Datasets:

xpertsystems
/

oil024-sample

+---
+license: cc-by-nc-4.0
+task_categories:
+- tabular-classification
+- tabular-regression
+- time-series-forecasting
+language:
+- en
+tags:
+- synthetic
+- oil-and-gas
+- midstream
+- pipeline
+- hydraulics
+- darcy-weisbach
+- swamee-jain
+- leak-detection
+- scada
+- flow-assurance
+- xpertsystems
+pretty_name: "OIL-024 — Synthetic Pipeline Flow Dataset (Sample)"
+size_categories:
+- 100K<n<1M
+---
+# OIL-024 — Synthetic Pipeline Flow Dataset (Sample)
+**SKU:** `OIL024-SAMPLE` · **Vertical:** Oil & Gas / Midstream Pipeline Operations
+**License:** CC-BY-NC-4.0 (sample) · **Schema version:** `oil024.v1`
+**Sample version:** `1.0.0` · **Default seed:** `42`
+A free, schema-identical preview of XpertSystems.ai's enterprise pipeline
+flow dataset for **hydraulic modeling, leak detection, flow assurance,
+SCADA telemetry analytics, pump/compressor optimization, and pipeline
+reliability ML**. The sample covers **55 pipelines** with
+**369 segments** across **10 pipeline types**,
+**10 fluid families**, **10 global regions**, and
+**7 terrain types**, with **150,137 rows** linked
+across **12 tables** spanning **7 days of 180-minute time-
+series**.
+**OIL-024 has the strongest hydraulic-physics anchoring of any OIL SKU**
+— full Swamee-Jain (1976) friction factor + Darcy-Weisbach (1857) pressure
+drop + Newton's cooling thermal model + Sloan-Koh hydrate physics
+implemented end-to-end through 369-segment hydraulic profiles.
+---
+## What's in the box
+| File | Rows | Cols | Description |
+|---|---:|---:|---|
+| `pipeline_master.csv` | 369 | 21 | Pipeline + segment catalog: 10 fluid types × 10 regions × 7 terrains × 5 API 5L grades × 6 coatings × MAOP + design flow + pigging/SCADA flags |
+| `hydraulic_profiles.csv` | 20,664 | 14 | **Darcy-Weisbach pressure drop + Swamee-Jain friction + Reynolds** + flow regime classification (laminar/transition/turbulent) + mass balance error |
+| `thermal_profiles.csv` | 20,664 | 9 | Temperature + ambient + **Newton's cooling heat loss** + thermal gradient + Joule-Thomson cooling |
+| `pump_station_operations.csv` | 3,752 | 9 | API 610 pump performance: RPM + efficiency + suction/discharge pressure + power + cavitation risk |
+| `compressor_operations.csv` | 1,344 | 8 | API 617 compressor performance: compression ratio + efficiency + fuel gas consumption (gas pipelines only) |
+| `valve_operations.csv` | 20,664 | 7 | Per-segment valve operations: position + throttling state + control response latency |
+| `transient_events.csv` | 21 | 8 | 15-class event taxonomy: pump trip, compressor trip, surge, water hammer, slugging, hydrate risk, leak, pigging run, etc. |
+| `flow_assurance.csv` | 20,664 | 8 | Wax / hydrate / slugging risk scores + wax deposition thickness per Sloan-Koh (2008) |
+| `leak_detection.csv` | 3 | 9 | API 1130 + API RP 1175 CPM leak detection: leak rate + pressure signature + detection delay |
+| `corrosion_erosion.csv` | 20,664 | 8 | NACE SP0169 corrosion rate + erosion index + wall loss + leak probability |
+| `scada_telemetry.csv` | 20,664 | 10 | SCADA sensor telemetry: signal value + telemetry latency + quality + drift flag |
+| `optimization_labels.csv` | 20,664 | 8 | **FEATURE-COUPLED ML labels**: optimization score + failure risk + 4-class efficiency grade (A/B/C/D) + recommended action |
+Total: **150,137 rows** across 12 CSVs, ~14.6 MB on disk.
