Project Reference · Congo (Brazzaville) · Associated Gas Recovery
Congo Associated Gas / NGL / LNG Project
The documented Congo oilfield reference covers a phased associated-gas recovery and utilization development. Direct project evidence includes inlet metering/compression, drying, light-hydrocarbon recovery and product loading in Phase I, followed by expanded associated-gas recovery and natural-gas liquefaction in later phases.
Development
Phase I · II · III
Core Route
Recovery · Drying · NGL / LNG
Evidence Rule
Phase-Specific Data Only
Project Background
A multi-phase project built around recovery and use of oilfield associated gas.
The project source records an associated-gas recovery and utilization development in Congo (Brazzaville), implemented through Phase I, Phase II and Phase III. Supporting source material also states that the associated-gas recovery/utilization system was applied across all three phases.
This page keeps the documented phase capacities, products and process units strictly attached to the phase in which they appear. They are evidence of a real project reference, not standard LINSON OIL performance values.
Associated Gas Source
The project starts with an oilfield associated-gas stream and a defined utilization route.
For a similar project, feed composition, flow range, pressure/temperature, liquids/solids, H2S/CO2 and other contaminants must be confirmed before selecting compression, dehydration, hydrocarbon recovery or liquefaction equipment.
New-Project Feed Checklist
Gas composition
Full gas analysis and hydrocarbon composition sufficient for process selection.
Flow / P / T
Normal/min/max/design flow, inlet pressure/temperature and expected operating variation.
Contaminants / liquids
Water/moisture, free liquid, solids, H2S/CO2 and other treatment constraints where relevant.
Utilization objective
NGL/light-hydrocarbon recovery, LNG, fuel/power use, dry-gas export or another customer-defined route.
Phase Development Logic
Three phases, with different documented capacity and product scopes.
Capacities below are retained only because the source ties them to a specific phase. They must not be reused as standard package sizes or general LINSON OIL capacity claims.
| Phase | Documented Capacity | Documented Scope / Products |
|---|---|---|
| Phase I | 100.0 × 104 Nm³/d skid-mounted light-hydrocarbon recovery unit | Inlet metering/compression, drying, light-hydrocarbon recovery and product loading; supporting fire protection, water supply/drainage, power distribution and automation are also listed. Remaining dry gas is documented for power generation, self-use and venting. |
| Phase II | 200.0 × 104 Nm³/d associated-gas recovery + 100 × 104 Nm³/d natural-gas liquefaction | Documented products include propane, butane, stabilized light hydrocarbon and LNG. Dry gas is documented for power generation and LNG production. |
| Phase III | 100 × 104 Nm³/d associated-gas recovery + 100 × 104 Nm³/d natural-gas liquefaction | The source confirms continued associated-gas recovery and natural-gas liquefaction. It does not separately publish a Phase III product list in the cited case text. |
Documented Process Route
Inlet handling → drying → hydrocarbon recovery → product / LNG interfaces.
Phase I directly documents inlet metering/compression, drying, light-hydrocarbon recovery and product loading. Later phases add associated-gas recovery and natural-gas liquefaction capacity. The exact detailed process scheme, technology selection and equipment count remain project-specific.
- 01 / INLET
Metering / Compression
Directly documented in the Phase I process-unit list as the plant inlet handling step.
- 02 / DRY
Drying
Directly documented before light-hydrocarbon recovery in the Phase I plant route.
- 03 / RECOVER
Light-Hydrocarbon / Associated-Gas Recovery
Directly documented across the phased development; specific technology and recovery performance are not generalized.
- 04 / PRODUCT
Product Loading / LNG Interface
Phase I lists product loading; Phase II and III directly include natural-gas liquefaction capacity.
NGL / LNG / Dry-Gas Interfaces
Keep every product claim attached to the documented phase.
The Phase II case text directly names propane, butane, stabilized light hydrocarbon and LNG as products. It also states that dry gas is used for power generation and LNG production. Phase I separately states that remaining dry gas is used for power generation, self-use and venting.
Project Evidence Only
No NGL recovery rate, propane/butane yield, LNG yield, dry-gas composition, product purity, power consumption or economic return is stated as a standard or guaranteed result.
Utilities & Supporting Systems
Phase I source evidence includes plant supporting facilities—not only process skids.
The Phase I source directly lists fire protection, water supply/drainage, power supply/distribution and automation among the supporting facilities. The detailed equipment inside those systems is not inferred beyond the source.
Fire Protection
Directly listed as a Phase I supporting facility.
Water Supply / Drainage
Directly listed as part of the overall Phase I plant support scope.
Power Distribution
Directly documented among Phase I supporting facilities.
Automation
Directly documented as a supporting system; exact control architecture is not published here.
Manufacturing / FAT / Delivery
Similar project packages are executed against approved project documents and interfaces.
LINSON OIL's general capabilities support skid integration, material verification/traceability, applicable NDT, pressure/leak testing, complete-assembly inspection, instrument/electrical/control-system testing, FAT, export delivery and commissioning support. These are execution capabilities for similar projects and are not presented as a complete original Congo contract scope.
Engineering Clarification
Process Data, P&ID, Data Sheets, Equipment List, battery limits and applicable customer specifications.
Fabrication / Assembly
Project-defined vessel, piping, skid and package fabrication/assembly according to approved documents.
Inspection / FAT
Project-specific ITP, inspection/testing, customer/EPC/TPI witness and FAT as required.
Delivery / Site Interface
Packing, shipment split, transport, installation guidance, commissioning and after-sales boundaries by contract.
Project Evidence
What the Congo reference directly demonstrates.
Multi-phase deployment
The associated-gas recovery/utilization system is documented as applied in Phase I, Phase II and Phase III.
Phase I route
Inlet metering/compression, drying, light-hydrocarbon recovery and product loading, plus listed plant supporting facilities.
Phase II products
Propane, butane, stabilized light hydrocarbon and LNG are directly named in the source.
Later-phase LNG development
Phase II and Phase III both directly include natural-gas liquefaction capacity.
Phase capacities and products on this page are project-reference data only. They are not standard package ratings, guaranteed yields or universal LINSON OIL process performance.
Related Equipment
Equipment relevant to similar associated-gas recovery projects.
These are related procurement pages, not a complete original Congo project equipment list.
Associated Gas / NGL Recovery Unit
Recovery package for project-defined associated-gas composition and product objectives.
LNG Process Package
Natural-gas liquefaction package for project-defined feed and product basis.
Molecular Sieve Gas Dehydration Unit
Deep-dehydration route where selected by the project process basis.
Metering & Separation Skid
Project-defined inlet separation/metering package where applicable.
Gas-Liquid Separator
Gas/liquid separation equipment for inlet and process interfaces.
Custom Process Skid
Integrated equipment, piping, valve, instrument and control package by defined scope.
Similar Project RFQ
Send the gas composition, utilization objective and package boundary.
Share gas composition, flow and P/T range, contaminants, required NGL/LNG/dry-gas route, product basis, utilities, P&ID, Process Data, Equipment List, Technical Specification and project battery limits.
Detailed datasheets, drawings and project-specific technical documents are prepared after the operating conditions, scope of supply and commercial basis have been sufficiently clarified.