Surface production operations. Volume 2, Design of by Maurice Stewart

By Maurice Stewart

Updated and higher than ever, Design of Gas-Handling structures and amenities, third variation includes tremendously multiplied chapters on gas-liquid separation, gasoline sweetening, fuel liquefaction, and gasoline dehydration —information worthy and significant to creation and method engineers and architects. ordinary fuel is on the vanguard of todays strength wishes, and this e-book walks you thru the apparatus and tactics utilized in gas-handling operations, together with conditioning and processing, that can assist you successfully layout and deal with your gasoline construction facility. Taking a logical strategy from thought into functional software, Design of Gas-Handling structures and amenities, third version contains many helping equations in addition to precise tables and charts to facilite procedure layout. in keeping with real-world case reports and event, this must-have education consultant is a reference that no traditional fuel practitioner and engineer could be without.

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

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Additional resources for Surface production operations. Volume 2, Design of gas-handling systems and facilities

Example text

In general, most upstream facilities use conduction, convection, or a combination of the two. Radiant energy from a direct flame, in fluid-fluid exchangers, the temperatures are not hot enough for radiation to be a significant mechanism. 53 Heat Transfer Theory It is important in calculating the heat given off by a flare. 173 Â 103 Btu/h ft. The value of “h” is a proportionality constant used to characterize liquid film resistance. The value “k” is the thermal conductivity of the solid separating the two fluids.

13 Determine Cooling and condensation weighted temperature difference. 13 LMTD for cooling and condensation.

This diagram can be used to investigate thermodynamic fluid properties as well as their thermodynamic phenomena, such as retrograde condensation and the Joule-Thomson effect. Please note, however, that a P-H diagram is likely to be available only for a single component of the mixture unless the diagram is created by simulation software packages such as those mentioned above. 18. 17 A P-H diagram for propane. Courtesy of GPSA Engineering Data Book. 6 specific gravity natural gas. 1 OBJECTIVES The objective of this chapter is to help the reader understand the role of heat exchangers (HEX) in upstream operations.

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