+---
+## Calibration: industry-anchored, honestly reported
+Validation uses a **10-metric scorecard** with targets sourced exclusively to
+**named industry standards**: **Swamee & Jain (1976)** "Explicit equations
+for pipe-flow problems", **Colebrook-White (1939)** turbulent friction
+factor, **Darcy-Weisbach (1857)** pressure drop equation, **Moody (1944)**
+Moody chart, **Reynolds (1883)** laminar-turbulent transition, **Hagen-
+Poiseuille (1839)** laminar friction (64/Re), **API 5L** (Line Pipe), **ASME
+B31.4** (Liquid Hydrocarbon Pipelines), **ASME B31.8** (Gas Transmission
+Pipelines), **API 1130** (Computational Pipeline Monitoring), **API RP
+1175** (Pipeline Leak Detection), **NACE SP0169** (External Corrosion
+Control), **Sloan & Koh (2008)** hydrate thermodynamics, **PHMSA** pipeline
+safety statistics, **CSA Z662** (Canadian Oil/Gas Pipeline Systems),
+**API 610** (Centrifugal Pumps), **API 617** (Axial and Centrifugal
+Compressors), Newton's law of cooling.
+**Sample run** (seed `42`, n_pipelines=55, days=7, interval=180min):
+| # | Metric | Observed | Target | Tolerance | Status | Source |
+|---|---|---:|---:|---:|---|---|
+| 1 | avg diameter in | 21.9704 | 22.0 | ±6.0 | ✓ PASS | API 5L Line Pipe specification + ASME B31.4/B31.8 — mean nominal pipe diameter for mixed transmission portfolio (8-48 inch standard sizes; 22 inch median for mixed crude/gas/refined products mix per PHMSA pipeline inventory) |
+| 2 | avg maop psi | 1501.7934 | 1480.0 | ±250.0 | ✓ PASS | ASME B31.4 (Liquid Hydrocarbon Pipelines) + ASME B31.8 (Gas Transmission) — typical MAOP for transmission pipelines (1000-2000 psi normal range per PHMSA; 1480 psi reflects mixed portfolio mean) |
+| 3 | avg reynolds number | 1069625.4263 | 1000000.0 | ±600000.0 | ✓ PASS | Reynolds (1883) laminar-turbulent transition + Moody (1944) — typical operating Reynolds number for transmission pipelines (200K-2M typical for crude/gas; 1M reflects high-flow turbulent regime per Darcy-Weisbach analysis) |
+| 4 | avg friction factor | 0.0156 | 0.016 | ±0.008 | ✓ PASS | Swamee-Jain (1976) friction factor + Moody (1944) Moody chart — typical Darcy friction factor for turbulent transmission pipeline operation (0.010-0.025 range per ε/D ratios of 0.0001-0.001) |
+| 5 | avg mass balance error pct | 0.1719 | 0.2 | ±0.15 | ✓ PASS | API 1130 Computational Pipeline Monitoring + API RP 1175 — typical mass balance error for SCADA-instrumented pipelines (0.05-0.5% normal; >1% triggers leak alarm per API standards) |
+| 6 | avg pump efficiency pct | 72.7872 | 73.0 | ±6.0 | ✓ PASS | API 610 (Centrifugal Pumps for Petroleum) — typical pump efficiency for transmission pipeline pump stations (68-82% at BEP per Hydraulic Institute; demand-modulated operation reduces from peak) |
+| 7 | thermal heat loss pearson correlation | 0.8272 | 0.75 | ±0.15 | ✓ PASS | Newton's law of cooling (heat_loss ∝ ΔT) — expected strong positive correlation between (pipe_temp - ambient_temp) and heat_loss_btu_hr_ft per fundamental heat transfer physics. Validates generator's thermal model. |
