced. 

The vaporization process requires energy both to overcome intermolecular attractions and to push back the surroundings to make room for the vapor. The quantity AU measures the former, while AH takes both into account. In connection with the mixing process, it is the contribution of intermolecular forces which we seek to evaluate, so AU is a more suitable measure of this quantity. 

Ethylbenzene Separation. Ethylbenzene [100-41-4] which is primarily used in the production of styrene, is difficult to separate from mixed Cg aromatics by fractionation. A column of about 350 trays operated at a refluxTeed ratio of 20 is required. No commercial adsorptive unit to accomplish this separation has yet been installed, but the operation has been performed successhiUy in pilot plants (see Table 5). About 99% of the ethylbenzene in the feed was recovered at a purity of 99.7%. This operation, the UOP Ebex process, requires about 40% of the energy that is required by fractional distillation. 

Active Transport. Maintenance of the appropriate concentrations of K" and Na" in the intra- and extracellular fluids involves active transport, ie, a process requiring energy (53). Sodium ion in the extracellular fluid (0.136—0.145 AfNa" ) diffuses passively and continuously into the intracellular fluid (<0.01 M Na" ) and must be removed. This sodium ion is pumped from the intracellular to the extracellular fluid, while K" is pumped from the extracellular (ca 0.004 M K" ) to the intracellular fluid (ca 0.14 M K" ) (53—55). The energy for these processes is provided by hydrolysis of adenosine triphosphate (ATP) and requires the enzyme Na" -K" ATPase, a membrane-bound enzyme which is widely distributed in the body. In some cells, eg, brain and kidney, 60—70 wt % of the ATP is used to maintain the required Na" -K" distribution. 

An important by-product of most energy technologies is heat. Few energy conversion processes are carried out without heat being rejected at some point in the process stream. Historically, it has been more convenient as weU as less cosdy to reject waste heat to the environment rather than to attempt significant recovery. The low temperatures of waste heat in relation to process requirements often make reuse impractical and disposal the only attractive alternative (see Process energy conservation). 

During emulsification new surfaces are created between the two phases. Such a process requires energy the surface free energy, numerically identical to the easily measured surface tension, reflects this amount. 

For the same production capacity, the oxygen-based process requires fewer reactors, all of which operate in parallel and are exposed to reaction gas of the same composition. However, the use of purge reactors in series for an air-based process in conjunction with the associated energy recovery system increases the overall complexity of the unit. Given the same degree of automation, the operation of an oxygen-based unit is simpler and easier if the air-separation plant is outside the battery limits of the ethylene oxide process (97). 

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