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Equipment design and scale

Processing solids, since equipment design and scale-up are greatly limited by our lack of fundamental understanding of solids behavior. [Pg.17]

Category A where standardised tests already exist and the interpretation of data is well established and accepted the only work needed is in publicising their existence and use. Category B where test methods exist but there is disagreement as to the significance of the measured values in equipment design and scale-up validation testwork is clearly needed here. Category C where no standardised test procedures are yet available for a particular powder property and these need to be developed experimentally. [Pg.1]

Flowability is a difficult thing to measure as it depends very much on the design and characteristics of the delivery device as well as on the powder itself. The procedures for the free flow time are far from standard at the moment and improvement might be needed here. It seems, however, that it is far better to measure flowability by the failure properties which are functions of the powder only and for which theories exist to be used in equipment design and scale-up. [Pg.78]

Laboratory experiments using rodents, or the use of gas analysis, tend to be confused by the dominant variable of fuel—air ratio as well as important effects of burning configuration, heat input, equipment design, and toxicity criteria used, ie, death vs incapacitation, time to death, lethal concentration, etc (154,155). Some comparisons of polyurethane foam combustion toxicity with and without phosphoms flame retardants show no consistent positive or negative effect. Moreover, data from small-scale tests have doubtful relevance to real fine ha2ards. [Pg.481]

References 29 through 38 provide additional information on filters and the design and scale-up principles. Note that vendors are some of the best sources of information on equipment. Look at some of the Web sites noted in this and other sections describing equipment. [Pg.417]

The typical factors to consider when pondering B2C will include size and scale of operation, use of existing equipment, flexibility for multiproduct operation, start-up and shutdown, cleaning frequency, inventory, validation, traceability of product with respect to raw materials, equipment design, and availability as well as operational experience [50]. [Pg.321]

Regarding the above formulation and process, the thermal stability was determined by estimating the isothermal lifetime from thermo-gravimetric data. Process scientists for scale-up equipment design and temperature specifications sought answers to the following four basic questions ... [Pg.107]

The value of /jim is determined by the discontinuity in the dependence of cell current on applied cell voltage which occurs when the interfacial concentration approaches zero. The polarisation parameter is convenient in the design and scale-up of electrodialysis equipment. It can be easily measured in small-scale stacks at a given value of bulk concentration and then used to predict limiting current densities in larger stacks at other concentrations. Most stacks use operating values of the polarisation parameter that are 50-70 per cent of the limiting values. [Pg.467]

In stagewise equipment, the design and scale-up is simple and is often determined from bench data. The stage efficiency is usually high, and the capacity is determined by the settler design necessary to achieve coalescence of the dispersed phases. For differential contactors, such as columns, the flow capacity is determined by the droplet size and the type of internals (see... [Pg.299]

One must also stress the importance of quality considerations during compounding and full adherence to current good manufacturing practices while producing parenteral products. Personnel responsible for the process design and scale-up of the equipment must assure proper documentation... [Pg.86]

To obtain results of interest for the design and scaling-up of industrial devices, experiments were carried out at small pilot plant scale. The conditions for the equipment and system design are listed in Table 7.3. [Pg.169]

The following considerations are most important in equipment selection, testing, and design and scale-up of L-L systems ... [Pg.299]


See other pages where Equipment design and scale is mentioned: [Pg.388]    [Pg.388]    [Pg.113]    [Pg.91]    [Pg.92]    [Pg.4]    [Pg.566]    [Pg.388]    [Pg.388]    [Pg.113]    [Pg.91]    [Pg.92]    [Pg.4]    [Pg.566]    [Pg.419]    [Pg.39]    [Pg.542]    [Pg.862]    [Pg.327]    [Pg.66]    [Pg.133]    [Pg.156]    [Pg.457]    [Pg.55]    [Pg.68]    [Pg.109]    [Pg.112]    [Pg.457]    [Pg.39]    [Pg.169]    [Pg.265]    [Pg.862]    [Pg.135]    [Pg.4]    [Pg.555]    [Pg.1327]    [Pg.16]    [Pg.68]    [Pg.232]    [Pg.294]    [Pg.327]    [Pg.2877]    [Pg.41]    [Pg.2094]    [Pg.1457]   
See also in sourсe #XX -- [ Pg.91 , Pg.92 ]




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