Phase I / II / III Completed

Associated Gas Recovery & LNG Liquefaction System

Congo (Brazzaville) -- Jiarou Oilfield

Jiarou Oilfield gas processing facility, Congo Brazzaville

PRIMARY -- Jiarou Oilfield Field Installation

LNG road tanker loading at the facility

SECONDARY -- Product Output Operations

Project Facts

Client & Location
Intl. Oil Operator / Jiarou Oilfield, Congo
Total Gas Capacity
300×10⁴ Nm³/d gas recovery
LNG Capacity
200×10⁴ Nm³/d LNG liquefaction
Products
LNG, Propane, Butane, Stable Light HC, Dry Gas
Manufactured By
LINSON OIL, Dongying, China

The Jiarou Oilfield -- Context

The Jiarou Oilfield is an oil-producing field in the Republic of Congo (Congo Brazzaville), operated by an international oil company. Like many African oilfields, Jiarou's primary product is crude oil -- but its associated natural gas, produced alongside the crude at the wellhead, represented a significant resource that was not being captured.

Without gas recovery infrastructure, associated gas from oil production is either vented to atmosphere or flared. Venting and flaring waste a recoverable energy resource, generate greenhouse gas emissions, and -- in an increasing number of jurisdictions -- attract regulatory penalties and ESG liability for the operating company.

The Jiarou project was conceived to convert this flared associated gas into marketable products: LNG for road tanker distribution to domestic and regional markets, LPG (propane and butane) for domestic cooking and industrial use, and stable light hydrocarbons for blending or export. The project was structured in three phases, scaling capacity as product markets developed and infrastructure was established.

Map showing project location in Republic of Congo

The Engineering Challenge

What Made This Project Technically and Logistically Demanding

Remote Location Without Established Infrastructure

The Jiarou Oilfield is located in a remote area with limited local manufacturing, engineering, and maintenance capability. All process equipment had to be designed, fabricated, and tested in China, then exported and transported to the site. The equipment had to be designed for reliable field operation with the available local operations team.

Multi-Stage Gas Processing Integration

Converting raw associated gas to LNG and NGL requires a precise sequence of steps. A failure in dehydration affects the LNG cold box; incorrect NGL fractionation affects product value. The process design must anticipate interdependencies and build in margins that accommodate fluctuating oilfield production over the field's producing life.

Multi-Phase Project Execution Continuity

The structured phases required LINSON OIL to maintain engineering and design continuity across time. Each phase built on installed capacity, interfacing with existing equipment, designed to avoid disruption to ongoing operations. Phase II and III equipment had to interface seamlessly with Phase I infrastructure already in service.

The Solution -- Three Phases

Phase I

NGL Recovery and Dry Gas to Power

Capacity: 100×10⁴ Nm³/d associated gas recovery

Associated gas from the Jiarou Oilfield separators enters the Phase I processing system at wellhead pressure. The gas passes through an inlet separation and conditioning stage -- removing entrained liquid, regulating pressure, and removing water to the dehydration specification.

The conditioned gas then enters the NGL extraction stage, where heavier hydrocarbon components (C3+: propane, butane, and stable light hydrocarbons) are separated from the leaner gas stream by a refrigeration-based condensation process.

The separated NGL is stabilised and dispatched as liquid product. The lean residue gas is delivered to the oilfield's power generation facility, eliminating the need for diesel fuel import for power generation.

Products from Phase I

  • Natural gas liquids (propane, butane, stable light hydrocarbons)
  • Dry lean gas (fuel gas to oilfield power generation)
Phase I system NGL recovery and power generation equipment
Phase II system expansion and LNG liquefaction modules
Phase II

Expanded Gas Recovery + LNG Liquefaction

Capacity: 200×10⁴ Nm³/d gas recovery + 100×10⁴ Nm³/d LNG liquefaction

Phase II doubled the gas recovery capacity to 200×10⁴ Nm³/d -- accommodating increased oilfield production and previously un-captured gas from additional well connections. A dedicated LNG liquefaction train was added alongside the expanded gas recovery system.

After NGL extraction, the residue gas enters the LNG liquefaction cold box. The cold box uses a refrigeration cycle to progressively cool the gas to approximately -162°C, at which point the methane condenses to liquid form (LNG). The LNG is collected in insulated storage tanks and loaded into cryogenic road tankers for distribution.

The addition of LNG significantly increased the value recovered from the associated gas, making it the primary route to gas monetisation for remote oilfields without pipeline infrastructure.

