By Maurice Stewart
Updated and higher than ever, Design of Gas-Handling platforms and amenities, third variation includes significantly increased chapters on gas-liquid separation, fuel sweetening, fuel liquefaction, and gasoline dehydration —information beneficial and significant to construction and strategy engineers and architects. common gasoline is on the leading edge of todays power wishes, and this e-book walks you thru the gear and strategies utilized in gas-handling operations, together with conditioning and processing, that will help you successfully layout and deal with your fuel construction facility. Taking a logical strategy from thought into functional software, Design of Gas-Handling structures and amenities, third variation contains many aiding equations in addition to specific tables and charts to facilite method layout. in keeping with real-world case stories and adventure, this must-have education consultant is a reference that no ordinary fuel practitioner and engineer will 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
Read Online or Download Surface production operations. Volume 2, Design of gas-handling systems and facilities PDF
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Additional resources for Surface production operations. Volume 2, Design of gas-handling systems and facilities
Sample text
The designer must also consider system economics. One must allocate the streams to minimize equipment cost and operating cost. Mechanical and materials constraints include: • Minimizing • Initial equipment cost [capital expense (OPEX)] and • Operating cost [operating expense (OPEX)] • Thermal expansion • Flange and tube leaks • Safety • Materials versus process conditions Fouling information is highly proprietary. The designer must understand and control fouling to avoid its high costs. 1 Key Parameter for Design and Troubleshooting The allowable pressure drop should be set by process constraints.
20) Qg ¼ 1,000,000 where Qg ¼ gas flow rate, MMscfd. 23) where Q1 ¼ liquid flow rate, bpd; SG ¼ specific gravity of liquid (water ¼ 1). Often, the designer is given the mole fraction of each component in the feed stream but is not given the mole flow rate for the stream. It may be necessary to estimate the total number of moles in the feed stream (F) from an expected stock-tank oil flow rate. As a first approximation, it can be assumed that all the oil in the stock tank can be characterized by the C7 + component of the stream.
5 BASIC HEAT TRANSFER THEORY Sensible heat is energy transferred solely as a result of a temperature change. 1 Heat Transfer Mechanisms Conduction Conduction is the transfer of heat from one molecule to an adjacent molecule while the particles remain in fixed positions relative to each other. It is the primary mechanism in solids and some fluids that are stagnant or have low flow rates. Convection Convection is the transfer of heat by the physical movement of molecules from place to place, for example, the mixing of warmer and cooler portions of a fluid in a heater.