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Leveling equipment

For draining principal items of process equipment, level-controUed condensate chambers provide much better performance and rehabiUty than steam traps. Usage is generally justified when condensate flow is greater than 4500 kg /h. [Pg.227]

Research and education focus on the mesoscale (equipment level) ... [Pg.26]

The process reliability simulation VIP should be initiated in the feasibility phase (FEL-2) to produce a block-level RAM model. Based on the results of that model, a more detailed equipment-level RAM model should be developed starting in the definition phase (FEL-3). [Pg.52]

In the simplest case, integration of reaction and separation may take place on the purely equipment level, without introducing any new functional interrelations between the operations involved—the reaction does not influence the separation, nor has the separation process any effect upon the reaction. The aimed result of such combination can be ... [Pg.272]

An example of a mapping from the equipment representation to the thermodynamic state representation is shown in Fig. 5. It represents an isothermal vertical packed-bed catalytic reactor equipped with temperature and pressure sensors, an explosion vent, and a distributor plate. Notice that the equipment and sensors are not associated with the state representation. They are contained in the base representation and reside in the process description at the equipment level. As discussed earlier, flow, work, heat, and mass interactions are all modeled independently. This allows us to evaluate independently the effect of these processes. Independent evaluation assists in the identification, evaluation, and assessment of event pathways leading to hazardous states. [Pg.204]

Based on knowledge of the extraction techniques discussed in this chapter, make a comparison of each technique. As a suggestion, the following headings could be used for comparison purposes brief description of technique sample mass extraction time per sample solvent type solvent consumption sequential or simultaneous extraction relative cost of equipment level of automation approval of methods (USEPA). [Pg.137]

The demonstration plot of the experimental site should be constructed to evaluate the effectiveness of phytoremediation. The field activities consist of site mobilization, plot layout an construction, and soil sampling combined with other agricultural practices designed secifically for phytoremediation and adapted for the conditions present at the site. The activities has to be conducted in accodance with the personal protective equipment, level of protection, action levels and other health and safety practices, i.e. hazard analysis general safety reccomendations evaluation of the mechanical, electrical, fire hazards, gas and power lines, heat stress, noise, chemical hazards. [Pg.300]

The next level of detail for operating instructions, which is probably the most widely used, is to have instructions that are at the equipment level. The procedure provided in Figure 6.29 shows this level of detail. [Pg.330]

However, if the hexamine feed is stopped via TSH2 (Process control engineering (PCE) monitoring equipment level 2 in Table 4.1), which is activated after 786 s in the first case and after 4,024 s in the second, the variation of temperature with time is milder, since the continuing feed of (cold) nitric acid leads to a reduction of hexamine concentration and hence of the reaction rate. [Pg.128]

Indicators Number of breakdowns in critical communication equipment. Level of team training focusing on communication - such as Crew Resource Management (CRM). Periodic assessment of Team mutual awareness, quahty of communication in critical operations related to clarity, process awareness and risk awareness. [Pg.51]

Involuntary release of part of the explosive gas mixture at electrical equipment level. This situation can be caused by a filling fault (overflow) or by the movement of air ... [Pg.1964]

It is thus probable that the hydrogen concentration is no longer explosive at electrical equipment level. Hydrogen leakage in the network due to equipment failure can however stiU be envisaged. [Pg.1964]


See other pages where Leveling equipment is mentioned: [Pg.184]    [Pg.185]    [Pg.376]    [Pg.377]    [Pg.379]    [Pg.9]    [Pg.101]    [Pg.235]    [Pg.336]    [Pg.337]    [Pg.49]    [Pg.50]    [Pg.180]    [Pg.229]    [Pg.325]    [Pg.1023]    [Pg.1024]    [Pg.2542]    [Pg.99]    [Pg.1027]    [Pg.1028]    [Pg.153]    [Pg.376]    [Pg.377]    [Pg.379]    [Pg.534]    [Pg.534]    [Pg.680]    [Pg.1061]    [Pg.75]    [Pg.936]    [Pg.272]    [Pg.494]   
See also in sourсe #XX -- [ Pg.376 ]

See also in sourсe #XX -- [ Pg.376 ]




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