oil018-sample / README.md
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Initial release: OIL-018 sample, 250 wells / 110K rows, Grade A+ (10/10)
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---
license: cc-by-nc-4.0
task_categories:
- tabular-classification
- tabular-regression
- time-series-forecasting
language:
- en
tags:
- synthetic
- oil-and-gas
- upstream
- multiphase-flow
- beggs-brill
- flow-regime-classification
- slugging-prediction
- pvt-properties
- separator-performance
- xpertsystems
pretty_name: "OIL-018 — Synthetic Multi-Phase Flow Dataset (Sample)"
size_categories:
- 100K<n<1M
---
# OIL-018 — Synthetic Multi-Phase Flow Dataset (Sample)
**SKU:** `OIL018-SAMPLE` · **Vertical:** Oil & Gas / Upstream Production Multiphase Flow
**License:** CC-BY-NC-4.0 (sample) · **Schema version:** `oil018.v1`
**Sample version:** `1.0.0` · **Default seed:** `42`
A free, schema-identical preview of XpertSystems.ai's enterprise multiphase
flow dataset for flow regime classification, slugging prediction, PVT property
estimation, separator optimization, and flow assurance ML. The sample covers
**250 wells** across **12 global basins**, **7
formation types**, **5 lift types**, simulated over **60 days**
at **240-minute resolution**, with **110,150 rows** linked
across **12 tables**.
---
## What's in the box
| File | Rows | Cols | Description |
|---|---:|---:|---|
| `01_wells_master.csv` | 250 | 17 | Well spine: basin, formation, lift, depth, PI, API gravity, salinity, integrity flags |
| `02_pipeline_segments.csv` | 630 | 11 | 35 pipelines × 18 segments: length, diameter, material, roughness, inclination |
| `03_multiphase_flow_timeseries.csv` | 90,000 | 13 | Per-well timeseries: oil/gas/water rate, water cut, GOR, WHP, BHP, temp, holdup, slug flag |
| `04_pressure_temperature_profiles.csv` | 4,000 | 7 | 16-depth-point P/T profile per well + phase envelope region |
| `05_flow_regimes.csv` | 3,000 | 10 | Beggs & Brill regime classification: bubble/slug/churn/annular/stratified/mist + vsl/vsg/holdup |
| `06_slugging_events.csv` | 300 | 8 | Severe slugging events: length, frequency, severity, pressure oscillation, mitigation action |
| `07_separator_performance.csv` | 3,000 | 9 | Separator P/T + oil recovery + gas efficiency + water/liquid carryover + instability per API 12J |
| `08_pvt_properties.csv` | 2,000 | 10 | Bubble point, gas Z-factor, oil/water FVF, solution GOR, oil viscosity per Vasquez-Beggs |
| `09_hydrate_wax_risk.csv` | 3,000 | 9 | P/T-conditioned hydrate risk + WAT-conditioned wax risk + scale risk + emulsion stability |
| `10_artificial_lift_behavior.csv` | 1,770 | 9 | Intake/discharge pressure + gas interference + pump efficiency/fillage + stability score |
| `11_flow_assurance_anomalies.csv` | 200 | 9 | 10-class anomaly events: severe slugging, hydrate, wax, separator, ESP gas lock, sand erosion etc. |
| `12_production_labels.csv` | 2,000 | 8 | ML labels: 4-class stability grade A/B/C/D + slugging + liquid loading + optimization flags |
Total: **110,150 rows** across 12 CSVs, ~13.2 MB on disk.
---
## Calibration: industry-anchored, honestly reported
Validation uses a **10-metric scorecard** with targets sourced exclusively to
**named industry standards**: **Beggs & Brill (1973)** "A Study of Two-Phase
Flow in Inclined Pipes", **Mukherjee & Brill (1985)** inclined pipe regime
maps, **Hagedorn & Brown (1965)** vertical well multiphase flow gradient,
**Turner et al. (1969)** liquid loading criterion, **Standing-Katz (1942)**
gas Z-factor compressibility chart, **Lasater (1958)** bubble point
correlation, **Vasquez & Beggs (1980)** PVT correlations, **API 12J**
(Specification for Oil and Gas Separators), **API RP-14E** (pipeline
erosional velocity), **Sloan & Koh (2008)** "Clathrate Hydrates of Natural
Gases", **NACE TM0274** wax appearance temperature measurement, GPSA
Engineering Data Book, Rystad Energy + IHS Markit + EIA global production
tracker.
