πŸŒ€ Compressor Performance Estimator

Polytropic Head β€’ Discharge Temperature β€’ Stages β€’ Power β€’ Z-effect β€’ Anti-surge (Screening)

Scope: Polytropic compression screening for centrifugal/axial style estimation. Anti-surge is an approximate control-line estimate; real surge line must come from OEM map.

Suction / Discharge Conditions

Gas Properties

Performance Assumptions

Flow

Staging Limits (Design Rules)

Anti-surge (Screening)

Compression Results

Overall Pressure Ratio, PR: -
Polytropic Exponent used, n: -
Avg Compressibility, Zavg: -
Polytropic Head, Hp: -
Discharge Temperature, T2: -

Staging Estimate

Stages Required (by PR & T2): -
Estimated Stage PR: -
Estimated T2 per Stage: -

Power

Gas Power (shaft), Pgas: -
Driver Power, Pdriver: -

Anti-surge (Screening)

Estimated Surge Control Flow: -
Recommended Min Operating Flow: -
Formulas (screening):
1) Overall pressure ratio: PR = P2/P1
2) If n is blank, an effective polytropic exponent is derived from k and Ξ·p using:   (nβˆ’1)/n = (kβˆ’1)/(kΒ·Ξ·p)   β‡’   n = 1 / (1 βˆ’ (kβˆ’1)/(kΒ·Ξ·p))
3) Polytropic head (per kg): Hp = (n/(nβˆ’1)) Β· (ZavgΒ·RspecΒ·T1) Β· (PR((nβˆ’1)/n) βˆ’ 1)
4) Discharge temperature (polytropic path): T2 = T1 Β· PR((nβˆ’1)/n)
5) Specific gas constant: Rspec = Ru/MW, with Ru=8314.462618 J/(kmolΒ·K)
6) Power: Pgas = ṁ(kg/s) · Hp (W); Driver power = Pgas /(ηm·ηd)
Note: Zavg is taken as (Z1+Z2)/2 for screening. For rigorous work use an EOS and OEM map.

Technical Notes

Purpose: This tool is intended for preliminary/screening estimates for compressor polytropic head, discharge temperature, staging and power. Final selection and surge control must be based on the OEM compressor map and validated real-gas properties (EOS) for the specified composition and operating envelope.

Variable Definitions

P1, P2 = suction & discharge absolute pressure (bar(a))
T1 = suction temperature (Β°C), converted internally to Kelvin (K)
T2 = estimated discharge temperature (Β°C) along a polytropic path
PR = overall pressure ratio = P2/P1 (dimensionless)
MW = molecular weight (kg/kmol)
k = Cp/Cv at suction (dimensionless)
Z1, Z2 = compressibility factors at suction & discharge (dimensionless); Zavg=(Z1+Z2)/2 (screening)
Ξ·p = polytropic efficiency (dimensionless, 0–1)
n = polytropic exponent (dimensionless). If provided by user it is treated as the actual exponent.
ṁ = mass flow rate (kg/h), converted internally to kg/s
Hp = polytropic head per unit mass (J/kg, shown as kJ/kg)
Pgas = gas power at shaft (kW), Pdriver = required driver power (kW) including Ξ·m and Ξ·d

Formulas / Logic

1) Polytropic exponent:
If n is blank, an effective n is derived from k and Ξ·p using: (nβˆ’1)/n = (kβˆ’1)/(kΒ·Ξ·p). This is a common compressor screening relationship linking efficiency to the effective polytropic path.

2) Discharge temperature (screening):
T2 = T1 Β· PR^((nβˆ’1)/n) (Kelvin). (For rigorous prediction, use EOS + vendor polytropic correlations).

3) Polytropic head:
Hp = (n/(nβˆ’1)) Β· (Zavg Β· Rspec Β· T1) Β· (PR^((nβˆ’1)/n) βˆ’ 1).
Rspec = Ru/MW where Ru = 8314.462618 J/(kmolΒ·K).

4) Power:
Pgas = ṁ · Hp. Driver power = Pgas/(ηm·ηd).

5) Staging estimate:
Stages are estimated from (a) maximum allowable per-stage PR and (b) temperature limit per-stage based on intercooling assumption. This is a design-rule check only; OEM maps and mechanical limits govern final stage count/casing selection.

6) Anti-surge screening:
If suction volumetric flow is not provided, Q1 is estimated from ideal-gas density with Z1: ρ1 = P1·MW / (Z1·Ru·T1). Then Q1 = ṁ/ρ1. The surge control flow and minimum operating flow are screening heuristics; actual surge and control lines must be derived from the OEM map and control philosophy.

Assumptions / Notes / References

β€’ Preliminary estimation tool; not a substitute for OEM performance curves or test procedures.
β€’ Real-gas behavior is approximated via user-provided Z1 and Z2; for high pressure/complex mixtures, use an EOS (e.g., Peng–Robinson) from a simulator.
β€’ Applicable industry references for terminology and compressor practice include API 617 (axial & centrifugal compressors) and performance/testing practices such as ASME PTC 10 (compressor performance test code).
β€’ Temperature limits depend on gas, seals, metallurgy, lube oil, and vendor limitsβ€”always confirm allowable T2 with project/vendor data sheets.
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