Operating specifications. 3.2.1. The non-return valve shall be so designed as to withstand a pressure of 1.5 times the working pressure (MPa) without leakage and deformation.
Operating specifications. 7.1 Gas must comply with Gas specifications Gas Delivered by the Shipper to the Operator at an Inlet Point or Delivered to the Shipper by the Operator at an Outlet Point must comply with the Gas specifications set out in Item 1 of Schedule 3.
Operating specifications. 7.2.1. The PRD (pressure triggered) of Class 0, shall be so designed to operate at temperatures as specified in Annex 5O.
Operating specifications. 4.2.1. The pressure relief valve and pressure relief device in Class 0 shall be so designed as to withstand a pressure of 1.5 times the working pressure (MPa) with the outlet closed off.
Operating specifications. 5.2.1. The excess flow valve, if it is not integrated in the tank, shall be so designed as to withstand a pressure of 1.5 times the working pressure (MPa).
Operating specifications. 2.2.1. The CNG automatic valve shall be so designed as to withstand a pressure of 1.5 times the working pressure (MPa) without leakage and deformation.
Operating specifications. 2.2.1. The LNG automatic valve shall be so designed as to withstand a pressure of 1.5 times the working pressure (MPa) without leakage or deformation (see Annex 5A).
Operating specifications. 3.2.1. The LNG check valve shall be so designed as to withstand a pressure of 1.5 times the working pressure (MPa) without leakage and deformation at cryogenic temperature.
Operating specifications. 4.2.1. The LNG pressure relief valve in Class 5 shall be so designed as to withstand a pressure of 1.5 times the working pressure (MPa) at cryogenic temperature with the outlet closed off.
Operating specifications. 5.2.1. The LNG excess flow valve, if it is not mounted inside the tank, shall be so designed as to withstand a pressure of 1.5 times the working pressure (MPa) at cryogenic temperature.