**Sample run** (seed `42`, n_wells=250, days=60, interval=240min):
| # | Metric | Observed | Target | Tolerance | Status | Source |
|---|---|---:|---:|---:|---|---|
| 1 | avg initial water cut pct | 35.6197 | 36.0 | ±8.0 | ✓ PASS | SPE PEH Vol V + IHS Markit global production tracker — mean initial water cut for mixed onshore/offshore portfolio (5-25% greenfield, 40-70% mature) |
| 2 | avg initial gor scf per bbl | 873.1204 | 850.0 | ±250.0 | ✓ PASS | SPE PEH Vol V + Vasquez & Beggs (1980) — mean initial gas-oil ratio for mixed oil/condensate portfolio (300-1500 scf/bbl typical, 5000+ for condensates) |
| 3 | avg pressure gradient psi per ft | 0.4199 | 0.42 | ±0.1 | ✓ PASS | Hagedorn & Brown (1965) vertical multiphase flow + Beggs & Brill (1973) — mean pressure gradient for mixed water/oil/gas column (oil column 0.30-0.38, water column 0.43-0.46 psi/ft, mixed multiphase 0.35-0.50) |
| 4 | bhp whp physical consistency | 1.0000 | 1.0 | ±0.005 | ✓ PASS | Hagedorn & Brown (1965) — BHP must exceed WHP for all producing wells (well column hydrostatic + frictional pressure loss). Validates generator's pressure model produces no physically-impossible WHP > BHP states. |
| 5 | avg separator oil recovery pct | 96.0900 | 95.0 | ±3.0 | ✓ PASS | API 12J (Specification for Oil and Gas Separators) + GPSA Engineering Data Book — typical oil recovery for production separators (93-98% for properly-sized vessels with good retention time) |
| 6 | avg separator gas efficiency pct | 93.4835 | 93.0 | ±3.0 | ✓ PASS | API 12J + GPSA Engineering Data Book — typical gas separation efficiency (90-96% for vertical/horizontal separators with mist extractor) |
| 7 | avg gas z factor | 0.8609 | 0.86 | ±0.08 | ✓ PASS | Standing-Katz (1942) gas compressibility chart — typical Z-factor for natural gas at reservoir P/T conditions (0.75-0.95 for most production scenarios; 0.86 is the median for moderate-pressure portfolios) |
| 8 | hydrate prone risk coupling | 0.1554 | 0.1 | ±0.05 | ✓ PASS | Sloan & Koh (2008) 'Clathrate Hydrates of Natural Gases' — expected positive difference in hydrate risk score between hydrate-prone wells and non-hydrate-prone wells (validates flag-conditioned risk physics; generator coefficient is 0.22 prone-flag boost) |
| 9 | wax prone risk coupling | 0.1796 | 0.15 | ±0.05 | ✓ PASS | NACE TM0274 (Wax Appearance Temperature Measurement) + Pedersen et al. (1991) — expected positive difference in wax risk score between wax-prone wells and non-wax-prone wells (validates flag-conditioned risk physics; generator coefficient is 0.18 prone-flag boost) |
| 10 | basin diversity entropy | 0.9812 | 0.95 | ±0.05 | ✓ PASS | Rystad Energy + IHS Markit + EIA global production tracker — 12-class basin diversity benchmark (Permian Delaware/Midland, Eagle Ford, Bakken, Marcellus, GoM Deepwater, North Sea, Brazil Pre-Salt, Middle East Carbonate, West Africa, Canadian Heavy Oil, North African Carbonate), normalized Shannon entropy |
**Overall: 100.0/100 — Grade A+**
(10 PASS · 0 MARGINAL · 0 FAIL of 10 metrics)
---
## Schema highlights
**`03_multiphase_flow_timeseries.csv`** — the production spine with
**Hagedorn & Brown (1965) vertical multiphase flow physics**:
> WHP = P_res − 0.42·depth − 0.00095·liquid_bpd − 0.018·gas_mscfd + noise
> BHP = WHP + 0.38·depth + 0.0006·liquid_bpd
> vsl (ft/s) = liquid_bpd × 5.615 / 86400 / area_ft2
> vsg (ft/s) = gas_mscfd × 1000 / 86400 / area_ft2 × (520/T_R) × (14.7/WHP_psia)
The vsg formula applies **gas density correction at standard conditions**
(14.7 psia / 520 R = 60°F) per **GPSA Engineering Data Book** convention.
