products

Safety Devices

Dilock Dilock It is a safety device that quickly interrupts the gas flow shun the controlled pressure reach the intervention set valve due to any malfunction. Special suitable for natural gas, L.P.G. end non corrosive gas.
PF EVRM NA PF EVRM NA PF EVRM NA/6NA type valve is a manual reset safety valve that is normally open
PF EVRM NC PF EVRM NC PF EVRM NC/6NC type valve is a manual reset safety valve that is normally closed
PF VLM PF VLM VLM type valve is a slow opening single-stage solenoid valve normally closed
PF VMM PF VMM VMM type valve is a combination of two solenoid valves in an only compact and versatile valve housing
PF VRM PF VRM VMM type valve is a fast opening single-stage solenoid valve, normally closed (open when energized)
HBC 975 HBC 975 This is a safety device (SAV) which quickly intercepts gas flow when the pressure it is monitoring reaches a pre-set limit due to any anomaly in the system, or when required by the operator at installation point or from remote point.
PVS 782 PVS 782 PVS type slam shut valves are pilot-operated relief valves in which the opening and the closing of the main plug is controlled by a pilot device
PVS 803 PVS 803 PVS type slam shut valves are pilot-operated relief valves in which the opening and the closing of the main plug is controlled by a pilot device
SBC 782 SBC 782 This is a safety device (SAV) which quickly intercepts gas flow when the pressure it is monitoring reaches a pre-set limit due to any anomaly in the system, or when required by the operator at installation point or from remote point.
SCN SCN The SCN is a compact safety device (SAV) which quickly intercepts gas flow
VS/AM 65 VS/AM 65 The VS/AM 65 relief valve is a safety device (SBV) which vents gas when the system pressure exceeds the set value due to temporary events such as expansion due to rise in gas temperature or downstream pressure shocks caused by sudden changes of flow rate etc.
VS/AM 58 VS/AM 58 The VS/AM 58 relief valve is a safety device (SBV) which vents gas when the system pressure exceeds the set value due to temporary events such as expansion due to rise in gas temperature or downstream pressure shocks caused by sudden changes of flow rate etc.

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