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Specific Equipment

As previously mentioned, when the rate coefficient of the reaction has to be determined, it is recommended to eliminate mass transfer effects as much as possible. Also, to get rid of the problem of the interfacial area, specific equipment with known Ay has been devised. The wetted wall column was used in early studies to determine the kinetics of the reaction itself. Care has to be taken to have a laminar film (Re 250-400) and to avoid ripples that increase the interfacial area. In a film flowing down a vertical tube of a diameter t/, the velocity u at any depth / from the interface is given by [Pg.359]

In classical versions, both the gas and the liquid generally flow countercurrently. In more recent versions such as those shown in Fig. 6.5.4-1 only the liquid flows and the amount of gas absorbed as a function of time is followed by means of a gas buret and a soap film meter. From the lowering of the soap meniscus, the amount of A that is absorbed may be calculated. Dividing this amount by the elapsed time yields the rate of absorption. Looking now at the jet, with its known Ay and contact time between gas and liquid, t, an amount is absorbed  [Pg.359]

The average rate of absorption is Q/ F. This is exactly the quantity measured by the gas buret and soap film meter, so that [Pg.359]

Another equipment frequently used for rapid reactions is the laminar jet in which the liquid velocity is uniform, so that the contact time is nothing but the height/velocity ratio. The contact time can be varied from 0.001 s to 0.1 s by varying the liquid rate from the Jet. Such equipment, an example of which is shown in Fig. 6.5.4-Z, has been used by Nysing et al. [1959] and Sharma and Danckwerts [1963]. [Pg.360]

Laminar jet with soap-film gas flow meter. After Beek (1968). [Pg.361]


Some variables often have dependencies, such as reservoir porosity and permeability (a positive correlation) or the capital cost of a specific equipment item and its lifetime maintenance cost (a negative correlation). We can test the linear dependency of two variables (say x and y) by calculating the covariance between the two variables (o ) and the correlation coefficient (r) ... [Pg.165]

Table 3 lists typical failure rate data for a variety of types of process equipment. Large variations between these numbers and specific equipment can be expected. However, this table demonstrates a very fundamental principle the more compHcated the device, the higher the failure rate. Thus switches and thermocouples have low failure rates gas—Hquid chromatographs have high failure rates. [Pg.476]

The numbers computed usiag this approach are only as good as the failure rate data for the specific equipment. Frequendy, failure rate data are difficult to acquire. For this case, the numbers computed only have relative value, that is, they are useful for determining which configuration shows iacreased reUabiUty. [Pg.477]

Once the fault tree is constructed, quantitative failure rate and probability data must be obtained for all basic causes. A number of equipment failure rate databases are available for general use. However, specific equipment failure rate data is generally lacking and. [Pg.2276]

Is the equipment to be used for manufacturing ABC Co. products greater than ten years old (note specific equipment) ... [Pg.155]

Under certain situations, for specific equipment configurations, it may be possible to safely operate above the NFPA limit of 60% of the LFL. If this method of operation is to be considered, system-specific test data should be generated which demonstrates dial the combusdble concentradon can be controlled in a safe manner, and only then in consultadon with appropriate company and (where required) regulatory authorities. [Pg.36]

Data cell A unique compartment of the taxonomy in which data are stored, defined by specific equipment, service and failure descriptions. [Pg.285]

Figure 7-15. Safety valve protecting specific equipment operation. Figure 7-15. Safety valve protecting specific equipment operation.
The transport of pre-boiler corrosion debris to the boiler section includes the oxides of iron, copper, nickel, zinc, and chromium and results from the corrosion of pre-heaters and condensers, and the like. Specifically, equipment components variously fabricated from admiralty brass, aluminum brass, cupronickels, and stainless steels are most affected. [Pg.212]

The fundamental technology for cleaning has changed little over the years (especially for smaller, lower pressure boilers), but irrespective of the degree of sophistication or the specific equipment to be cleaned,... [Pg.629]

