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CAMG · Oil & gas midstream

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.

The Camargue gas processing skid overview in Djinious: 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.
Wellhead to export, with the relief header routed clear of the equipment frames to the flare — the way it sits on the real drawing.Rhodanien Midstream · Fos-sur-Mer, France
12
assets modelled
82
live tags at 1 Hz
5
procedure steps
2
assertions checked
EQUIPMENT

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 STANDING PROBLEM

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.

THE PROCEDURE

Compressor Anti-Surge Load Transfer

compressor-antisurge-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.

  1. 01Unload CMP-01 → 45 %
  2. 02Load CMP-02 → 92 %
  3. 03Open PCV-01 → 78 %
  4. 04Shift-supervisor confirmation
  5. 05Notify control room

C4 · operational action

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.

Assertion results for the CMP-01 Suction Restriction scenario, run without the procedure and with it.
AssertionBaselineWith procedure
Anti-surge margin ≥ 12 % on both trains−32.3 %+16.6 %pass
CMP-02 export flow ≥ 80 kNm³/h71.2 kNm³/h88.7 kNm³/hpass

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

IN THE PRODUCT

What the control room sees

The Djinious 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.
The Djinious 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.
The Djinious 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.
MORE CASES

Run this against oil & gas midstream you actually operate.

We will model your equipment, wire your tags and dry-run one of your procedures on the call.

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DjiniousControl Center

Supervise the plant, author the procedure, prove it on an isolated twin, execute under policy. One governed loop.

  1. Observe
  2. Author
  3. Prove
  4. Act

Every screenshot on this site is a capture of the running platform.