+| 8 | optimization failure pearson correlation | -0.9944 | -0.95 | ±0.1 | ✓ PASS | Generator's deterministic formula: failure_risk = (100 - optimization_score) × 0.7 + leak_prob × 0.3. Near-deterministic inverse coupling validates feature-coupled label generation for pipeline reliability ML. |
+| 9 | corrosion leak pearson correlation | 0.9708 | 0.85 | ±0.1 | ✓ PASS | NACE SP0169 External Corrosion Control + API 1130 + PHMSA pipeline incident data — expected strong positive correlation between corrosion rate and leak probability (generator formula: leak_prob = corrosion/25 × 50 + erosion × 0.12). Validates integrity-leak physics. |
+| 10 | pipeline type diversity entropy | 0.9596 | 0.92 | ±0.04 | ✓ PASS | 10-class pipeline type taxonomy per ASME B31.4/B31.8 + PHMSA classification (crude oil transmission, natural gas transmission, refined products, offshore subsea flowline, multiphase gathering, water injection, CO2 transport, heavy oil diluent, LNG transfer, hydrogen-ready), normalized Shannon entropy |
+**Overall: 100.0/100 — Grade A+**
+(10 PASS · 0 MARGINAL · 0 FAIL of 10 metrics)
+---
+## Schema highlights
+**`pipeline_master.csv`** — 10-class pipeline type taxonomy per **PHMSA /
+ASME B31.4 / B31.8**:
+| Type | Weight | Typical Fluid |
+|---|---:|---|
+| crude_oil_transmission | 20% | crude (light/medium/heavy) |
+| natural_gas_transmission | 18% | dry/wet gas |
+| refined_products | 11% | gasoline / diesel / jet |
+| offshore_subsea_flowline | 10% | multiphase |
+| multiphase_gathering | 12% | mixed wellhead fluids |
+| water_injection | 7% | brine / produced water |
+| co2_transport | 6% | CO2 (dense phase) |
+| heavy_oil_diluent | 6% | bitumen + diluent |
+| lng_transfer | 5% | LNG (cryogenic) |
+| hydrogen_ready | 5% | H2 / H2 blends |
+Material grades: API 5L X42 / X52 / X60 / X65 / X70 — standard transmission-
+grade pipe per **API 5L specification**.
+**`hydraulic_profiles.csv`** — **Swamee-Jain (1976) friction + Darcy-Weisbach (1857)
+pressure drop** implementation:
+> Re        = ρ × v × D / μ                                       (Reynolds 1883)
+> f_lam     = 64 / Re                                              (Hagen-Poiseuille, Re < 2300)
+> f_turb    = 0.25 / [log10(ε/(3.7D) + 5.74/Re^0.9)]²              (Swamee-Jain)
+> dp_friction = f × (L/D) × (ρ × v² / 2)                          (Darcy-Weisbach)
+> dp_elev   = ρ × g × Δh                                           (Bernoulli)
+> dp_total  = (dp_friction + dp_elev) × wax_factor
+PVT-aware fluid properties for 10 fluid families with temperature and
+pressure dependence:
+| Fluid | Density (kg/m³) | Viscosity (Pa·s) |
+|---|---:|---|
+| Light crude | ~790 × (1 - 0.00038·ΔT) | 0.004 × exp(-0.022·(T-100)) |
+| Medium crude | ~850 | 0.018 |
+| Heavy crude | ~930 | 0.12 |
+| Dry gas | 48 × (P/1000) × (520/T_R) | 1.2e-5 |
+| LNG | 430 × (1 - 0.0006·(T+260)) | 1.2e-4 |
+| CO2 | 700 × (P/1500)^0.15 | 7e-5 |
+| Hydrogen blend | 18 × (P/1000) × (520/T_R) | 9e-6 |
+**`thermal_profiles.csv`** — **Newton's law of cooling**:
+> heat_loss_btu_hr_ft ∝ (pipe_temp - ambient_temp)
+> joule_thomson_cooling ∝ pressure_drop  (gas pipelines, ~0.002 multiplier)
+The sample's **(temp-ambient) ↔ heat_loss Pearson correlation is r ≈ +0.83**
+— **strong positive coupling validates Newton's cooling physics**.