By considering the theoretical and applied aspects of electrochemistry jointly, one can more readily comprehend their intimate correlation and gain a fuller insight into this science as a whole. The applied part of the book outlines the principles of some processes and illustrates their practical significance but does not describe technical or engineering details or the design of specific equipment, as these can be found in speciahzed treatises on applied electrochemistry. [Pg.739]

The specific equipment used for each step depends on the incinerator type and the physical and chemical characteristics of the wastes the incinerator is designed to bum. Wastes are fed into the incinerator in batches or in a continuous stream. Liquid wastes are often pumped and atomized into fine droplets that bum more easily. Solid wastes may be fed into the incinerator in bulk or in containers using a conveyer, a gravity system, or a ram feeder.8... [Pg.956]

The selection of optimum inspection methods and frequencies for high temperature hydrogen attack in specific equipment or applications is the responsibility of the user. The information below and in Tables D-1 and D-2 are intended to assist the user in making such decisions. [Pg.40]

The chemical engineering undergraduate spends most of his time sizing equipment. Usually in the problems assigned the type of equipment to be used is specified. For a distillation column the student would be told whether it is a bubble cap, a sieve plate, a valve tray, a packed column, or something else, and then asked to size it for a desired separation. In other cases he would be given the size of the specific equipment and asked to determine what the output would be for a given input. [Pg.106]

These accidents actually occurred. Anyone familiar with the specific equipment or procedures will appreciate the lessons learned. [Pg.535]

When an IVD is developed as a kit or system to be used with specific equipment and is sold to multiple laboratories, it is considered a device in interstate commerce and is subject to premarket review. When the IVD is a novel test, premarket approval (PMA) will be based on the analytical and clinical validation that will determine whether the test is safe and effective for clinical use. When there is evidence that the IVD is substantially equivalent to a legally marketed device, FDA clears such tests under section 510(k) of the Device Amendments to the Food, Drug and Cosmetic Act. The necessary level of evidence and requirements are described in more detail below. [Pg.109]

Fuel costs vary significantly by region, and the numbers in this row assume minimum fuel cost. For a specific application, contact manufacturers of specific equipment to get an idea of fuel consumption. Contact local gas, diesel, or other fuel supplier (or see Department of Energy databases) to get an estimate of what fuel will cost. [Pg.293]

Experimental data can be obtained from the DSC and from reaction calorimeters for the conditions of the desired reactions, and from the DSC, the ARC, the Reactive System Screening Test (RSST—Fauske and Associates) and from the Vent Size Package (VSP) for conditions allowing undesired reactions. The pressure effect can be studied using the ARC or DIERS methods. From the results of these tests, the rate of temperature rise and the maximum acceptable conditions for specific equipment can be calculated. The same holds for the pressure rise rate. [Pg.93]

Application of plastic films for soil solarization requires specific equipments and time-spending procedures, as well as the plastic disposal at crop end can be expensive and represent a serious environmental problem (Parish et al. 2000). [Pg.227]

Fixed foam water deluge spray systems for general area or specific equipment. [Pg.214]

A report by the National Renewable Energy Laboratory, studied 65 distributed energy projects and found that various technical, business practice, and regulatory barriers can block distributed generation projects from being developed. These barriers include lengthy approval processes, project-specific equipment requirements and high standard fees. [Pg.228]


See other pages where Specific Equipment is mentioned: [Pg.30]    [Pg.43]    [Pg.123]    [Pg.1915]    [Pg.2563]    [Pg.344]    [Pg.80]    [Pg.231]    [Pg.541]    [Pg.504]    [Pg.1]    [Pg.343]    [Pg.343]    [Pg.369]    [Pg.947]    [Pg.292]    [Pg.1]    [Pg.200]    [Pg.438]    [Pg.37]    [Pg.94]    [Pg.99]    [Pg.106]    [Pg.428]    [Pg.207]    [Pg.245]    [Pg.827]   


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