"> Vapor Recovery/Return System - Equipment Database

Vapor Recovery/Return System

medium 2 models total

A vapor recovery/return system captures the hydrocarbon vapor a tanker's cargo tanks displace during loading and routes it back through a shore connection instead of releasing it to atmosphere, cutting emissions and product loss during the loading operation specifically, not during the voyage.

Read more — Vapor Recovery/Return System explained

What Sets This Type Apart

Ordinary tank venting through pressure/vacuum valves lets displaced vapor escape to atmosphere as cargo is loaded. A vapor recovery or vapor return system instead connects the ship's vapor manifold to shore piping so that vapor displaced by the incoming liquid cargo is pushed back to the terminal's recovery or flare system rather than vented on deck. It is specific to the loading evolution at terminals fitted for vapor balancing or vapor recovery; it does not replace the ship's normal P/V valves and mast risers, which remain the safety venting path when the vapor connection is not in use or fails.

Vapor recovery / return system
Deck-level vapor path on a tanker: each cargo tank's vapor space vents through a P/V valve into a common header running to the ship's manifold connection, then by hose to the shore vapor recovery unit.

Main Components

Vapor manifold and shore connection

A dedicated line and flange, separate from the liquid cargo manifold, sized to carry the vapor volume displaced at maximum loading rate without pressuring the tanks above their design limit.

Vapor collection header

Runs along the tank deck, tying each cargo tank's vapor space into the common line through isolation valves, so individual tanks can be included or excluded from the recovery circuit.

Pressure control and relief

High-velocity vents and P/V valves remain in the system as the fallback if the shore vapor line cannot take the full flow or the connection is broken; a pressure/vacuum breaker protects the collection header itself from over- or under-pressure.

Flame screens and detonation arrestors

Fitted in the vapor line to stop a flame front from propagating back into the cargo tanks if an ignition source reaches the shore-side vapor system.

Selection and Sizing

Sizing is driven by the loading rate the ship is designed for, since vapor displacement tracks liquid loading volume almost directly.

  • Maximum design loading rate per tank and in total, which sets the vapor line diameter and valve capacity needed.
  • Allowable tank pressure range, since the vapor return path must keep pace with displacement without pushing tank pressure toward the P/V valve's set point.
  • Cargo type and vapor characteristics; some cargoes carry vapor recovery requirements tied to their flash point or toxicity rather than pure convenience.
  • Compatibility of the ship's manifold connection standard with the terminals the vessel regularly calls at.

Regulations and Class

MARPOL Annex VI and regional port regulations increasingly require vapor emission control at terminals handling volatile cargoes, which drives the shore-side requirement for a compatible ship connection; class rules for the cargo system require the P/V valves and venting arrangement to remain fully functional and independently capable of protecting the tanks regardless of whether a vapor return connection is in use. Flame arrestors and detonation arrestors in the vapor path are subject to type approval and periodic inspection under the society's cargo system survey requirements.

Typical Faults

FaultCauseConsequence
Flame screen blockageFouling from polymerising cargo vapor or ice formation in cold conditionsRestricted vapor flow, rising tank pressure during loading, possible unplanned P/V valve lift
Isolation valve left shutTank not included in the vapor circuit at the pre-loading line-upThat tank vents locally instead of through the recovery line, undermining the terminal's emission commitment
Manifold connection mismatchShip and shore vapor connections use different standards or gasketsDelayed cargo operation or a connection made with an unsuitable adapter
Overpressure during loadingVapor return line undersized or restricted relative to actual loading rateTank pressure rises toward the P/V valve set point, forcing a reduced loading rate

What to Look for in a Supplier

  • Documentation of vapor line capacity against the ship's stated maximum loading rate, not a generic size match.
  • Flame and detonation arrestor type approval certificates specific to the cargo range the ship carries.
  • Manifold connection dimensions matched to the terminals in the vessel's trading pattern.
  • Clear maintenance and inspection intervals for flame screens, which foul faster than most crews expect.

