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Process fluctuations

Design nd Operation. The destruction efficiency of a catalytic oxidation system is determined by the system design. It is impossible to predict a priori the temperature and residence time needed to obtain a given level of conversion of a mixture in a catalytic oxidation system. Control efficiency is determined by process characteristics such as concentration of VOCs emitted, flow rate, process fluctuations that may occur in flow rate, temperature, concentrations of other materials in the process stream, and the governing permit regulation, such as the mass-emission limit. Design and operational characteristics that can affect the destmction efficiency include inlet temperature to the catalyst bed, volume of catalyst, and quantity and type of noble metal or metal oxide used. [Pg.506]

As mentioned, intermediate storage dampens the effects of process fluctuations, reduces process cycle times, and increases flexibility in process scheduling. It is intuitively clear that the size and location of intermediate storage will influence the plant performance. Below, a basic analysis will be given for single-product plants. [Pg.482]

The injection molding screw diameter chosen should be matched to the part s shot volume, which - as a general rule - should be not more than about 70% of the screw s theoretical swept volume. If the screw (diameter) chosen is too small, the swept volume will tend towards the shot volume, leaving insufficient leeway for correcting process fluctuations. On the other hand, if the injection unit is too large, only a small part of the swept volume will be employed per shot and the remainder of the melt in the barrel will possibly be exposed to too much heat. Furthermore, even small variations in the screw stroke would cause considerable variation in the shot weight. [Pg.273]

Uncertainties in costs can have a major impact in evaluating the feasibility of a process. Fluctuations of product prices are easier to manage, because they are regulated by the market. The prices of raw materials are more uncertain. These should consider the transportation costs, whose contribution is significant for remote sources. Internal prices of commodity chemicals are much more advantageous on an integrated platform. [Pg.246]

The service conditions for which the vessel must be suitable. These inevitably include normal and design figures, to allow for process fluctuations. The design pressure allows for the operation of safety devices in a way that is prescribed by the code. [Pg.227]

The process limits chosen for the validation of the cycle limits should be wide enough to guarantee that the target cycle is sufficiently robust to withstand the small process fluctuations that occur routinely in industrial freeze-dryers. For example, if the programmed shelf temperature is 30°C... [Pg.567]

SPC allows normal equipment and process fluctuations to be considered over a longer period of time. To warrant adjustment, sample results must demonstrate a downward or upward trend away from the key target setpoints. [Pg.344]

During a stable state of manufacture, the amount of fresh materials should be equivalent to that of the products. Therefore, the proportion of the fresh material, returned material and the residue is commonly unchanged. However, if the production process fluctuates or has accident, the balance of material will be broken. As a result, the change in the proportion occurs, which affects the quality of the product. [Pg.315]

In any chemical process there are always some fluctuations, either in conditions, or in feed properties. Consequently, there will be some fluctuations in product quality as well. In batch processes, one product batch may not be exactly the same as the next one. In continuous processes, fluctuations in process conditions are difficult to avoid. These will generally result in fluctuations in product quality, though any backmixing in the process will reduce the variations in the al product properties. In practice, there are two kinds of restrictions in quality fluctuations ... [Pg.312]

It is traditional industrial practice to move each MV and DV individually. The magnitudes of the moves should be carefully chosen, because too small a move may result in the step responses being obscured by normal process fluctuations and measurement noise. On the other hand, too large a change may result in an output constraint violation or nonlinear process behavior that cannot be accurately described by a linear model. [Pg.407]

What factors in the polymerization reaction are responsible for the sequence structure of the polymer When the sequence distribution of the polymer chain is completely characterized, and when proper control has been exercised, it should be possible to relate the structure to the basic polymerization process. In the ideal circumstance, discovering the relationships between the chemistry and the structure is quite easy. However, in the real case, it is quite difficult due to process fluctuations and experimental error in the measurements. In every case, it is possible to gain some insight into the nature of the polymerization process. Here, we will demonstrate the ideal case and later point the direction for the cases observed in the real world. [Pg.21]


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