PV valves are the individual tank-mounted relief devices that open on overpressure or vacuum, separate from the mast riser breaker on the inert gas main, and they are usually the first thing checked when a cargo tank shows an unexplained pressure alarm.
The 0 models with the most complete data of 0 in PV Valves (Pressure/Vacuum). Every row links to full specifications, documents and service notes.
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An inert gas system has its own mast riser pressure/vacuum breaker, but that device only protects the common distribution main, not each individual tank once its branch valve is shut. PV valves sit directly on the tank dome or the venting header serving a small group of tanks, and they are the device that actually keeps a single tank inside its designed pressure envelope during loading, discharging, ballasting, or simple thermal expansion of the vapour space on a hot day. Where the mast riser breaker is a coarse, high-capacity safety…
An inert gas system has its own mast riser pressure/vacuum breaker, but that device only protects the common distribution main, not each individual tank once its branch valve is shut. PV valves sit directly on the tank dome or the venting header serving a small group of tanks, and they are the device that actually keeps a single tank inside its designed pressure envelope during loading, discharging, ballasting, or simple thermal expansion of the vapour space on a hot day. Where the mast riser breaker is a coarse, high-capacity safety net, the tank PV valve is a precision-set component whose cracking pressures directly limit how the cargo plan can be run.
A weighted or spring-loaded disc sits on a machined seat; rising tank pressure lifts it to vent vapour, and vacuum pulls a separate vacuum pallet open to draw in inert gas or air, preventing the tank from being sucked inward.
On larger tankers a small pilot valve senses pressure and triggers a much larger main valve to open fully once set point is reached, giving tight sealing at normal pressure but high flow capacity in an upset condition.
Where full free-flow venting is required, the vent outlet is shaped to discharge vapour as a high-velocity jet straight upward, dispersing flammable vapour away from the deck rather than letting it roll along the surface.
Corrosion-resistant mesh across the outlet stops a stray spark or flame from travelling back down into the tank, and is one of the parts most often found clogged or corroded away during inspection.
Set points follow the tank design pressure, commonly in the range of roughly +1400 mmWG for the positive side and around -350 mmWG for vacuum on a typical product or crude tanker, though the exact figures come from the ship's trim and stability and cargo system documentation rather than a fixed industry number. Sizing has to cover the worst-case simultaneous scenario: maximum loading rate plus the vapour generated by a sudden rise in ambient temperature, since undersizing a valve leaves the tank without adequate relief exactly when it is needed most.
| Fault | Consequence |
|---|---|
| Pallet seat corroded or coated in cargo residue | Valve sticks shut, tank overpressures during loading, or sticks open, wasting inert gas |
| Set pressure drifted low from spring fatigue | Nuisance lifting during normal operations, inert gas consumption rises |
| Flame screen blocked with salt or paint overspray | Reduced flow area, effective set pressure rises well above the nameplate value |
| Pilot sensing line pinched or iced in cold trades | Main valve fails to open on demand, tank left without relief |
Never isolate a PV valve for maintenance without confirming an alternative relief path is open on that tank; a blanked-off valve during tank cleaning has caused more than one crushed or overpressured tank top.
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