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Gas Dewatering Calculator

McKetta-Wehe ยท GPSA ยท Pipeline Dehydration Specs

Gas Dewatering Requirements Calculator
Evaluates natural gas dewatering needs for pipeline transport. Calculates water content at operating conditions using McKetta-Wehe correlation, determines required water removal rate, and recommends the optimal dehydration method based on dewpoint depression.

Gas Flow & Conditions

MMSCFD
psig
°F
air=1.0

Water Content & Dewpoint Spec

lb/MMSCF
°F
Dewpoint Specs

Pipeline tariffs typically require <7 lb/MMSCF or a water dewpoint of 32°F. Cryogenic plants need <1 ppmv (<0.1 lb/MMSCF). Arctic pipelines may require -40°F dewpoint.

Acid Gas Content (Optional)

mol%
mol%
/* McKetta-Wehe Water Content */
W = A × exp(B / T) / P
// W = lb H2O/MMSCF at P and T
// Corrected for acid gas and SG

About This Calculator

Evaluates gas dewatering requirements using McKetta-Wehe water content correlation and GPSA dehydration method selection guidelines.

Calculations Include:

  • Inlet Water Content: McKetta-Wehe chart correlation with acid gas correction
  • Outlet Water Content: From required dewpoint specification
  • Water Removal Rate: Daily and hourly removal requirements
  • Method Recommendation: TEG, molecular sieve, refrigeration, or CaCl2
  • TEG Circulation: Estimated glycol rate if TEG is recommended

โšก Quick Reference โ€” Dewatering Methods

TEG Glycol: 30-80°F depression
Mol. Sieve: >100°F depression
Refrigeration: 20-60°F depression
CaCl2: 15-30°F depression
Pipeline Spec: <7 lb/MMSCF
Cryogenic: <0.1 lb/MMSCF

Dehydration Method Comparison

Method Dewpoint Cost
TEG Glycol -40 to 32°F Low-Med
DEG Glycol 0 to 40°F Low
Mol. Sieve -150 to -60°F High
Refrigeration 15 to 40°F Med-High
CaCl2 30 to 50°F Very Low
Water Content vs. Dewpoint

Water content in natural gas is determined by temperature and pressure. Higher temperatures increase water carrying capacity while higher pressures reduce it. The McKetta-Wehe chart is the industry-standard method for sweet gas; acid gas correction factors are applied for CO2 and H2S content per GPSA.

Hydrate Prevention

Gas dewatering is the primary method for preventing hydrate formation. Reducing water content below the saturation point at the coldest expected pipeline temperature eliminates free water and prevents hydrate nucleation. For gathering systems, target a dewpoint 15-20°F below the minimum ground temperature.

References

  • GPSA Engineering Data Book, Sections 20-21
  • McKetta-Wehe Water Content Chart
  • Campbell Gas Conditioning and Processing
  • API 14E โ€” Pipeline Sizing