![]() Td =td / tt = 2.6(D)(H-1)/(St) = td = Miniumum shell thickness = D = Normal tank diameter, in feet H = depth of tank, in feet G = design Specific gravity of liquid Sd = allowable Str Stre ess fo for De Design co condition E = joint efficiency St = allowable allowable stress 516-60 Hydro Test CA = Corrosion Allowance For Fourth Course 516-60 PlateĠ.2365 0.2365 inches inches 94.5 18 1 21,30 ,300 0.85% 24,000 0.0625 0.2500 Td =td / tt = 2.6(D)(H-1)/(St) td = Miniumum shell thickness, in inches D = Normal tank diameter, in feet H = depth of tank, in feet G = design Specific gravity of liquid Sd = allowable Str Stre ess fo for De Design co condition E = joint efficiency St = allowable stress 516-60 Hydro Test CA = Corrosion Allowance For Third Course 516-60 PlateĠ.209 50.00 28 1 21,30 ,300 0.85% 24,000 0.0625 0.3750įileName: _office WorkSheet: Steel DesignĪPI 650 Design Calculations Shell Design : td = 2.6(D)(H -1)(G)/Sd= Td =td / tt = 2.6(D)(H-1)/(St) = td = Miniumum shell thickness, in inches =ĭ = Normal Normal tank diameter, in feet = H = depth of tank tank, in feet = G = design Specific gravity of liquid = Sd = allowable Str Stre ess fo for De Design co condition E = joint efficiency St = allowable stress516-60 Hydro Testĥ0.00 32.00 1 21,30 ,300 0.85% 24,000 0.0625ĬA = Corrosion Allowance For Second Course 516-60 Plate Miniumum shell thickness, in inches, t d = td / tt = 2.6(D)(H-1)/(St) td = G = design Specific gravity of liquid Sd = allowable Stress for Design condition E = joint efficiency St = allowable allowable stress 516-60 Hydro Test CA = Corrosion AllowanceĠ.224 in. Fixed cone roof with internal floating roof.įROM FROM ( BOTT BOTTOM OM COUR COURSE SE)) PLA PLATE TO TO (TOP (TOP COU COURS RSE) E) PLA PLATE TE td = 2.6(D)(H -1)(G)/Sd= Items marked with an asterisk ( *) to be completed by Vendor/Fabricator.Ģ. Internals (attach separate sheet, as req'd):Ĥ6 Design Specifications: 47 Tank Insulation ? 49 Fireproofing ?ġ. Operating Temperature 30 Flash Point (Closed Cup) : 31 Negative Pressureģ3 (Hydro)test Pressure expressed in Psig 34 Minimum Fluid Temperature Barr’s team of storage tank emission experts is available to support you with initial setup of BTECS as well as customization for data input, emissions reporting, and compliance tracking.STORAGE TANK SPECIFICATION ng s n ts ts CRUDE OIL StorageĢ9 Vapor Pressure Max. By doing so, you will gain access to our online community where we provide BTECS access and more information related to the tool. Api 650 Tank Calculation Spreadsheet free#
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