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Floor space comparison

Films. Both structural and nonstructural adhesives are commonly available in film form. Adhesives applied in the form of dry films offer a clean, hazard-free operation with minimum waste and excellent control of film thickness. However, the method is generally limited to parts with flat surfaces or simple curves. Optimum bond strength requires curing under heat and pressure, which may involve considerable equipment and floor space, particularly for large parts. Film material cost is high in comparison to liquids, but waste or material loss is the lowest of any application method. [Pg.409]

The Gibbs-Vorce electrolyzer is one of these it is extremely simple and compact, so that for a current of 1000 A only some 1.4 sq. m of floor space is needed (in comparison with the horizontal Billiter electrolyzer which requires some 6.5 sq. m of floor space for every 1000 A). [Pg.268]

Membrane systems give a compact and modular constmction, which occupies less floor space in comparison to the conventional treatment systems. This becomes extremely attractive in the land-scarce countries such as Japan and Singapore. [Pg.204]

In addition to the requirements of processing so much feed and solvent with a required number of theoretical stages, there are the practical considerations concerning contamination, entrainment, emulsification, floor space, height requirements, cleanability, and versatility to handle other than design rates. The suitability of various type extractors with respect to each of these considerations is listed in Table 3. Not all of the features compared in the table can be equated. The tabulation is provided to show comparisons to aid in the selection of suitable equipment. [Pg.378]

Comparison of disc and drum filters indicates that the former may be expected to give two to three times the flow rate of the latter for equal floor space and the same radii. For the disc filter, there is an optimum value of the inner radius (R of Figure 22.44) that yields a maximum flow rate. The optimum ratio of inner to outer radii varies from about 0.6 to 0.75 and is independent of the properties of the slurry (Tiller 1974). [Pg.1639]

The results presented here are for a simplified model where capital cost is based on list costs of all equipment under study, published energy consumption, and replacement parts costs. The model doesn t attempt to quantify soft costs involved in equipment setup times, floor space consumption, downtime, etc. which appear to favor a robotic approach. The capital cost comparison is sensitive to the cost of the robot. [Pg.2211]

All the apparatus, chemicals, etc. should be available in the laboratory and be efficiently accommodated and stored. Suitable office furniture also forms part of the equipmentto be provided. Fig. 1 is presented as a suggestion of what a modern laboratory building should comprise and how its internal layout may be. The individual work rooms should be of ample size and preferably all be on the same floor - the ground floor, if possible. If this is impracticable for architectural reasons, the rooms in question should at least be conveniently accessible from all parts of the cement works. Cellars or basements should not be used as laboratory space, but may be used for the storage of certain bulky materials or equipment (e.g., standard sand for mortar tests, empty receptacles and moulds, comparison specimens which have to be kept for some time, etc.) and may also accommodate the heating installation. [Pg.386]


See other pages where Floor space comparison is mentioned: [Pg.38]    [Pg.38]    [Pg.355]    [Pg.1157]    [Pg.355]    [Pg.198]    [Pg.749]    [Pg.785]    [Pg.367]    [Pg.223]    [Pg.70]    [Pg.268]    [Pg.137]   
See also in sourсe #XX -- [ Pg.38 ]




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