Dry Gas Seal Screening
Use this skill for public, educational dry gas seal screening on centrifugal compressors. It estimates the seal-gas and separation-gas supply demand from the primary seal leakage rate and flags retrograde-condensation risk by comparing the seal cavity temperature against a hydrocarbon dew point at the seal/vent reference condition.
When to Use
- When a user asks whether a compressor dry gas seal has adequate seal-gas supply margin.
- When an agent needs a quick condensation-risk triage for the primary vent / standpipe dead-leg before a detailed seal study.
- When examples must run without confidential seal vendor data, machine line lists, or project seal-gas conditioning specifications.
Inputs
seal_leakage_rate_nl_per_min: primary seal leakage rate at standard conditions in NL/min per seal.
seal_cavity_temperature_c: seal cavity (process-side) temperature in degrees C.
hydrocarbon_dew_point_c: hydrocarbon dew point at the seal/vent reference condition in degrees C.
seal_count: number of seals supplied (default 2: drive end and non-drive end).
supply_margin: seal-gas supply margin over leakage, dimensionless, default 1.25.
separation_gas_rate_nl_per_min: separation (secondary) gas rate per seal in NL/min, default 0.0.
Outputs
total_seal_gas_supply_nl_per_min: screening seal-gas supply demand.
separation_gas_supply_nl_per_min: screening separation-gas supply demand.
seal_gas_supply_margin_ratio: the applied supply margin over leakage.
condensation_margin_c: seal cavity temperature minus the hydrocarbon dew point.
condensation_warning: ok, watch, or high (a small or negative margin means higher condensation risk).
assumptions: public assumptions used by the placeholder model.
Engineering Method
The Python class DryGasSealModel uses open, public concepts only:
- seal-gas supply demand is the primary seal leakage multiplied by the seal count and a supply margin, reflecting the API 692 intent that supply must exceed leakage to keep the seal faces clean.
- separation-gas supply demand scales with the seal count.
- the condensation margin compares the seal cavity temperature against a hydrocarbon dew point at the seal/vent reference condition. A small or negative margin flags retrograde condensation risk in the primary vent piping and standpipe dead-legs, which is the failure mode that seal-gas conditioning units exist to prevent.
This is educational and screening-only logic. It is not a seal vendor method, not a seal-gas conditioning design, and not a replacement for validated dry gas seal analysis and a qualified rotating-equipment review.
Python Usage Pattern
from dry_gas_seal_screening import DryGasSealModel
model = DryGasSealModel()
result = model.evaluate(
seal_leakage_rate_nl_per_min=280.0,
seal_cavity_temperature_c=44.0,
hydrocarbon_dew_point_c=40.0,
seal_count=2,
supply_margin=1.25,
separation_gas_rate_nl_per_min=120.0,
)
print(result.condensation_warning)
print(result.total_seal_gas_supply_nl_per_min)
print(result.condensation_margin_c)
If the optional neqsim Python package is available, the result records that fact so an agent can recommend moving to validated NeqSim seal-gas dew-point and condensation analysis. If it is not installed, the example still runs with public placeholder logic.
Validation Checklist
Common Mistakes
| Symptom |
Cause |
Fix |
| Condensation never flagged |
Dew point taken at cavity pressure instead of the vent/expanded condition |
Use the hydrocarbon dew point at the seal/vent reference condition |
| Supply demand looks low |
Supply margin set to 1.0 |
Use a supply margin above 1.0 consistent with the seal-gas control philosophy |
| Wrong total supply |
Seal count not matching the machine arrangement |
Set seal_count to the actual number of seals supplied |
Limitations
- No seal vendor leakage curves, clearance models, or qualification data are included.
- No isenthalpic (Joule-Thomson) expansion or transient standpipe cooldown is modelled.
- No seal-gas conditioning unit (heater/separator) sizing is performed.
- Not suitable for safety-critical, design, guarantee, or standards-compliance work.
Related NeqSim Functionality
This educational screening corresponds to validated, rigorous functionality in the NeqSim Java library that a qualified engineer should use for design-grade work:
neqsim.process.equipment.compressor.DryGasSealAnalyzer — isenthalpic seal-gap expansion, retrograde condensation mapping, dead-leg cooldown, condensate accumulation, and seal-gas conditioning unit sizing per API 692.
neqsim.process.measurementdevice.HydrocarbonDewPointAnalyser — hydrocarbon dew-point evaluation for the seal-gas stream.
neqsim.process.equipment.valve.ThrottlingValve — Joule-Thomson expansion modelling across the seal gap.
In Python the same classes are reachable through the neqsim package (for example from neqsim import jneqsim).
