Highlights
Design of a fluid flow system for therm fluid-based process industry Petroleum is one of the major sources of energy supply particularly in the transport sector throughout the world. This energy is produced by refining the petroleum crude oil through the heat and mass transfer process in a closed thermodynamic system. It is one of the interesting thermo fluids applications in industrial scale. There are two main fossil fuel feed sources that are used in the refinery - one is crude oil which is a mixture of a number of hydrocarbons and the other source is natural gas condensate which is the liquid hydrocarbon (ranging from C1 to C18) formed as a byproduct during the processing of the natural gas. This condensate is lighter than the crude oil which can be refined in a distillation column to obtain petrol or gasoline, kerosene and diesel products. This project is focusing on natural gas condensate for the refining process which consists of some integrated steps as shown by the process flow diagram
from the feed to distillation in Figure.There are four main part of this Project as shown below-
PART 1: Pumps (feed pump P-101, products pumps P-102, P-103, P-104) and pipeline design for both feed and finish products. In this part, the following criteria should be considered and addressed–
1. Complete schematic drawing showing relevant components (use CAD/drafting software)
2. Fittings ∑KL values Tables for both plant feed and products pipeline
3. Pipe material, diameter (I/O), busting pressure, friction factor (f) for entire system considering HEN system loss
4. System equation (static head, dynamic head, and head loss) for P-101
5. Duty point (DP) for feed pump P-101
6. Pump characteristics at DP (head, power, efficiency, specific speed, etc.)
7. Draw velocity triangles for inlet and outlet of the pump impeller
8. Calculate theoretical head (H), power and compare with DP values
9. Cavitation check (NPSHA) for feed pump P-101
10. Apply similarity laws for product pumps design P-102, P-103, P-104
11. Analyse CH, CP vs CQ at a fixed speed for P-102, P-103, P-104 separately
12. Cavitation check (NPSHA) for all product pumps
13. Calculate total power cost per day for running all pumps
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