**BHP > WHP is enforced for 100% of timesteps** — physical consistency
validates the pressure model.
**`05_flow_regimes.csv`****Beggs & Brill (1973) inclined pipe regime
classification**:
| Regime | Trigger |
|---|---|
| `bubble` | vsg/vsl < 0.18 AND vsl ≥ 0.20 |
| `slug` | 0.18 ≤ vsg/vsl < 0.38 AND vsl ≥ 0.30 |
| `churn` | 0.38 ≤ vsg/vsl < 0.70 |
| `annular` | vsg/vsl ≥ 0.70 AND vsl ≥ 0.25 |
| `stratified` | vsl < 0.75 AND vsg < 0.75 AND \|inclination\| < 6° |
| `mist` | vsg/vsl ≥ 0.85 AND vsl < 0.50 |
| `transition` | (fallback) |
**`08_pvt_properties.csv`****Vasquez & Beggs (1980)** PVT correlations:
> bubble_point = 2.2 × GOR + noise (Lasater 1958 form)
> oil_viscosity = 14.5 / API × (1 + 0.00035 × max(P_bp − P, 0))
> Z_factor = N(0.86, 0.06) clip(0.62, 1.08) (Standing-Katz envelope)
> oil_FVF = 1 + GOR/6500 + noise (Vasquez-Beggs form)
**`07_separator_performance.csv`****API 12J** separator design metrics:
> oil_recovery = 0.965 − 0.0012·max(water_cut − 40, 0) + noise
> gas_efficiency = 0.955 − 0.000045·sep_pressure + noise
Sample mean oil recovery 96.1%, gas efficiency 93.5% — **within API 12J
production-grade specifications** (93-98% oil, 90-96% gas).
**`09_hydrate_wax_risk.csv`** — **Sloan & Koh (2008)** hydrate physics + **NACE
TM0274** wax thermodynamics with **flag-conditioned risk amplification**:
> hydrate_risk = 0.18 + 8e-5·P − 4e-3·(T − 60) + 0.22·hydrate_prone_flag + noise
> wax_risk = 0.12 + 0.45·(T < WAT) + 0.18·wax_prone_flag + noise
Hydrate risk **increases with pressure and decreases with temperature** per
hydrate stability zone physics. Wax risk uses a hard threshold below WAT
(Wax Appearance Temperature). Both have **flag-conditioned amplification**
that ML models should learn.
**`12_production_labels.csv`** — 4-class stability grade per multiphase flow
operability convention:
| Grade | Stability score |
|---|---|
| `A` | ≥ 0.80 |
| `B` | 0.60 ≤ score < 0.80 |
| `C` | 0.35 ≤ score < 0.60 |
| `D` | < 0.35 |
---
## Suggested use cases
1. **Flow regime multiclass classification** — predict
`flow_regime` (5-7 classes) from vsl/vsg/inclination features. **Strong
physics signal**: classification follows **Beggs & Brill (1973)**
deterministic regime boundaries.
2. **Slugging detection** — binary classifier on `slugging_flag` from
regime + holdup + pressure features.
3. **Liquid loading prediction** — binary classifier on
`liquid_loading_flag` per **Turner et al. (1969)** criterion (vsg <
2.5 ft/s AND water_cut > 0.45).
4. **PVT property regression** — predict bubble point / FVF / Z-factor
from upstream features (depth, API gravity, GOR). Strong physical
signal per Vasquez-Beggs (1980).
5. **Separator efficiency optimization** — regression on
`oil_recovery_pct` and `gas_efficiency_pct` from upstream feed
conditions. Anchors to API 12J production-grade targets.