Products from Phase II (Additional)

  • LNG (100×10⁴ Nm³/d production capacity; road tanker distribution)
  • Propane (domestic and industrial LPG market)
  • Butane (LPG blending and domestic fuel)
  • Stable light hydrocarbons (condensate blending or export)
Phase III

Additional LNG Capacity

Capacity: 100×10⁴ Nm³/d gas recovery + 100×10⁴ Nm³/d LNG liquefaction

Phase III added a further 100×10⁴ Nm³/d of gas recovery capacity and a second 100×10⁴ Nm³/d LNG liquefaction train -- bringing the total system to 300×10⁴ Nm³/d of gas recovery and 200×10⁴ Nm³/d of LNG liquefaction capacity across the three phases.

The Phase III equipment interfaces with both Phase I and Phase II infrastructure, sharing common inlet separation, utility systems, and product dispatch facilities where possible. The LNG production from Phase III trains combined with Phase II gives the Jiarou Oilfield a significant LNG output volume.

Combined system showing full facility at maximum capacity
Phase Gas Recovery LNG Capacity Additional Products
Phase I 100×10⁴ Nm³/d -- NGL; dry gas to power
Phase II 200×10⁴ Nm³/d 100×10⁴ Nm³/d Propane, Butane, Stable light HC, LNG
Phase III 100×10⁴ Nm³/d 100×10⁴ Nm³/d Additional LNG train
Total 300×10⁴ Nm³/d 200×10⁴ Nm³/d Full product slate

Delivery Scope -- What LINSON OIL Provided

Engineering

  • Process design from inlet gas composition and product specification
  • Equipment sizing: all vessels, heat exchangers, compressors, columns, and skids
  • P&ID development for each process stage
  • Heat and material balance
  • Export packaging specification

Fabrication (All In-House)

  • All pressure vessels (GB 150 / A2 license): separator vessels, adsorber vessels, column vessels, heat exchangers
  • All pipe spools (GC2 piping license): ASME B31.3 compliant; RT-examined
  • All structural skid frames
  • PLC control panels (each processing module)

Testing

  • Factory acceptance testing per module before export
  • Instrument loop check on all modules
  • Control system function test per module
  • Pressure tests (all vessels and piping)

Export and International Delivery

  • Export crating per ISPM-15 standard for all wooden packaging
  • Equipment preservation for sea freight transit time and tropical storage conditions
  • Freight coordination to Congolese port of entry
  • Full export documentation: commercial invoice, packing list, bill of lading, certificate of origin, inspection certificates
  • Import documentation support for Congo Brazzaville customs clearance

Commissioning Support

  • LINSON OIL commissioning engineers at site for initial system start-up
  • Process performance verification against design basis
  • Operations team training on equipment operation and routine maintenance

Why This Project Matters As A Reference

Shipping documentation showing Congo Brazzaville destination

International Engineering Delivery

This is not a domestic Chinese project cited as an international reference. The equipment was designed in China, fabricated in Dongying, exported internationally, and commissioned at a remote oilfield in Central Africa. Every stage of the international delivery chain -- export documentation, sea freight, in-country customs clearance, and field commissioning -- was managed and executed. The project is internationally deliverable because it has been internationally delivered.

Multi-Phase Project Continuity

The three-phase structure required LINSON OIL to maintain engineering continuity and technical accountability across multiple project phases delivered over an extended period. An equipment supplier who delivers Phase I and disappears leaves the client without continuity for Phase II and III. LINSON OIL delivered all three phases -- maintaining the engineering design continuity, equipment interface compatibility, and commissioning knowledge that multi-phase projects require.

Full Gas Processing Train -- Not Component Supply

LINSON OIL designed and fabricated the complete associated gas recovery and LNG liquefaction system -- not individual components sourced from separate suppliers. The process design, the equipment fabrication, the control systems, and the commissioning were all within LINSON OIL's single scope. For the client, this meant one technical point of accountability for the system's performance -- not multiple vendors pointing at each other when a problem arose.

Scale of Delivery

200×10⁴ Nm³/d of LNG liquefaction capacity across two trains is not a pilot-scale system. This is a commercially operating LNG production facility supplying product to road tanker distribution networks. The engineering, fabrication, and commissioning demands of a system at this scale are substantially more rigorous than those of a smaller demonstration or evaluation installation.

LINSON OIL export logistics and international project commissioning

Planning an Associated Gas Recovery or LNG Project -- in Africa or Elsewhere?

The Jiarou project demonstrates LINSON OIL's capability to design, fabricate, export, and commission a complete associated gas recovery and LNG liquefaction system at a remote international oilfield -- from process brief to operating facility. If your project involves associated gas monetisation, NGL recovery, or small-to-mid-scale LNG in any geography, send us your gas volume and product target. Our engineers will respond with a preliminary system concept and reference within 1-2 business days.

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