+**`flow_assurance.csv`** — **Sloan-Koh (2008) hydrate physics**:
+> wax_risk     = (118 - temp_f) × 1.8 + viscosity × 0.35 + current_wax × 600
+> hydrate_risk = (95 - temp_f) × 2.2 + pressure/50 + 20·is_gas
+> slugging_risk = multiphase × N(45, 15) + 20 × |sin(t/7)|
+**`leak_detection.csv`** — **API 1130 + API RP 1175** computational pipeline
+monitoring leak detection:
+> leak_rate_bpd          = lognormal(2.8, 0.9) clip 2-850
+> pressure_signature     = 50 + leak_rate/8 + noise
+> detection_delay_sec    = lognormal(7.0, 0.8) clip 60-86400
+**`optimization_labels.csv`** — **deterministic feature-coupled labels**:
+> opt_score = 100 - |demand - 0.92| × 60 - max(wax, hydrate) × 0.18 - leak_prob × 0.22 - anomaly × 8
+> failure_risk = (100 - opt_score) × 0.7 + leak_prob × 0.3
+> grade = 'A' if opt_score ≥ 85 else 'B' if ≥ 70 else 'C' if ≥ 55 else 'D'
+The sample's optimization↔failure Pearson correlation is r ≈ **−0.994** —
+**near-deterministic inverse coupling validates formula-level label
+generation**.
+---
+## Suggested use cases
+1. **Pressure drop prediction** — regression on `pressure_drop_psi` from
+   flow + diameter + roughness + temp features. **Strong physics**:
+   Darcy-Weisbach signal validated.
+2. **Friction factor prediction** — predict `friction_factor` from
+   Reynolds + roughness ratio per Swamee-Jain / Moody chart.
+3. **Leak probability scoring** — regression on `leak_probability_score`
+   per NACE SP0169 + API 1130. **Strong physics**: corrosion-leak r ≈ +0.97.
+4. **Flow assurance binary classification** — predict `flow_assurance_state
+   == 'critical'` from temperature + viscosity + pressure features per
+   Sloan-Koh.
+5. **Wax deposition forecasting** — time-series forecasting of
+   `wax_deposition_thickness_mm` per coupled accumulation physics.
+6. **Pipeline efficiency grade classification** — 4-class ordinal
+   classifier on `efficiency_grade` (A/B/C/D). **Strong feature
+   coupling** — models WILL learn meaningful patterns.
+7. **Pump cavitation prediction** — regression on `cavitation_risk_score`
+   from RPM + demand features per API 610 + Hydraulic Institute.
+8. **15-class transient event classification** — multi-class classifier
+   on `event_type` (rare events at sample scale; see Honest Disclosure §1).
+9. **Mass balance anomaly detection** — anomaly detection on
+   `mass_balance_error_pct` per API 1130 CPM leak detection.
+10. **Multi-table relational ML** — entity-resolution + graph neural-
+    network learning across the 12 joinable tables via `pipeline_id`,
+    `segment_id`, `timestamp`.
+---
+## Loading
+```python
+from datasets import load_dataset
+ds = load_dataset("xpertsystems/oil024-sample", data_files="hydraulic_profiles.csv")
+print(ds["train"][0])
+```
+Or with pandas:
+```python
+import pandas as pd
+master = pd.read_csv("hf://datasets/xpertsystems/oil024-sample/pipeline_master.csv")
+hyd    = pd.read_csv("hf://datasets/xpertsystems/oil024-sample/hydraulic_profiles.csv")
+thm    = pd.read_csv("hf://datasets/xpertsystems/oil024-sample/thermal_profiles.csv")
+fa     = pd.read_csv("hf://datasets/xpertsystems/oil024-sample/flow_assurance.csv")
+labels = pd.read_csv("hf://datasets/xpertsystems/oil024-sample/optimization_labels.csv")
+# Full multi-table feature engineering:
+joined = (hyd
+    .merge(thm, on=["timestamp", "pipeline_id", "segment_id"])
+    .merge(fa,  on=["timestamp", "pipeline_id", "segment_id"])
+    .merge(labels, on=["timestamp", "pipeline_id", "segment_id"])
+    .merge(master, on=["pipeline_id", "segment_id"]))
+# Predict efficiency_grade from hydraulics + thermal + flow assurance features
+```
+---
+## 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 calibrated for pipeline ML research, not for
+live operational decisions. Several notes:
+1. **Flow regime is ~100% turbulent** because transmission pipeline
+   Reynolds numbers naturally exceed 4000 (sample mean Re ≈ 1.1M).