Never treat the vapor return connection as a substitute for watching tank pressure during loading; if the shore side cannot keep pace, the ship's own P/V valves are still what stands between the tank and an overpressure, so the loading rate has to come down, not the vigilance.

1 manufacturers · 2 models

Wärtsilä

2
Alma (Wärtsilä) Alma Marine VRU
Alma Marine VRU
variable · Conditioned Air / Exhaust Air · absorption-based vapor recovery unit
Type
vapor_recovery
Method
absorption
Common Failures & Inspection Points
  • Absorption media saturation
  • Blower failure
  • Return line blockage
Service: Absorption-based VRU. Media replacement per schedule.
Spare Parts: Alma (Wärtsilä): Spare parts per manufacturer. Lead time: 3-8 weeks. Keep seals and valve inserts on board.
Strengths
  • Compact footprint suitable for retrofits on existing tankers
  • Low power consumption compared with compression‑type VRUs
  • Integrated control system from Wärtsilä simplifies operation and monitoring
  • Proven reliability of the Alma brand in harsh marine environments
  • Scheduled media replacement is straightforward, minimizing downtime
Weaknesses
  • Absorption media must be replaced regularly to avoid saturation loss
  • Performance limited for very high VOC loads or heavy‑hydrocarbon streams
  • Reliance on a blower; failure can halt recovery until repaired
  • Not ideal for cryogenic vapours (e.g., LNG) without additional equipment
  • Potential blockage in return line requires vigilant maintenance
Typical Vessels: Crude Oil TankerProduct TankerChemical Tanker
Decision Guide: Choose if the vessel must meet IMO D‑2 or regional vapor‑recovery regulations, operates with moderate hydrocarbon vapour loads, and values a low‑energy, compact solution. Avoid if the cargo includes high‑VOC or cryogenic gases, if maintenance windows are extremely limited, or if a compression‑type VRU is required for very high recovery rates.
Use Cases: Commonly installed on oil and product tankers to treat vent gas from cargo tanks during loading/unloading, integrated into the ship's cargo handling system to return recovered vapour to the tanks and reduce emissions. Also used on chemical tankers where specific hydrocarbon streams are within the absorption media’s capability.
Wartsila Vapor Recovery Unit
variable · Conditioned Air / Exhaust Air · oil‑free screw compressor
Type
vapor_recovery
Common Failures & Inspection Points
  • Compressor failure
  • Condenser fouling
  • Vapor return valve malfunction
  • Flame arrestor blockage
Service: Required in SECA/ECA zones. Annual compressor overhaul.
Spare Parts: Wartsila (Hamworthy): Spare parts per manufacturer. Lead time: 3-8 weeks. Keep seals and valve inserts on board.
Strengths
  • High vapor recovery efficiency (typically >95%)
  • Compact, integrated design suitable for limited deck space
  • Oil‑free compression reduces contamination risk
  • Built‑in condenser and flame arrestor provide complete system functionality
  • Proven track record on new builds and retrofits in emission control areas
Weaknesses
  • Higher initial capital cost compared with basic venting kits
  • Requires annual compressor overhaul and regular condenser cleaning
  • Performance can degrade if the condenser becomes fouled by oil mist
  • Flame arrestor blockage may occur if not inspected regularly
  • Limited maximum capacity for ultra‑large crude carriers
Typical Vessels: Oil product tankerChemical tankerLPG/LP gas carrier (product segment)Bulk liquid carrier
Decision Guide: Choose if: the vessel operates in SECA/ECA zones, regulatory compliance with IMO MARPOL Annex VI is required, and space on deck is limited. Avoid if: budget constraints dominate or the ship’s cargo turnover does not justify the higher recovery efficiency.
Use Cases: Installed on new‑build product tankers to meet upcoming emission regulations, or retrofitted onto existing vessels operating in high‑traffic emission control areas such as North Sea and US coastal zones. Used during loading/unloading cycles to capture volatile organic compounds and return them to cargo tanks.