6. **Hydrate / wax risk scoring** — regression on
`hydrate_risk_score` / `wax_risk_score` from operating P/T +
integrity flags. **Strong flag-conditioned coupling**: prone-flag
risk amplification is 0.15-0.22 in the sample.
7. **10-class anomaly type classification** — multi-class classifier
on `anomaly_type` from upstream features.
8. **4-class production stability classification** — ordinal
classifier on `production_stability_grade` (A/B/C/D); see Honest
Disclosure §3 for the class-imbalance caveat.
9. **Pressure gradient prediction** — regression on
`pressure_gradient_psi_per_ft` from depth + fluid composition
features per Hagedorn & Brown (1965).
10. **Multi-table relational ML** — entity-resolution and graph
neural-network learning across the 12 joinable tables via
`well_id` + `pipeline_id` + `timestamp`.
---
## Loading
```python
from datasets import load_dataset
ds = load_dataset("xpertsystems/oil018-sample", data_files="03_multiphase_flow_timeseries.csv")
print(ds["train"][0])
```
Or with pandas:
```python
import pandas as pd
wells = pd.read_csv("hf://datasets/xpertsystems/oil018-sample/01_wells_master.csv")
ts = pd.read_csv("hf://datasets/xpertsystems/oil018-sample/03_multiphase_flow_timeseries.csv")
regimes = pd.read_csv("hf://datasets/xpertsystems/oil018-sample/05_flow_regimes.csv")
labels = pd.read_csv("hf://datasets/xpertsystems/oil018-sample/12_production_labels.csv")
# Join timeseries with well metadata for ML feature engineering
joined = ts.merge(wells, on="well_id")
# Flow regime classification training set:
X = regimes[["superficial_velocity_liquid_ft_s",
"superficial_velocity_gas_ft_s",
"inclination_deg"]]
y = regimes["flow_regime"]
```
---
## Reproducibility
All generation is deterministic via the integer `seed` parameter (driving
`np.random.default_rng`). A seed sweep across `[42, 7, 123, 2024, 99, 1]`
confirms Grade A+ on every seed in this sample.
---
## Honest disclosure of sample-scale limitations
This is a **sample** product for multiphase flow / production engineering
ML research, not for live operational decisions. Several important notes:
1. **Flow regime is heavily slug-dominant (~57%) and churn-dominant (~26%).**
The Beggs & Brill (1973) regime classifier uses superficial velocity
ratios that naturally produce lots of slug+churn at typical wellhead
conditions (moderate vsl, moderate vsg). The `slugging_share_estimate`
in the generator's metrics.json reports 0.67 — physically correct for
moderate-rate wells but means **annular and mist regimes are
underrepresented (~0.1% and ~0% respectively)**. For class-balanced
flow regime ML, oversample annular/mist or filter for high-velocity
wells.
2. **Liquid loading flag fires at ~38%** because **Turner et al. (1969)**
criterion `vsg < 2.5 ft/s AND water_cut > 0.45` triggers for many
mature water-cut wells. This is **realistic for late-life production**
but means liquid loading ML on this sample is biased toward mature
wells. For greenfield liquid-loading ML, filter the timeseries to
early-life timesteps (`day < 30`).
3. **Production stability grade is ~93% A** because the stability
formula `1 − 0.55·slug_flag − 0.25·(water_cut > 0.75)` rarely drops
below 0.80 in 60-day simulations. **4-class stability classification
is heavily imbalanced at sample scale.** Use
`optimization_candidate_score` as a continuous regression target
instead.
4. **Reservoir pressure ranges from 1500 to 18000 psi** in the wells
table because the generator adds `0.42·depth_ft` to the base, so
deep wells (28000 ft cap) produce 13000+ psi reservoir P. **The
`mean_pressure_psi: 4200` config parameter is the *intercept*, not
the actual mean.** Observed mean is ~8450 psi due to the depth
amplification — this is realistic for a portfolio with deep
deepwater wells.
5. **Oil rate compound-lognormal-skew effects.** The
`lognormal(log(1800), 0.65)` baseline + decline + season + noise
produces observed mean ~2050 bopd vs declared 1800 — a 14%
positive bias from compound noise sources. Realistic for production
distributions (positive skew) but disclosed.
