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Equipment Costing

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Power consumption, PC=PT/?p/?M=PB/?M=QH?/(33,000?p?M) Q= flow rate, H = head, ? = density ... FM material of construction factor. Fiberglass 1.8. Stainless ... – PowerPoint PPT presentation

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Title: Equipment Costing


1
Equipment Costing
  • Chapter 22 (p558-597)
  • CH EN 4253
  • Terry A. Ring

2
Pumps Electric Motors
  • Pump Types (Centrifugal, Gear, Plunger)
  • Centrifugal Pump
  • Size factor, SQ(Head)0.5
  • Base Cost, CBexp(9.2951- 0.6019ln(S)
    0.0519ln(S)2)
  • CpFTFMatCB
  • Fm materials factor see Table 22.21
  • FT pump type factor see Table 22.20
  • Other types of pumps have different CB formulas
  • Electric Motor to drive pump
  • Power consumption, PCPT/?p/?MPB/?MQH?/(33,000?p
    ?M)
  • Q flow rate, H head, ? density
  • Efficiencies (pump and motor) are a function of
    flow rate or break horsepower (power without any
    losses), respectively
  • CBexp5.48660.013141ln(PC)0.053255 ln(PC)2
    0.028628 ln(PC)3-0.0035549ln(PC)4
  • CpFTCB
  • FT motor types factor see Table 22.22
  • ?M90

3
Fans
  • Fan
  • Sizing factor is the volumetric flow rate, Q
  • Different CB formula for different types of fans
  • CPFHFM CB
  • FH Head factor see Table 22.24
  • FM material of construction factor
  • Fiberglass 1.8
  • Stainless steel 2.5
  • Nickel Alloy 5.0
  • Motor size by PCQHt(in. water)/(6,350 ?F?M)
  • ?M 90

4
Blowers
  • Sizing factor is the power consumption, PC
  • Centrifugal (turbo) Blower
  • CBexp6.65470.7900ln(Pc)
  • CPFm-fansCB
  • Motor
  • Motor size by PCQHt(in. water)/(6,350 ?F?M)
  • ?M 90

5
Compressors
  • Compressor types
  • Centrifugal, CBexp7.22230.80ln(PC)
  • Reciprocating, CBexp7.60840.80ln(PC)
  • Screw, CBexp7.76610.7243ln(PC)
  • Size factor is the power consumed, PCPB/?C
  • CPFDriveFMatCB
  • FDrive 1(electric motor), 1.15 (steam), 1.25(gas
    turbine)
  • FMat 1.0 Carbon steel,2.5 SS, 5.0 Nickel Alloy

6
Heat Exchangers
  • Types of Heat exchangers
  • Floating, CBexp11.667-0.8709ln(A)0.09005ln(A
    )2
  • Fixed Head, CBexp11.0545-0.9228ln(A)0.09861l
    n(A)2
  • U-tube, CBexp11.147-0.9186ln(A)0.09790ln(A)
    2
  • Kettle, CBexp11.967-0.8709ln(A)0.09005ln(A)
    2
  • Thermosiphon, CB
  • Double pipe, CBexp7.1248-0.16ln(A)
  • Size Factor is HX area, A
  • CPFpFMatFLCB
  • Pressure Factor, Fp 0.98030.018(P(psig)/100)0.0
    017(P(psig)/100)2
  • Not for double pipe
  • Materials Factor, Fmatab(A/100), a b from
    Table 22.25
  • Tube Length Factor FL 1.25 for 8 ft, 1.0 for 20
    ft. on a sliding scale

7
Fired Heaters
  • Size Factor is the heat duty, Q
  • CBexp0.085050.766ln(Q)
  • CPFPFMatCB
  • FP0.986-0.0035(P(psig)\500)0.0175(P/500)2
  • Fmat1.4 Cr-Mo alloy steel, 1.7 for stainless
    steel

8
Pressure Vessels
  • Storage Tanks
  • Distillation Towers
  • Tray
  • Packed
  • Absorber Towers
  • Stripping Towers

9
Pressure Vessels
  • Sizing Factor is the weight of steel, W
  • Horizontal Vessels, 1,000ltWlt920,00 lb
  • CBexp8.717-0.2330ln(W)0.4333ln(W)2
  • Vertical Vessels, 4,200ltWlt1,000,00 lb
  • CBexp6.775-0.18255ln(W)0.02297ln(W)2
  • Add Platform Costs,
  • Horizontal, 3ltDilt12 ft
  • CPL1580(Di)0.20294
  • Vertical, 3ltDilt21 ft
  • CPL258.1(Di)0.7396(L)0.70684
  • Weight, Wp(Dits)(L0.8Di)ts?s
  • CFMCBCPL
  • FM materials factor see Table 22.26

10
Hoop Stress Calc for thickness, ts
  • Design Pressure is function of operating
    pressure, Po
  • For Pogt 1,000psig use Pd1.1Po
  • For Polt 1,000psig but not for vacuum
  • Pdexp0.606080.91615ln(Po)0.0015655ln(Po)2
  • Thickness
  • ts PdDi/(2SE-1.2 Pd)
  • S max allowable stress for steel is f(T)
  • E weld efficiency (fraction)
  • Minimum wall thickness for given diameters
  • May add extra thickness for wind, corrosion
  • Different calculation for vacuum vessels
  • Also account for leakage when vacuum vessel is
    used

11
Distillation Towers
  • Pressure vessel with plates or packing and
    additional nozzels and manholes
  • Tray Cost
  • CTNTFNTFTTFTMCBT
  • Nno. trays
  • FNT 1 for Ngt20 otherwise FNT2.25/(1.0414NT)
  • FTT tray type, 1.0 sieve, 1.87 bubble cap
  • FTM Materials, f(D)
  • Carbon Steel FTM1.0
  • 316 SS FTM1.4010.0788 Di

12
Packed Distillation Column
  • Pressure vessel with platforms plus packing
  • Packing Cost basis is volume of packing, VP
  • CVpCPKCDR
  • CPK is installed cost per unit volume
  • Distributor cost, CDR

13
Absorbers/Strippers
  • Pressure Vessel plus platforms and packing
  • Separate costs for blowers
  • Separate costs for motors

14
Other process equipment
  • Different sizing factors
  • Different basis cost equations

15
Other Process Equipment
  • Various Size Factors
  • Table 22.32
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