+   **Laminar regime is essentially absent at sample scale** — only
+   pipelines with very viscous fluids (heavy crude) at very low flow
+   rates would produce laminar flow. For laminar-regime ML, filter to
+   `primary_fluid == 'heavy_crude' AND flow_bpd < 5000` or wait for the
+   full product which adds explicit low-flow scenarios.
+2. **Pump cavitation risk is ~0** because the generator's formula
+   `(rpm - 2700)/12 + N(0, 5)` clips at 0 for typical 1750 rpm
+   operation. Real cavitation risk requires NPSH-margin physics
+   (OIL-021 implements this correctly). For pump cavitation ML, use
+   OIL-021 instead; OIL-024 cavitation is a placeholder.
+3. **Integrity state is 100% 'normal'** at 7-day sample horizon because
+   `leak_probability > 40` threshold (for 'watch' classification)
+   requires longer-horizon corrosion accumulation. The full product
+   (30-day prod mode) and full-scale simulations show meaningful
+   'watch' and 'high_risk' populations. For integrity-state
+   classification ML, use the full product or augment with
+   external corrosion-progression simulations.
+4. **Transient events are sparse** (~20 events per 55 pipelines at
+   sample scale). For 15-class event-type classification ML, **use the
+   full product** (12000+ pipelines for 30 days) or **filter to
+   pipeline-day aggregated event flags** rather than per-timestep
+   events.
+5. **Leak events are very rare** (~3 leak entries across 55 pipelines).
+   Leak ML requires the full product. For leak detection ML at sample
+   scale, **use `leak_probability_score` regression** rather than the
+   binary leak flag.
+6. **Sensor drift flag rate is ~0.04%** because the generator only
+   sets `drift_flag = True` when `event_type == 'sensor_drift'`, which
+   is one of 15 event types at 0.6% rare event rate. For sensor drift
+   ML, use full product or rely on signal-quality `quality_flag`
+   instead.
+7. **Flow ↔ pressure drop correlation is weak (r ≈ +0.06)** because the
+   relationship is dominated by **between-segment** variance in
+   diameter, length, and fluid type rather than **within-segment**
+   flow-pressure scaling. **For Darcy-Weisbach ML, normalize pressure
+   drop per-segment** (dp/L or use friction factor) before fitting.
+   Within a single segment, the relationship is strong (r > 0.85
+   typically).
+8. **Flow assurance critical rate is ~38%** — higher than realistic
+   field operation (5-15% typical). The generator's wax_risk formula
+   `(118-temp) × 1.8` triggers easily at ambient temperatures; real
+   field operation includes insulation and heat-tracing that reduces
+   wax onset. For realistic flow assurance ML, **filter critical
+   classifications by insulation type** (`insulation_type in
+   ['high', 'subsea_wet_insulated']` for realistic
+   thermal-protected operation).
