Surface Production Operations: Vol 2: Design of Gas-Handling by Maurice Stewart

By Maurice Stewart

Updated and higher than ever, Design of Gas-Handling structures and amenities, third version includes significantly improved chapters on gas-liquid separation, gasoline sweetening, gasoline liquefaction, and fuel dehydration -information priceless and demanding to construction and approach engineers and architects. common fuel is on the vanguard of latest power wishes, and this e-book walks you thru the gear and techniques utilized in gas-handling operations, together with conditioning and processing, that will help you successfully layout and deal with your fuel creation facility. Taking a logical strategy from thought into functional program, Design of Gas-Handling structures and amenities, third variation contains many aiding equations in addition to specific tables and charts to facilite approach layout. in accordance with real-world case experiences and event, this must-have education consultant is a reference that no ordinary fuel practitioner and engineer might be without.

  • Packed with charts, tables, and diagrams
  • Features the prerequisite ASME and API codes
  • Updated chapters on gas-liquid separation, fuel sweetening, fuel liquefaction and gasoline dehydration

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Additional resources for Surface Production Operations: Vol 2: Design of Gas-Handling Systems and Facilities, Third Edition

Example text

55 gases. Courtesy of GPSA Engineering Data Book. 2 Compressibility factor for specific gravity. 6 gases. Courtesy of GPSA Engineering Data Book. 3 Compressibility factor for specific gravity. 65 gases. Courtesy of GPSA Engineering Data Book. 4 Compressibility factor for specific gravity. 7 gases. Courtesy of GPSA Engineering Data Book. 5 Compressibility factor for specific gravity. 8 gases. Courtesy of GPSA Engineering Data Book. 6 Compressibility factor for specific gravity. 9 gases. Courtesy of GPSA Engineering Data Book.

TEMA addresses flowinduced vibration in detail. 3 illustrates where tube vibrations may occur. 0. Prior to the 1999 addendum, all pressure vessels and process piping was required to be hydrostatic tested to 150% of stated design pressure. For example, if a pressure vessel’s design pressure is 100 psig, then the hydrostatic test pressure must be 150 psig; so 100/150 ¼ 2/3. ” API RP 521 states that if the design pressure of the low-pressure side of a heat exchanger is within 2/3 of the design pressure of the high pressure side, then one would not have to include tube rupture as a credible relieving scenario.

Design standards have evolved over the years due to investigation of catastrophic plant incidents and large-scale laboratory tests by Southwest Research Institute 1977-1979. Tube rupture industry standards and recommended practices include the following: • ASME Section VIII Division 1 UG-133 (d) Code case VIII-80-56 (6/25/80) requires relief provisions for steam boilers only. • API Recommended Practice 521 discusses inadequacy of ASME code rule and is not helpful. It recommends considering complete break of one tube or break at one end, which would be the worst-case scenario.

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