Aerial view of the refinery process units connected by pipe racks

The refinery

Full conversion, maximum middle distillates

One 150,000 bpsd crude and vacuum train feeds a two-stage hydrocracker, a delayed coker, three hydrotreaters and a gasoline block. The residue is converted, so the refinery makes no fuel oil.

Concept visualisation
View of the coke store, hot tanks and hydrogen plants with the delayed coker behind
Concept visualisationCoker, hydrogen and sulphur

Configuration

A proven recipe for medium-sour Gulf crude

The configuration combines distillation, hydrocracking, delayed coking, hydrotreating, hydrogen production and sulphur recovery: the established route to maximise Euro 5 diesel and jet fuel from this crude family.

Units are sized for an Oman-anchored crude diet of about 33.5 °API and 1.5 wt% sulphur, with flexibility from 30 to 40 °API at full rate; a heavier Gulf diet runs at reduced rate. The design targets a Nelson complexity index of about 9.5.

Four hot intermediate tanks on the parcel let the train ride through a hydrocracker or coker outage, and major turnarounds follow a four-year cycle.

Process units

Unit list and planning capacities

Process units and planning capacities
UnitCapacity
Crude distillation unit (CDU)150,000 bpsd
Vacuum distillation unit (VDU)75,000 bpsd
Two-stage hydrocracker52,500 bpsd
Delayed coker33,000⁠–⁠35,000 bpsd
Diesel hydrotreater47,500 bpsd
Kerosene hydrotreater22,500 bpsd
Naphtha hydrotreater32,500 bpsd
Continuous catalytic reformer (CCR)15,000 bpsd
Isomerisation unit7,500 bpsd
Hydrogen plants (steam methane reforming)2 × 80 MMscfd
Sulphur recovery (Claus) with tail-gas treatment3 × 130 t/d
Gas plant and LPG recovery, amine regeneration, sour-water stripping, flare-gas recovery and wastewater treatmentIntegrated

Planning capacities from the project basis. A licensor and LP study in 2027 will confirm unit sizes, yields and balances on current crude assays.

The plot, pipe racks and utility connections reserve space and tie-ins for a second train.

Products

What the refinery makes

Saleable liquids are about 94.4% of the crude volume, and diesel and jet fuel make up about two thirds of the output.

Saleable products at full rate

Thousand barrels per day (kbpd)

  • Diesel, 10 ppm sulphur68.6
  • Jet A-127.3
  • Gasoline20.7
  • Naphtha18.0
  • LPG7.0

Total saleable liquids141.6 kbpd

The refinery also makes about 1,473 t/d of fuel-grade petroleum coke and 246 t/d of sulphur at full rate, both exported in bulk through the port.

Planning yields for the design crude, to be confirmed by the licensor and LP study. The hydrocracker can swing about 5% of output by weight between jet fuel and diesel.

Specifications

Products to the specifications buyers name

  • 01

    Diesel

    A single 10 ppm sulphur, EN 590-type grade that meets Euro 5 markets and over-complies where 50 ppm or more is allowed.

  • 02

    Jet fuel

    Jet A-1 to international specification, with batch certification and segregated handling.

  • 03

    Gasoline

    A 92 RON pool with 95 RON capability, benzene at or below 1% by volume and 10 ppm sulphur.

  • 04

    Naphtha

    Full-range naphtha for export to petrochemical crackers.

  • 05

    LPG

    Propane and butane, kept segregated, for regional import terminals.

  • 06

    Coke and sulphur

    Fuel-grade petroleum coke and formed sulphur in covered storage, exported in bulk.

Inside the process core

Built around the main pipe racks

A street-level view along a plant road: the main rack with air coolers, heaters and drums, and pipe bridges over the road.

Street-level view along a refinery road under pipe bridges, with process units on both sides
Concept visualisationProcess core at street level

Utilities

Self-supplied power, steam, hydrogen and water

  • 01

    Cogeneration

    Two 60 MW-class gas turbines with heat-recovery steam generators and a steam turbine, about 165 MW gross, supply the plant’s average load of about 115 MW and 125 t/h of process steam.

  • 02

    Grid connection

    Two 132 kV circuits to the free-zone grid station provide standby supply; a non-firm surplus of about 25 MW can be offered to the grid.

  • 03

    Hydrogen

    Two 80 MMscfd steam methane reformers supply the hydrocracker and hydrotreaters; one can hold about 65% of rate if the other trips.

  • 04

    Sulphur recovery

    Three 130 t/d Claus trains with tail-gas treatment recover about 246 t/d of sulphur at full rate, with a spare train at the design crude.

  • 05

    Water

    A 25,000 m³/d seawater reverse-osmosis plant supplies all process and domestic water; the refinery draws no groundwater.

  • 06

    Natural gas

    About 2.45 million m³ a day at phase 1, for hydrogen production and cogeneration, to be competed for under the national gas allocation process.

Enquiries

Talk to the development team

For investor, lender, partner and media enquiries, write to us. Public documents are on the Downloads page.