Petroleum Refining Design and Applications Handbook. A. Kayode Coker

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Petroleum Refining Design and Applications Handbook - A. Kayode Coker

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target="_blank" rel="nofollow" href="#ulink_5d338473-d061-5b5d-ba20-861b95f7bee2">Figure 14.17d.

      In order to represent the basic type of solution flowing in a line, designations or codes to assign to the lines can be developed for each process. Some typical codes are:

RW - River Water
TW - Treated Water
SW - Sea Water
BW - Brackish Water
CW - Chilled Water
S - Low Pressure Steam
S150 - 150 psi Steam
S400 - 400 psi Steam
V - Vent or Vacuum
C - Condensate (pressure may be indicated)
D - Drain to sewer or pit
EX - Exhaust
M - Methane
A- - Air (or PA for Plant Air)
F - Freon
G - Glycol
SA - Sulfuric Acid
B - Brine
Cl - Chlorine
P - Process mixture (use for in-process lines not definitely designated by other symbols)

      Sometimes it is convenient to prefix these symbols by L to indicate that the designation is for a line and not a vessel or instrument.

      The process designer must also consider the corrosive nature of the fluids involved when selecting construction of materials for the various process and utility service lines. Some designers attach these materials designations to the line designation on the flowsheets, while others identify them on the Line Summary Table (Figure 14.20d). Some typical pipe materials designations are:

CS40 - Carbon steel, Sch. 40
CS80 - Carbon steel, Sch. 80
SS316/10 - Stainless steel 316m Sch. 10
GL/BE - Glass bevel ends
N40 - Nickel, Sch. 40
TL/CS - Teflon-lined carbon steel
PVC/CS Polyvinyl chloride - lined CS
PP - Solid polypropylene (designated weight sch)

      The process designer also needs to designate the hydraulic test pressures for each line. This testing is performed after construction is essentially complete and often is conducted by testing sections of pipe systems, blanking off parts of the pipe or equipment, if necessary. Extreme care must be taken to avoid over pressuring any portion of pipe not suitable for a specific pressure, as well as extending test pressure through equipment not designed for that level. Vacuum systems must always be designed for “full vacuum,” regardless of the actual internal process absolute vacuum expected. This absolute zero designed basis will prevent the collapse of pipe and equipment should internal conditions vary. Some line design systems include the test pressure in the line code, but this often becomes too unwieldy for drafting purposes.

Examples: 2″-CL6-CS40
3″-CL6a-CS40
4″-RW1-CS40
16″-S150-CS40
3″-P-TL/CS

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