Project Reference · Condensate Processing · Stabilization Skid
Longfengshan Condensate Stabilization Project
The Longfengshan reference documents unstabilized condensate from metering separators and production separators entering a condensate stabilization skid. The documented process uses heat exchange followed by a stabilization tower with stripping and rectification sections to remove lighter components.
Feed Source
Metering / Production Separators
Process
Heat Exchange · Stripping · Rectification
Package
Condensate Stabilization Skid
Project Background
A real condensate stabilization reference tied to upstream separation.
The project source identifies the Northeast Bureau Longfengshan condensate stabilization unit and states that unstabilized condensate from metering separators and production separators enters the condensate stabilization skid for stabilization.
This page uses that reference to demonstrate the verified feed source and stabilization process logic. It does not publish non-public client specifications, commercial terms, project schedule, proprietary drawings or unverified operating results.
Feed Condensate Source
The documented feed comes from upstream metering and production separation.
The direct source names both metering separators and production separators as sources of unstabilized condensate feeding the stabilization skid. For a similar new project, the upstream separator conditions and condensate analysis should be confirmed rather than inferred from this case.
SOURCE A
Metering Separators
A directly documented upstream source of unstabilized condensate in the Longfengshan reference.
SOURCE B
Production Separators
A second directly documented upstream source feeding the stabilization skid.
Process Requirement
The verified objective is removal of lighter components to stabilize condensate.
The project source explicitly describes the use of rectification and stripping principles to remove light components from condensate. It does not provide a publishable standard RVP, throughput, product yield, temperature, pressure, tray count or reflux ratio.
Feed Analysis
For a new project, confirm condensate composition, light components, water/solids and corrosion-relevant constituents.
Operating Envelope
Confirm normal/min/max/design flow, pressure and temperature rather than reusing unknown case values.
Product Basis
Define stabilized-condensate acceptance criteria and downstream storage/transfer requirements.
Overhead / Off-Gas
Define vapor destination, pressure/interface requirements and any recovery, fuel-gas or flare connection.
Stabilization Skid Scope · Evidence Boundary
Keep the documented process equipment separate from broader package capability.
The source directly verifies a condensate stabilization skid, heat exchanger and stabilization tower with stripping and rectification sections. LINSON OIL's broader capabilities support piping, valves, instruments, electrical/control, skid assembly, FAT and delivery for similar packages, but those generic capabilities are not presented as confirmed original Longfengshan contract inclusions unless separately evidenced.
DIRECT PROJECT EVIDENCE
Condensate Stabilization Skid
The source explicitly states that unstabilized condensate enters the condensate stabilization skid.
DIRECT PROJECT EVIDENCE
Heat Exchanger
The source explicitly states that the condensate is heated by a heat exchanger before entering the stabilization tower.
DIRECT PROJECT EVIDENCE
Stripping Section
The stabilization tower is directly described as including a stripping section.
DIRECT PROJECT EVIDENCE
Rectification Section
The same stabilization tower is directly described as including a rectification section.
Heat Exchange / Stripping / Rectification Logic
A documented sequence from feed heating to tower stabilization.
The source states that condensate is heated in a heat exchanger and then enters a stabilization tower using the volatility difference between light and heavy components. The tower contains both stripping and rectification sections.
- 01 / FEED
Receive Unstabilized Condensate
The documented feed enters from metering and production separation.
- 02 / HEAT
Heat Exchange
The source directly states that condensate is heated by a heat exchanger before entering the stabilization tower.
- 03 / STRIP
Stripping
The stripping section contributes to removal of lighter components from the condensate.
- 04 / RECTIFY
Rectification / Product Handover
The rectification section is part of the tower arrangement; final stabilized-liquid and vapor interfaces are defined from the specific project basis.
Equipment Integration
A similar new package requires process, mechanical and control interfaces to be engineered together.