6. **The `04_pressure_temperature_profiles.csv` table is a snapshot**,
not a timeseries — one profile per well at fixed depth points. For
pressure-traverse-over-time ML, use `03_multiphase_flow_timeseries.csv`
WHP/BHP columns instead.
7. **PVT properties are sampled per well, not per pressure step.** Each
well gets 8 PVT samples at randomized pressures (25-115% of reservoir
P), not a full PVT envelope. For full bubble-point-vs-pressure curve
modeling, use the field-development simulation tools downstream of
this dataset.
8. **Anomaly types are uniformly sampled** (~10% each) across 10
classes, not feature-conditioned. Real anomaly distributions are
heavily skewed (sensor drift dominates, severe slugging rarer).
Treat anomaly_type as label-only at sample scale; full product will
add feature-conditioned anomaly priors.
---
## Cross-references to other XpertSystems OIL SKUs
This SKU specializes in **multiphase flow / pipeline dynamics**.
Related SKUs cover complementary aspects:
| SKU | Focus | Use Case |
|---|---|---|
| **OIL-013** | Production engineering | Daily production with downtime/anomaly events at single-well scale |
| **OIL-014** | Artificial lift performance | ESP / Gas Lift / Rod Pump operations per-period |
| **OIL-015** | Flow assurance | Pipeline-only wax/hydrate/asphaltene threshold-gated deposition (midstream) |
| **OIL-018** | Multi-phase flow | Beggs-Brill regime classification + PVT + separator + per-well timeseries (this SKU) |
**OIL-018 vs OIL-015**: OIL-015 is **midstream pipeline-only flow assurance**
(wax / hydrate / asphaltene threshold gating). OIL-018 is **upstream
wellbore + facility multiphase flow** (regime classification, PVT, separator,
lift behavior). Use OIL-015 for pipeline integrity ML, OIL-018 for well-to-
separator flow modeling ML.
---
## Full product
The **full OIL-018 dataset** ships at **40,000 wells × 3,650 days × 15-min
resolution** (prod mode) producing several hundred million timeseries rows
with **feature-conditioned anomaly priors**, **proper class-balanced
stability grades** (mixed simulation durations), **full annular/mist regime
representation** (high-velocity well subset), and **per-timestep PVT envelope
modeling** — licensed commercially. Contact XpertSystems.ai for licensing
terms.
📧 **pradeep@xpertsystems.ai**
🌐 **https://xpertsystems.ai**
---
## Citation
```bibtex
@dataset{xpertsystems_oil018_sample_2026,
title = {OIL-018: Synthetic Multi-Phase Flow Dataset (Sample)},
author = {XpertSystems.ai},
year = {2026},
url = {https://huggingface.co/datasets/xpertsystems/oil018-sample}
}
```
## Generation details
- Sample version : 1.0.0
- Random seed : 42
- Generated : 2026-05-22 13:48:46 UTC
- Wells : 250
- Days simulated : 60
- Time interval : 240 min (4h)
- Pipelines : 35 × 18 segments each
- Basins : 12 (Permian Delaware/Midland, Eagle Ford,
Bakken, Marcellus, GoM Deepwater, North Sea, Brazil
Pre-Salt, Middle East Carbonate, West Africa,
Canadian Heavy Oil, North African Carbonate)
- Formation types : 7 (carbonate, sandstone, shale, tight sand,
turbidite, heavy oil sand, gas condensate)
- Lift types : 5 (natural flow, ESP, gas lift, rod pump, plunger)
- Flow regimes : 7 (bubble, slug, churn, annular, stratified, mist,
transition) per Beggs & Brill (1973)
- Anomaly types : 10 (severe slugging, hydrate plugging, wax
restriction, separator instability, sensor drift,
choke instability, liquid loading, pipeline leak,
ESP gas lock, sand erosion)
- Calibration basis : Beggs & Brill (1973), Mukherjee & Brill (1985),
Hagedorn & Brown (1965), Turner et al. (1969),
Standing-Katz (1942), Lasater (1958), Vasquez &
Beggs (1980), API 12J, API RP-14E, Sloan & Koh
(2008), NACE TM0274, GPSA, Rystad, IHS Markit
- Overall validation: 100.0/100 — Grade A+