By Maurice Stewart
Updated and higher than ever, Design of Gas-Handling structures and amenities, third variation includes significantly multiplied chapters on gas-liquid separation, gasoline sweetening, fuel liquefaction, and fuel dehydration —information useful and significant to construction and technique engineers and architects. common gasoline is on the leading edge of todays power wishes, and this booklet walks you thru the gear and approaches utilized in gas-handling operations, together with conditioning and processing, that will help you successfully layout and deal with your gasoline construction facility. Taking a logical technique from thought into functional software, Design of Gas-Handling platforms and amenities, third version contains many assisting equations in addition to special tables and charts to facilite procedure layout. in response to real-world case reports and adventure, this must-have education advisor is a reference that no traditional 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 fuel dehydration
Read Online or Download Surface production operations. Volume 2, Design of gas-handling systems and facilities PDF
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Additional info for Surface production operations. Volume 2, Design of gas-handling systems and facilities
Example text
10. 12 Nonlinear temperature profiles. 60 Surface Production Operations exchanger area cannot be calculated using Aq/(u) DtM when temperature profiles are nonlinear. Summaries of several procedures follow: 1. Calculate the area for each segment of the exchanger. The heat transfer coefficient (U) varies through the exchanger. The correct U for each segment depends on the fluid phase in that segment. The exchanger area is the sum of the segments’ areas. 2. 13 Determine Cooling and condensation weighted temperature difference.
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. Key pressure drop considerations include: • Evaluating design • Determining flow path length 49 Heat Transfer Theory • • Calculating pressure gradient (DP/L) Determining what is a reasonable pressure drop, depending on service • Minimize cost system. Restricted? Why? Impact limiting side • Impact of fouling • Evaluating performance • Compare to design • Another indicator of fouling • What is time trend?
Solid phase high-molecular-weight hydrocarbons, otherwise known as paraffins, can dramatically affect the viscosity of the crude sample. The cloud point is the temperature at which paraffins first become visible in a crude sample. 11. This change in the temperature-viscosity relationship can lead to significant errors in estimation. Therefore, care should be taken when estimating viscosities near the cloud point. The pour point is the temperature at which the crude oil becomes a solid and ceases to flow, as measured by a specific American Society of Testing Materials (ASTM) procedure (D97).