<p> ME-437 PIPELINE ENGINEERING Fall 2011</p><p>NAME OF THE PROJECT (UTILIZED SYSTEM) (PROGRAMMING LANGUAGE)</p><p>Supervised by: Dr. Ekin BİNGÖL</p><p>Assistant Alp Emre Öngüt</p><p>Prepared by (Name of the participant)</p><p>METU DATE ANKARA, TURKEY ME-437 PIPELINE ENGINEERING PROJECT FORMAT</p><p>-Title Page (see exemplary title page) -Introduction -Problem Definition o Map o Physical Properties of Fluid o Flowrate Distribution along Pipe -Design Methodology o Definition of Optimization Problem o Definition of Pipeline Design o Definition of Pump Selection o Definition of Objective Function -Design Iteration using Design Capacity as Main Flow Rate (Show all calculations) o Selection of Pipe Diameter and Thickness o Calculation of Friction Factor o HGL and MAOP for each iteration o Cost Calculations and Table Showing Cost Optimization -Pump Selection -Map of Final Design (Topography, HGL, places and specifications of pump stations) -Manipulation of Pumps for Operating Conditions (i.e. due to flow rate distribution) -Map of Off-Design Operating Condition (Topography, HGL, places and specifications of pump stations) -Conclusion and Recommendations for Future Work -References -Appendices o Supply all information you have utilized during design in forms of figures and tables o Cost Tables and Functions o Pump Specifications (Showing operating points for each pumps) o API table used in the necessary range o ……. Electricity Cost : 0.07 $/kW-h Total Life : 25 years Interest Rate : 0.1 Electricity Demand Charge : 5 $/kW-month</p><p>Pipeline Construction Costs ($)</p><p>Factor for Wrap Type of Diameter Basic Const. Cost Basic Wrap Cost Diameter Cost Condition (inch) ($/m) ($/m) ($/m) 12 40.80 0.50 12.00</p><p>24 81.60 1.00 24.00</p><p>Unmade 24.00 30 102.00 1.25 30.00</p><p>36 122.40 1.50 36.00</p><p>12 48.00 0.50 12.00</p><p>24 96.00 1.00 24.00</p><p>Agricultural 24.00 30 120.00 1.25 30.00</p><p>36 144.00 1.50 36.00</p><p>12 60.00 0.50 18.00</p><p>24 120.00 1.00 36.00</p><p>Rock 36.00 30 150.00 1.25 45.00</p><p>36 180.00 1.50 54.00</p><p>12 108.00 0.50 24.00</p><p>24 216.00 1.00 48.00</p><p>Swamp 48.00 30 270.00 1.25 60.00</p><p>36 324.00 1.50 72.00</p><p>12 216.00 0.50 24.00</p><p>24 432.00 1.00 48.00</p><p>Sea 48.00 30 540.00 1.25 60.00</p><p>36 648.00 1.50 72.00</p><p>Pipeline Material Costs ($) Pipe Wall Pipe Line Bend Location Diameter Pipe Cost Grade Thickness Weight Cost Class (mm) (mm) (Kg/m) ($/m) ($/m) 300 X42 6.40 49.68 34.77 1.74</p><p>400 X52 6.40 62.58 43.81 2.19</p><p>450 X46 7.90 87.71 61.40 3.07 Class 1 500 X52 7.90 97.63 68.34 3.42</p><p>600 X52 9.50 140.81 98.57 4.93</p><p>900 X56 12.7 282.12 197.48 9.87</p><p>300 X46 6.40 49.68 34.77 1.74</p><p>400 X60 6.40 62.58 43.81 2.19</p><p>450 X52 7.90 87.71 61.40 3.07 Class 2 500 X60 7.90 97.63 68.34 3.42</p><p>600 X60 9.50 141.26 98.88 4.94</p><p>900 X65 12.7 282.12 197.48 9.87</p><p>300 X42 9.50 73.76 51.63 2.58</p><p>400 X46 9.50 93.13 65.19 3.26</p><p>450 X52 9.50 105.05 73.54 3.68 Class 3 500 X60 9.50 116.97 81.88 4.09</p><p>600 X52 12.70 186.75 130.73 6.54</p><p>900 X65 15.90 351.41 245.99 12.30</p><p>300 X42 12.70 97.36 68.15 3.41</p><p>400 X46 12.70 123.18 86.22 4.31</p><p>450 X52 12.70 139.07 97.35 4.67 Class 4 500 X56 12.70 154.97 108.48 5.42</p><p>600 X65 12.70 186.75 130.73 6.54</p><p>900 X65 19.10 420.19 294.14 14.71 A PRACTICAL WAY OF CALCULATING THE WEIGHT OF LINE PIPES</p><p>W= (OD-WT) x WT x 0.02466 OD : mm WT : mm W : kg/m</p><p>COST OF LINE PIPE</p><p>MATERIAL SPECIFICATION CBP (USD/ kg) X42 0.56 X46 0.58 X52 0.60 X56 0.62 X60 0.64 X65 0.66</p><p>COST OF PE COATING</p><p>CPE=12 USD/m2</p><p>COST CALCULATION OF LINE PIPE</p><p>CO= (W x CBP) + [(OD/318) x CPE]</p><p>EXAMPLE Calculate the cost of 1 meter, X52 grade, line pipe with an outer diameter of 24 inches and a wall thickness of 11.1 millimeters using practical weight calculation formula. SOLUTION OD = 610 mm WT = 11.1 mm CBP=0.60 USD/kg CPE=12USD/kg W = (610-11.1) x 11.1 x 0.02466=163.93 kg/m CO = (163.93 x 0.60) + [(610/318) x 12] CO ≈ 121.4 USD </p>