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Oil & gas midstreamProcess & water

Camargue Gas Processing Skid

A midstream conditioning and export skid: emergency shutdown valve, two three-phase production separators, pressure control, two export compressors, interstage and export cooling, condensate export and a flare/relief system.

DjiniousCCOperations & SCADA
DjiniousCC
The Camargue gas processing skid overview in DjiniousCC: wellhead ESD valve, two separators, pressure control valve, two compressors, coolers, condensate tank and export pump, with a relief header routed up to the flare stack.
site code
CAMGsite code
assets
12assets
live tags
82live tags
authority class
C4authority classoperational action

Site CAMG, Fos-sur-Mer, France. These are not mock-ups: all five sites run side by side in the same DjiniousCC instance — 99 assets and 693 live tags, acquired at 1 Hz, historised, alarmed, and each with a procedure that has been dry-run and proven on an isolated twin.

A starved compressor walks toward its surge line

A fouled suction filter collapses CMP-01's inlet pressure and mass flow. Anti-surge margin goes negative while CMP-02 idles at part load. Surge damages the machine in seconds, and the operator's instinct — hold export by pushing the sick machine harder — is exactly wrong.

What the platform models here

Each family has a behavioural model that the live simulator and the proving twin share, so a dry-run behaves the way the plant does.

Three-phase separators · Centrifugal compressors · Heat exchangers · ESD & control valves · Condensate tank · Export pump · Flare stack

The procedure: Compressor Anti-Surge Load Transfer

Pull a starved export compressor away from its surge line and hold export throughput: unload CMP-01, transfer duty to CMP-02, open the pressure-control valve to shed back-pressure, and require operator confirmation before the change is applied. Authority class: C4 · operational action.

  1. Step 1

    Unload CMP-01 → 45 %

  2. Step 2

    Load CMP-02 → 92 %

  3. Step 3

    Open PCV-01 → 78 %

  4. Step 4

    Shift-supervisor confirmation

  5. Step 5

    Notify control room

The proof: CMP-01 Suction Restriction

A suction restriction starves CMP-01: inlet pressure and mass flow collapse and the machine enters surge while CMP-02 runs at part load.

Baseline — without the procedure

  • Anti-surge margin ≥ 12 % on both trains — measured −32.3 %
  • CMP-02 export flow ≥ 80 kNm³/h — measured 71.2 kNm³/h

With the procedure — every assertion holds

  • Anti-surge margin ≥ 12 % on both trains — measured +16.6 %
  • CMP-02 export flow ≥ 80 kNm³/h — measured 88.7 kNm³/h

The machine is pulled off the surge line and export is held, both proven before a single command reaches the skid.

What the control room sees

DjiniousCC
The DjiniousCC operator dashboard scoped to the gas skid, showing asset roll-up, availability and a live trend of inlet gas and both compressor export flows.
Inlet gas and both export trains on one trend, so a load transfer is visible as it happens.
DjiniousCC
The DjiniousCC simulation page: a scenario runner with baseline and with-process result panels, and a history of dry-runs showing pass and fail per plant.
The proving ground. Baseline and with-process runs sit side by side, and the history keeps every verdict.
DjiniousCC
The DjiniousCC digital twin view showing the plant hierarchy and asset relationships.
The twin the procedure is grounded in — site, areas, assets and their bound state tags.

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