LINSON OIL's general capability includes pressure-vessel, piping, skid, electrical, instrumentation and control design, plus skid integration and valve/instrument/electrical/control-system integration. This section describes execution capability for similar projects rather than adding unverified items to the original Longfengshan scope.
Heat-Transfer Interface
Coordinate exchanger duty, process connections, heating/cooling utility and control requirements from the approved process basis.
Tower / Vessel Interface
Coordinate stabilization tower nozzles, internals interface, supports, access and inspection requirements.
Piping / Valve / Instrument
Define interconnecting process piping, valves, drains/vents, instruments and package battery limits.
Control / Safety Interface
Map pressure/temperature/level control, alarms/interlocks and relief interfaces to the approved control philosophy.
New-Project Interface Checklist
Feed tie-in
Source, flow/P/T, composition, upstream separator condition and piping battery limit.
Stabilized liquid
Product acceptance basis, storage/transfer pressure, sampling and downstream connection.
Overhead vapor
Recovery, compression, fuel-gas, flare or other destination plus pressure/control interface.
Utilities / controls
Heating/cooling, power, instrument air, signals, control-system and hazardous-area basis if specified.
Manufacturing / Inspection
Inspection follows the approved equipment and package scope.
For similar projects, LINSON OIL's quality resources support incoming material verification/traceability, welding control, dimensional inspection, applicable NDT, pressure/leak testing where required, complete-assembly inspection, instrument/electrical/control testing and FAT according to the project specification and ITP.
Material / Welding Control
Material certificates, traceability, welding procedure/welder control and fabrication records as applicable.
Dimensional / NDT
Dimensional inspection and applicable RT/UT/MT/PT or other specified NDT.
Pressure / Leak / Assembly
Pressure, leak/tightness and complete-assembly checks where required by equipment and project scope.
FAT / TPI / Records
FAT, customer/EPC/third-party witness and final quality records according to the approved ITP.
Delivery / Site Interface
Use the project as process evidence—not as a source for an invented delivery schedule.
The available project source does not publish the Longfengshan delivery period, installation duration or commissioning schedule. For similar new projects, delivery and field support are defined from the actual package size, shipment split, destination and contract scope.
Shipment / Lifting
Confirm module split, lifting, transport restraints and destination limits after design development.
Mechanical Tie-Ins
Define feed, stabilized condensate, overhead/off-gas, relief, drain and utility piping interfaces.
Electrical / Control
Define power, signals, local/package controls and plant-control-system interface.
Commissioning / Spares
Installation guidance, commissioning, spare parts and after-sales scope are contract-defined.
Project Evidence
What the Longfengshan reference directly proves.
Feed source
Unstabilized condensate from metering separators and production separators.
Process objective
Removal of light components using rectification and stripping principles.
Heat-exchange step
Condensate is heated by a heat exchanger before entering the stabilization tower.
Tower configuration
The stabilization tower is described as containing both stripping and rectification sections.
Not Generalized
No RVP, project throughput, tower tray count, reflux ratio, operating temperature/pressure, product yield or project schedule is published here as a standard LINSON OIL value.
Related Equipment
Equipment relevant to similar condensate-stabilization packages.
These are related procurement pages and are not presented as a complete original Longfengshan supply list.
Condensate Stabilization Unit
Core stabilization package for project-defined feed and product requirements.
Process Heat Exchanger
Heat-transfer equipment for project-defined condensate heating/cooling duty.
Gas-Liquid Separator
Separation equipment for project-defined upstream/downstream interfaces.
Custom Pressure Vessels
Project-defined columns, drums and pressure-retaining equipment.
Custom Process Skid
Integrated package supply where piping, valves, instruments and controls are included by scope.
Flare Knockout Drum
Relief/off-gas supporting equipment where the project battery limit includes a flare-system interface.
Similar Project RFQ
Send the condensate analysis and stabilization basis.
Share feed composition, flow and P/T range, upstream separator conditions, stabilized-product requirement, overhead/off-gas destination, utilities, P&ID, Data Sheets, Technical Specification and 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.