+---
+## Cross-references to other XpertSystems OIL SKUs
+This SKU is the **second midstream SKU** in the catalog (after OIL-015 flow
+assurance):
+| SKU | Layer | Focus |
+|---|---|---|
+| OIL-015 | Midstream | Pipeline flow assurance (wax / hydrate / asphaltene threshold gating) |
+| **OIL-024** | **Midstream** | **Full pipeline hydraulics + SCADA + leak detection + transient events** *(this SKU)* |
+| OIL-018 | Upstream | Wellbore-to-separator multiphase flow (Beggs-Brill regime classification) |
+**OIL-024 vs OIL-015**: OIL-015 specializes in **flow-assurance-only**
+threshold-gated wax/hydrate/asphaltene deposition. **OIL-024 is the
+comprehensive midstream pipeline operations dataset** — full Swamee-Jain
+hydraulics + Darcy-Weisbach pressure drop + thermal profiles + SCADA
+telemetry + leak detection + 15-class transient event taxonomy + 10-fluid-
+type PVT-aware physics. Use OIL-015 for flow-assurance ML specifically,
+**OIL-024 for general pipeline operations / SCADA / hydraulic ML**.
+**OIL-024 vs OIL-018**: OIL-018 simulates **wellbore-to-separator**
+multiphase flow with Beggs-Brill regime classification (upstream).
+**OIL-024 simulates midstream transmission pipelines** with single-phase
+or multiphase flow assurance (downstream of separator). Use OIL-018 for
+upstream production multiphase ML, OIL-024 for **midstream transmission
+pipeline ML**.
+---
+## Full product
+The **full OIL-024 dataset** ships at **12,000 pipelines × 30 days × 60-min
+interval** (prod mode) producing tens of millions of rows with **richer
+event populations** (1000+ events for class-balanced 15-class ML), **full
+NPSH-conditioned pump cavitation physics**, **multi-day leak event
+populations**, **realistic flow assurance critical rates** (insulation-
+conditioned), and **explicit laminar-flow scenarios** (heavy-crude low-flow
+regimes) — licensed commercially. Contact XpertSystems.ai for licensing
+terms.
+📧 **pradeep@xpertsystems.ai**
+🌐 **https://xpertsystems.ai**
+---
+## Citation
+```bibtex
+@dataset{xpertsystems_oil024_sample_2026,
+  title  = {OIL-024: Synthetic Pipeline Flow Dataset (Sample)},
+  author = {XpertSystems.ai},
+  year   = {2026},
+  url    = {https://huggingface.co/datasets/xpertsystems/oil024-sample}
+}
+```
+## Generation details
+- Sample version    : 1.0.0
+- Random seed       : 42
+- Generated         : 2026-05-22 21:05:15 UTC
+- Pipelines         : 55
+- Segments          : 369 (avg 6.7 per pipeline)
+- Simulation days   : 7
+- Time-step interval: 180 minutes
+- Fluid families    : 10 (light/medium/heavy crude, dry/wet gas,
+                      refined product, water, CO2, LNG, hydrogen blend)
+- Pipeline types    : 10 (crude oil / natural gas /
+                      refined products / offshore subsea / multiphase
+                      gathering / water injection / CO2 transport / heavy
+                      oil diluent / LNG / hydrogen-ready)
+- Regions           : 10 (Permian Basin, Gulf Coast, North Sea,
+                      Middle East, Canadian Oil Sands, Offshore Brazil,
+                      West Africa, Alaska Arctic, Rocky Mountains,
+                      Appalachia)
+- Terrains          : 7 (flat, rolling, mountainous,
+                      offshore, subsea, arctic, desert)
+- Event types       : 15 (pump trip, compressor trip, valve throttle,
+                      emergency shutdown, restart, surge, water hammer,
+                      slugging, hydrate risk, wax deposition, SCADA
+                      outage, sensor drift, leak, corrosion alarm,
+                      pigging run)
+- Calibration basis : Swamee-Jain (1976), Darcy-Weisbach (1857), Moody
+                      (1944), Reynolds (1883), Hagen-Poiseuille (1839),
+                      Colebrook-White (1939), API 5L, ASME B31.4/B31.8,
+                      API 1130, API RP 1175, NACE SP0169, Sloan-Koh
+                      (2008), PHMSA, CSA Z662, API 610, API 617
+- Overall validation: 100.0/100 — Grade A+

compressor_operations.csv ADDED Viewed