Design of the main oil pipeline

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1 Purpose расчета….…….………………………………………………………………....3
2 Initial data ...................... ...................................................... .... 3
3 Determine the number of pumping stations ... ... .............................. 4
3.1 Design values \u200b\u200bof density, viscosity of the pumped oil ... .. ............ 4
3.2 Selection of pumping equipment ......................................................... .. 4
3.3 Determination of the diameter and thickness of the pipe wall ... .. .................. ...... 5
3.4 Hydraulic calculation pipeline. Determining the number of pumping станций………………………………………………………………………………… 7
3.5 Determination of the number of pumping stations .................................... ..8
Arrange 4 pumping stations along the route of the pipeline .................. 11
References ...................................................... .. 13
Appendix A ................................................................................. .15
Appendix B ................................................................................. ... 16
Appendix ................................................................................. ... 17

Additional information

Initial data for calculation:
- The annual capacity of the pipeline GG = 50 million. Tons / year;
- The length of the pipeline (no saddle points) L = 870 km;
- The difference between the geodetic marks z = Zc - Zl = 213 - 278 = 92 m;
- Average pump design temperature TR = 1,4S (Tr = 274.4 K);
- The density of the oil at a temperature of 293 K (20S), 293 = 866 kg / m3;
- The viscosity of the oil at 273K (0S), 273 = 80 mm2 / s .;
- Oil viscosity at 293 K (20S), 293 = 20 mm2 / s.

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