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Leak specifications

Techniques for detecting leaks out of the colunm are similar to tiiose for leaks into the column, except that the heat transfer medium, rather that the products, should be analyzed. Often, testing a heat exchanger drain or vent can reveal the presence of a leak. Specific sjmip-... [Pg.367]

Fire-Resistant Hydraulic Fluids. Fire-resistant hydrauhc fluids are used where the fluid could spray or drip from a break or leak onto a source of ignition, eg, a pot of molten metal or a gas flame (17). Conditions such as these exist in die-casting machines or in presses located near furnaces. Specific tests for fire resistance are conducted by Factory Mutual in the United States. [Pg.271]

Specification of the feed stream L (C + 2 variables), the ratio L i i/D, the heat leak q, and the pressure of either stream leaving the divider utilizes these design variables and defines one unique operation of the divider. [Pg.1261]

However, given that reconciliation will not always adjust measurements, even when they contain large random and gross error, the adjustments will not necessarily indicate that gross error is present. Further, the constraints may also be incorrect due to simphfications, leaks, and so on. Therefore, for specific model development, scrutiny of the individual measurement adjustments coupled with reconciliation and model building should be used to isolate gross errors. [Pg.2572]

Each test has specific limitations and may pass defects of various sizes and orientations. The specific limitations for a particular technique must be understood for correct interpretation of results. For example, hydrostatic tests and air-underwater tests may pass defects that run 70% of the wall thickness. Hydrostatic tests may pressurize a defect in such a way that leaking does not occur in the test but can in service. [Pg.318]

A VCM (vinyl chloride monomer) production unit uses three vertically mounted agitated reactors for the polymerization of vinyl chloride. Crude material balances infer about 8 to 10% monomer losses. Describe how you would go about assessing whether these losses are due to leaks such as fugitive air emissions. Be specific in recommending procedures and instruments. [Pg.147]

Process Detailed Design Detailed specification based on concept design Minimize number of possible leak paths Make plant friendly to control, operate, and maintain Avoid or simplify hazardous activities such as sampling, loading and unloading Process conceptual design and codes/standards and procedures Experience on past projects/designs... [Pg.16]

The hazards associated with normal plant operations, such as normal stack emissions and fugitive emissions, as well as those resulting from specific incidents such as spills, leaks, fires and explosions should be considered. [Pg.18]

Primary containment The enclosing structure around a red zone used in the atomic energy industry, which has a specific leak tiglitness. [Pg.1469]

Tile standard requires tlie preparer to describe tlie precautions for safe handling and use. Tliese include recommended industrial hygiene practices, precautions to be taken during repair and maintenance of equipment, and procedures for cleaning up spills and leaks. Some manufacturers also use Uiis section to include useful itiformation not specifically required by the standard, such as EPA waste disposal tnethods and state atid local requiretnents. [Pg.305]

Davenport has listed more tlian 60 major leaks of flammable materials, most, of which resulted in serious fires or unconfined vapor cloud explosions (UVCEs)." Table 16.3.1 classifies tlie leaks by point of origin and shows that if transport containers are excluded, pipe failures accounted for more than lialf tlie accidents. The biggest cause of tliese failures lias been shown to be poor construction due to use of wrong specifications or failure to follow specifications established. [Pg.469]

S" = Slip, quantity of fluid that leaks through internal clearances of rotary pump per unit time, GPM SpGr = Specific graHty of liquid at pumping temperature referred to water =1.0 s = Stroke, in. [Pg.221]

Estimate acceptable air leakages resulting from leakage around static and rotary seals, valves, access ports, and other items of mechanical nature required for process operation from the following equations and the specific leak rates 0 indicated in Table 6-8, which is based on w < 10 lb/hr. [Pg.368]


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See also in sourсe #XX -- [ Pg.184 ]




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