References
1---2name: neqsim-dry-gas-seal-screening3description: Educational dry gas seal supply and condensation screening for centrifugal compressors. USE WHEN: a task needs a public, screening-level estimate of seal-gas and separation-gas supply demand and a seal-gas condensation-margin check (cavity temperature versus hydrocarbon dew point) before detailed dry gas seal system design per API 692.4---56# Dry Gas Seal Screening78Use this skill for public, educational dry gas seal screening on centrifugal compressors. It estimates the seal-gas and separation-gas supply demand from the primary seal leakage rate and flags retrograde-condensation risk by comparing the seal cavity temperature against a hydrocarbon dew point at the seal/vent reference condition.910## When to Use1112- When a user asks whether a compressor dry gas seal has adequate seal-gas supply margin.13- When an agent needs a quick condensation-risk triage for the primary vent / standpipe dead-leg before a detailed seal study.14- When examples must run without confidential seal vendor data, machine line lists, or project seal-gas conditioning specifications.1516## Inputs1718- `seal_leakage_rate_nl_per_min`: primary seal leakage rate at standard conditions in NL/min per seal.19- `seal_cavity_temperature_c`: seal cavity (process-side) temperature in degrees C.20- `hydrocarbon_dew_point_c`: hydrocarbon dew point at the seal/vent reference condition in degrees C.21- `seal_count`: number of seals supplied (default 2: drive end and non-drive end).22- `supply_margin`: seal-gas supply margin over leakage, dimensionless, default 1.25.23- `separation_gas_rate_nl_per_min`: separation (secondary) gas rate per seal in NL/min, default 0.0.2425## Outputs2627- `total_seal_gas_supply_nl_per_min`: screening seal-gas supply demand.28- `separation_gas_supply_nl_per_min`: screening separation-gas supply demand.29- `seal_gas_supply_margin_ratio`: the applied supply margin over leakage.30- `condensation_margin_c`: seal cavity temperature minus the hydrocarbon dew point.31- `condensation_warning`: `ok`, `watch`, or `high` (a small or negative margin means higher condensation risk).32- `assumptions`: public assumptions used by the placeholder model.3334## Engineering Method3536The Python class `DryGasSealModel` uses open, public concepts only:3738- seal-gas supply demand is the primary seal leakage multiplied by the seal count and a supply margin, reflecting the API 692 intent that supply must exceed leakage to keep the seal faces clean.39- separation-gas supply demand scales with the seal count.40- the condensation margin compares the seal cavity temperature against a hydrocarbon dew point at the seal/vent reference condition. A small or negative margin flags retrograde condensation risk in the primary vent piping and standpipe dead-legs, which is the failure mode that seal-gas conditioning units exist to prevent.4142This is educational and screening-only logic. It is not a seal vendor method, not a seal-gas conditioning design, and not a replacement for validated dry gas seal analysis and a qualified rotating-equipment review.4344## Python Usage Pattern4546```python47from dry_gas_seal_screening import DryGasSealModel4849model = DryGasSealModel()50result = model.evaluate(51 seal_leakage_rate_nl_per_min=280.0,52 seal_cavity_temperature_c=44.0,53 hydrocarbon_dew_point_c=40.0,54 seal_count=2,55 supply_margin=1.25,56 separation_gas_rate_nl_per_min=120.0,57)5859print(result.condensation_warning)60print(result.total_seal_gas_supply_nl_per_min)61print(result.condensation_margin_c)62```6364If the optional `neqsim` Python package is available, the result records that fact so an agent can recommend moving to validated NeqSim seal-gas dew-point and condensation analysis. If it is not installed, the example still runs with public placeholder logic.6566## Validation Checklist6768- [ ] Inputs are in the documented units (NL/min, degrees C).69- [ ] Example inputs are public and synthetic.70- [ ] Tests cover ok, watch, high, and invalid-input cases.71- [ ] Results are described as educational screening indicators.72- [ ] Real seal system design is redirected to validated methods, API 692, and qualified review.7374## Common Mistakes7576| Symptom | Cause | Fix |77| --- | --- | --- |78| Condensation never flagged | Dew point taken at cavity pressure instead of the vent/expanded condition | Use the hydrocarbon dew point at the seal/vent reference condition |79| Supply demand looks low | Supply margin set to 1.0 | Use a supply margin above 1.0 consistent with the seal-gas control philosophy |80| Wrong total supply | Seal count not matching the machine arrangement | Set `seal_count` to the actual number of seals supplied |8182## Limitations8384- No seal vendor leakage curves, clearance models, or qualification data are included.85- No isenthalpic (Joule-Thomson) expansion or transient standpipe cooldown is modelled.86- No seal-gas conditioning unit (heater/separator) sizing is performed.87- Not suitable for safety-critical, design, guarantee, or standards-compliance work.8889## Related NeqSim Functionality9091This educational screening corresponds to validated, rigorous functionality in the NeqSim Java library that a qualified engineer should use for design-grade work:9293- `neqsim.process.equipment.compressor.DryGasSealAnalyzer` — isenthalpic seal-gap expansion, retrograde condensation mapping, dead-leg cooldown, condensate accumulation, and seal-gas conditioning unit sizing per API 692.94- `neqsim.process.measurementdevice.HydrocarbonDewPointAnalyser` — hydrocarbon dew-point evaluation for the seal-gas stream.95- `neqsim.process.equipment.valve.ThrottlingValve` — Joule-Thomson expansion modelling across the seal gap.9697In Python the same classes are reachable through the `neqsim` package (for example `from neqsim import jneqsim`).9899## References100101- NeqSim repository: https://github.com/equinor/neqsim102- NeqSim Skills Guide: https://github.com/equinor/neqsim/blob/master/docs/integration/skills_guide.md103- Public rotating-equipment references such as API 692 (Dry Gas Sealing Systems) and API 614 (Lubrication, Shaft-Sealing, and Oil-Control Systems) for general seal-gas concepts.