2. Temp. Min/Nor/Max (C) 3. Sp.Gr. Min/Nor/Max (-) 4. Vap.Press.Max.(Kg/cm2A) 5. Vis. Min/Nor/Max (cP) 6. Capacity Nor. (m3/hr) 7. Capacity Overdesign (%) 8. Capacity Design (m3/hr) 3) SUCTION CONDITIONS 1. Line Size / Class (inch/-) 2. Pipe Inside Dia. (mm) 3. Actual Length (m) 4. Equivalent Length (m) 5. Velocity (m/s) 6. Reynolds Number (-) 7. Fri. Loss (Kg/cm2/100m) 8. Min.Drum Pres.(Kg/cm2G) 9. Min. Liq. Static Head (m)10. Line Loss (Kg/cm2)11. Strainer Loss (Kg/cm2)12. Other Loss (Kg/cm2)13. Suct. Press. (Kg/cm2G) 5) DIFFERENTIAL PRESSURE 1. Disch. Press. (Kg/cm2G) 2. Suct. Press. (Kg/cm2G) 3. Special Margin (Kg/cm2) 4. Diff. Press. (Kg/cm2) 5. Head * (m)
* To be checked by controlling case (Min. Sp. Gr.) 6) NET POSITIVE SUCTION HEAD 1. Suct. Press. (Kg/cm2G) 2. Vap. Press. (Kg/cm2G) 3. Net (Kg/cm2) 4. NPSH Available * (m) 5. NPSH Required * (m)
* To be checked by controlling case (Max. Vap. Press.)
2.88792.3220.5659
4.49.84612.8879
0.57.458259.192///////
3/76.220501.38885555800.2956
1.99.410.14780.0502.8879////
PU-XXXXX//
70/1.26/3.10.24/22.8022.8
4) DISCHARGE CONDITIONS 1. Case (Destination) 2. Capacity Nor. (m3/hr) 3. Line Size (inch) 4. Pipe Inside Dia. (mm) 5. Actual Length (m) 6. Equivalent Length (m) 7. Velocity (m/s) 8. Reynolds Number (-) 9. Fri. Loss (Kg/cm2/100m)10. Pressure Loss (Kg/cm2) a. Line b. Orifice c. Exchangers d. Heaters e. Miscellaneous f. Sub-total (a..e)
11. Control Valve (Kg/cm2)12. Max.Dest.Pres.(Kg/cm2G)13. Elevation (m)14. Disch. Press. (Kg/cm2G)
0/5/0/0//5/0/1.9/5/7.53/
0.168/0.2/0/0//0.368/0.5/4.02/39.35/9.8461/
0.20.54.02409.7600.200
/4.6/1/25.4/30/60/2.5217/336272/
0/
/15.23/
3/76.2/50/125/0.9277/371118/0.1344/
31.55230600.3924107124
0
7) BRAKE HORSEPOWER BHP={ /{ =
22.8
m3/hr(Des.) x
1.26
(Sp.Gr.)* x
59.192}
m
}
367.1 x
0.7
(Pump Effi.-Frac.)
6.6174 KW
* To be checked by controlling case (Max. Sp. Gr.)
8) MAX. SHUT OFF PRESSURE 1. Max. Suct. Drum Press. (Kg/cm2G) 2. Max. Liq. Static Head (m) 3. Design Suct. Press. (Kg/cm2G) 4. Shut off Press. =
Des. Suct. Press.
(Note)
6.910.338.2016
7.4582
8.2016
+ 1.2 x Diff. Press.
=
Note; As guide only
17.151 Kg/cm2G
FORM A-MD02.032-123(B)
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