Big Chemical Encyclopedia

Chemical substances, components, reactions, process design ...

Articles Figures Tables About

Pressure overall

MVo2 is reduced with all calcium channel antagonists primarily because of reduced wall tension secondary to reduced arterial pressure. Overall, the benefit provided by calcium channel antagonists is related to reduced MVo2 rather than improved oxygen supply. [Pg.150]

These operating conditions are necessary 1) to achieve the breakdown of the stable methane molecule and 2) to optimize the size of the reactors by reducing the volume of gases with the higher pressures. Overall, the reactions are exothermic and generate a lot of heat that has to be removed from the system. [Pg.67]

Clinical research sponsors recognize the importance of maintaining a full pipeline of innovative medical therapies. Yet they are increasingly aware of their limited resources and financial pressures. Overall, 34 billion was spent on R D in 2002. Spending as a percentage age of drug sales, however, has been declining steadily, as companies must reallocate their resources to improve their own financial performance. Whereas nearly 20% of every revenue dollar went into research and development each year between 1995 to 1998, between 1999 to 2002, 17% of sales went into R D annually. [Pg.506]

A special injection system (3) permits a certain quantity of sample (liquid or dissolved) to be introduced precisely into the pressurized overall system. Separation of the substance mixture takes place in the column (4). [Pg.169]

In Equation 2.11, is constant for a particular valve. Other control valve vendors also have expressions for APaHow that are functions of vapour and critical pressures. Overall, this results in the following liquid sizing procedure ... [Pg.43]

Reactors in the overall process. It should be emphasized that many considerations other than those represented in Figs. 2.9, 2.10, and 2.11 also influence the decision on the choice of reactor. Safety considerations, operating pressure, materials of construction, etc. have a considerable effect on the outcome. [Pg.64]

It must be emphasized that it is not worth expending any effort optimizing pressure, feed condition, or reflux ratio until the overall heat-integration picture has been established. These parameters very often change later in the design. [Pg.78]

No attempt should be made to optimize pressure, reflux ratio, or feed condition of distillation in the early stages of design. The optimal values almost certainly will change later once heat integration with the overall process is considered. [Pg.92]

Steam costs vary with the price of fuel. If steam is only generated at low pressure and not used for power generation in steam turbines, then the cost can be estimated from local fuel costs assuming a boiler efficiency of around 75 percent (but can be significantly higher) and distribution losses of perhaps another 10 percent, giving an overall efficiency of around 65 percent. [Pg.408]

The above example is a simple one, and it can be seen that the individual items form part of the chain in the production system, in which the items are dependent on each other. For example, the operating pressure and temperature of the separators will determine the inlet conditions for the export pump. System modelling may be performed to determine the impact of a change of conditions in one part of the process to the overall system performance. This involves linking together the mathematical simulation of the components, e.g. the reservoir simulation, tubing performance, process simulation, and pipeline behaviour programmes. In this way the dependencies can be modelled, and sensitivities can be performed as calculations prior to implementation. [Pg.342]

If Other fall-off broadening factors arising m unimolecular rate theory can be neglected, the overall dependence of the rate coefficient on pressure or, equivalently, solvent density may be represented by the expression [1, 2]... [Pg.848]

In practical applications, gas-surface etching reactions are carried out in plasma reactors over the approximate pressure range 10 -1 Torr, and deposition reactions are carried out by molecular beam epitaxy (MBE) in ultrahigh vacuum (UHV below 10 Torr) or by chemical vapour deposition (CVD) in the approximate range 10 -10 Torr. These applied processes can be quite complex, and key individual reaction rate constants are needed as input for modelling and simulation studies—and ultimately for optimization—of the overall processes. [Pg.2926]

Chemical systems spontaneously react in a fashion that lowers their overall free energy. At a constant temperature and pressure, typical of many bench-top chemical reactions, the free energy of a chemical reaction is given by the Gibb s free energy function... [Pg.137]

Finally, probably the most important item affecting an ion beam is the overall gas pressure inside the instrument. Generally, a mass spectrometer operates under a high vacuum, in which... [Pg.372]

Statistically, in a high-pressure region, an ion will be struck by neutral molecules randomly from all angles. The ion receives as many collisions from behind as in front and as many collisions from one side as from the other. Therefore, it can be expected that the overall forward motion of the ion will be maintained but that the trajectory will be chaotic and similar to Brownian motion (Figure 49.4b). Overall, the ion trajectory can be expected to be approximately along the line of its initial velocity direction, since it is still influenced by the applied potential difference V. [Pg.375]


See other pages where Pressure overall is mentioned: [Pg.42]    [Pg.147]    [Pg.363]    [Pg.291]    [Pg.224]    [Pg.1353]    [Pg.147]    [Pg.412]    [Pg.197]    [Pg.331]    [Pg.303]    [Pg.563]    [Pg.42]    [Pg.147]    [Pg.363]    [Pg.291]    [Pg.224]    [Pg.1353]    [Pg.147]    [Pg.412]    [Pg.197]    [Pg.331]    [Pg.303]    [Pg.563]    [Pg.55]    [Pg.1]    [Pg.47]    [Pg.109]    [Pg.143]    [Pg.322]    [Pg.53]    [Pg.79]    [Pg.81]    [Pg.928]    [Pg.2522]    [Pg.13]    [Pg.227]    [Pg.237]    [Pg.266]    [Pg.69]    [Pg.113]    [Pg.41]    [Pg.87]    [Pg.343]    [Pg.231]   
See also in sourсe #XX -- [ Pg.20 , Pg.23 ]




SEARCH



A15-4 Overall sizing of a structural cage around the pressure vessel

Model for the overall pressure drop

Overall pressure drop

Overall pressure drop calculated

Overall relationship between mass flow and pressure difference

Palladium overall pressure

Variation of Equilibrium Constant, K, with Overall Total Pressure

© 2024 chempedia.info