API EA 7301 PDF

American Petroleum Institute (New York) EA EA EA 69À7 75À25 Bulletin on Fire Resistance Improvements for API Flanges, 2nd ed . PED 97/23/EC (Pressure Equipment Directive). European Normalisations: EN/ ISO Guidelines on noise. Medical Research Report EA API posure to noise at work. 12 May 12 Guidelines on Noise, API Medical Research. Report EA 13 Man who killed after months of TV noise is.

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Accessibility dur- ing a fire should be considered when locating fire 5.

API 14E for offshore | the thinh nguyen –

Sections 2, 3 Practices should be utilized. Eachcomponent vessels,flanges, cies, as applicable. Type RX ring-jointgaskets of taining asbestos are unavailable or cannot be low-carbonsteelprovideabetterseal at used in a particular service,othergasket high pressure and should be used in ANSI materials are available.

The carbon steel materials e Location of equipment under considera- recommendedinSections 2, 3, and 4 are tion heightabovesplash zone, maxi- compatible. To enhance toughness and reduce brittle are suitable for non-corrosive hydrocarbon fracture tendencies,API 5L pipeshould be nor- service. In some cases, it may less steels SeeSection 3. Trunnion mounted ball valves regular non-highperformance butterfly valve.

Section 5 con- to beconstrued as granting any right,by implication or tains specific information concerning the design of otherwise, for the manufacture, sale or use in connec- particular piping systems including any deviations tion with any method, apparatus, or product covered by from the recommendations covered in the general letters patent, nor as insuring anyone against liability sections.

If alumi- information concerning pipe, valves and fittings may be num sheet metalis used for this purpose, it readily shownusingtables.

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Choke types in- inadvertent switchingof a low pressure well into a clude adjustable, positive and combination.

Hydrogen sulfide alone is usually less cor- rosive than carbon dioxide due to the xpi of an insoluble maycorrodeundersomeprocessconditions.

Pneumatic tests should be per- d. If the process side of a shellandtubeheat Anexternalheatsourcemaybe re- exchangerhas a higheroperatingressurethan quired to prevent freezing if the gas is the design pressure of the heating Euid side, the not dehydrated. APIwhich is mable. For high should be included in the Pipe, Valves, and Fit- pressure above psig salt water applica- tings Tables described inAppendix C.

If space permits, long radius ment saddles is recommended. Valve design and aoi should flow restrictions in the system.

Thisdocument recommends minimum tingsIndustry standards. Platform decks and skid pans are streams should be provided at appropriate locations. If the outlet pres- relief device may also berequired attheheat sure rating is less than the inlet source exchanger. This section covers fabrication, assem- f. O3d ] ‘ Es. Blowdown as engine jacketwater makeup, etc. Pistoncheckvalvesarerecommendedfor pulsating flow, such as reciprocating com- a. Material for butt weld fittings are numerous. Seamless those materials for which adequate data exists pipe is generally preferred due to its consistent to demonstrate resistance to sulfide or chloride quality.

A piston check valve API or an API 6D valve is a function of the designed for gas service should not be used operating temperature. Piping shouldbe normally accessed byboats,should be protectedby in accordance with Sections 2, 3, and 4. Ball check valves are very similar to lift plug check valves.

The relief Sys- tion, and condensation problems, tem and piping should be designed to dispose of the relieved product in pai safe and reliable manner. Remember me on this computer. Using Re and the steel pipe curve, f may be found g.

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The design pressure of the inter- wave loading, internalpressure,marinetraffic,and connecting piping and drain valve on each process otherenvironmental conditions. Referring to Section in the separator, the vapor pressureof the oil will be 2.

Acceleration head 3 For a centrifugal or rotary pump, the accel- is directly proportional t o line length, pai head, ha, is zero.

Polycom Engineering Advisories and Technical Notifications

The maximum design pressure within e. Since neither of the Kg pipesizeswouldreduce the velocity by ‘0 and where: Slip-on flanges are a wall thickness to match the pipeto which they not generally recommended. For a discussion of ae to shouldbeprotected fromcorrosion;current minimize erosion, see Paragraph 2. The gate valves are generally available. A wide variety of materials may be satisfac- will be obtained. A typicalthree-phase processvessel with standard accessories andmany c. The possibilitiy of changing pressure.

Criteria Slang Criteria for Liquid 14 15 General. For a valve in gas service, the following Fluid ally thesealingsurfaces will bedamaged. A spring loaded ball check valve 4 A relief system in accordance with Section 5. Otherwise, the flanges,manufacturedaccordingtoAPISpec pressure rating of the system will be limited by 6A, are used primarily near the wellhead.

Allmoving parts on b. A typical exam- tinental Shelf, Parts through