{"text_format":"1","workbook":"xlsx","n_sheets":4,"sheets":["Data","N_dist","cdf_plot","pdf_plot"],"not_rendered":{"charts":4,"images":0,"macros":1,"external_links":0,"defined_names":25,"comments":0,"pivot_tables":0},"unopened":[{"sheet":"cdf_plot","index":2,"reason":"not_a_worksheet"},{"sheet":"pdf_plot","index":3,"reason":"not_a_worksheet"}],"bounds":{"document_bytes":16777216,"sheet_cells":100000,"rows_first":2000,"rows_last":500,"rows_between":2000,"halvings":0,"cell_chars":16384,"cell_head_chars":4096},"cells_cut":0,"cells_raw":0,"read":"whole","date_system":"1900"}

{"sheet":"Data","index":0,"n_rows":33,"n_cols":17,"rows_kept":33,"cut":false,"hidden":false,"merged":[]}
["Problem 1 Undersaturated oil field, TPG4230 V2020, Resit exam, Prof. Milan Stanko "]
["Annual uptime",360,"day"]
["Initial Reservoir Pressure, PRi",265,"bara"]
["Reservoir Pressure decline rate, CD",70,"bara"]
["Initial oil in place ",4000000,"[Sm3]"]
["Productivity index well (oil)",60,"Sm3/d/bara"]
["Oil density, Rho",861,"kg/m3"]
["Oil viscosity(average), Vis",1.0300000000000001E-3,"Pa s"]
["Tubing data",null,null,null,null,null,null,null,null,null,null,null,null,null,"NPV CALCULATIONS"]
["Measured depth, MD",2200,"m",null,null,null,null,null,null,null,null,null,null,null,"Discount rate","[1/year]",0.08]
["Deviation angle  (from horizontal)",90,"deg",null,null,null,null,null,null,null,null,null,null,null,"Oil price","[USD/Sm3]",180]
["Tubing inner Diameter, ID",0.154,"m",null,null,null,null,null,null,null,null,null,null,null,"COST","[1E06 USD]",200]
["Tubing Roughness",1.5E-5,"m",null,null,null,null,null,null,null,null,null,null,null,"NPV","[1E06 USD]"]
["Pipeline data",null,null,null,null,null,null,null,null,null,null,null,null,null,"NPVrev","[1E06 USD]"]
["Horizontal pipe length",14000,"m","time","qwell","DNp","Np","RF","PR","pwf","Pwh","Priserbase","psep","error","Discounted yearly revenue"]
["Pipeline inner diameter, ID",{"$f":"10*0.0254","v":0.254},"m","[year]","[Sm3/d]","[Sm3]","[Sm3]","[-]","[bara]","[bara]","[bara]","[bara]","[bara]","[bar]","[1E06 USD]"]
["Deviation angle  (from horizontal)",0,"deg",0,null,null,0,null,{"$f":"B3","v":265},null,null,null,null,null,0]
["Pipeline roughness",1.5E-5,"m",1]
["Riser data",null,null,2]
["vertical pipe length",180,"m",3]
["Flowline data diameter, ID",{"$f":"10*0.0254","v":0.254},"m",4]
["Deviation angle  (from horizontal)",90,"deg",5]
["Riser roughness",1.5E-5,"m",6]
["Separator Pressure",20,"bara",7]
[null,null,null,8]
[null,null,null,9]
[null,null,null,10]
[null,null,null,11]
[null,null,null,12]
[null,null,null,13]
[null,null,null,14]
[null,null,null,15]
[null,null,null,16]

{"sheet":"N_dist","index":1,"n_rows":22,"n_cols":3,"rows_kept":22,"cut":false,"hidden":false,"merged":[]}
["N [1E06 Sm3]","pdf","cdf"]
[2.4003673328371788,3.8026304940885007E-5,0]
[2.634633863614761,2.6328524453332033E-4,1.6075807993758643E-3]
[2.8689003943923432,1.0055107785341771E-3,8.3486249497444955E-3]
[3.1031669251699254,2.5379793719581606E-3,2.8274090483763108E-2]
[3.3374334559475076,4.7487396288773591E-3,7.0441681939728815E-2]
[3.5716999867250898,7.1106486512130598E-3,0.13999651162780433]
[3.805966517502672,8.9855472903212965E-3,0.23489627260782642]
[4.0402330482802542,9.9539259979661478E-3,0.34667111235386305]
[4.274499579057836,9.9400602956195312E-3,0.46394710705495873]
[4.5087661098354177,9.1377046245340859E-3,0.57617456154195468]
[4.7430326406129995,7.8579018174245677E-3,0.67590603437443075]
[4.9772991713905812,6.4004911670463831E-3,0.75936453819280236]
[5.211565702168163,4.9868386364425501E-3,0.82585794821803404]
[5.4458322329457447,3.7458219317840331E-3,0.87673780034014881]
[5.6800987637233264,2.7297535525209701E-3,0.91439246026027343]
[5.9143652945009082,1.9399386140924195E-3,0.9414987229486077]
[6.1486318252784899,1.3501250106022404E-3,0.96056747088154382]
[6.3828983560560717,9.2341567738177591E-4,0.97372714989447484]
[6.6171648868336534,6.224716765786826E-4,0.9826648328975226]
[6.8514314176112352,4.1456991488055049E-4,0.98865472775018903]
[7.0856979483888169,2.7335159897319523E-4,1]