Pressure for pentane storage and the mode of gas-phase equilibrium
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I seek help from experts: What is an appropriate pressure level for storing pentane? Are there any relevant regulatory requirements? (The maximum temperature is 40°C.) The pentane in the storage tank is transported externally via a pump; is a vapor equilibrium line required? The user is too far away; returning to the gas phase is not feasible.
You can refer to the table in the HG20570 equipment design pressure selection guidelines, which outlines the design pressures for liquefied hydrocarbons and mixed liquefied petroleum gas stored at normal temperatures; as a reference value, the design pressure for pentane tanks should not exceed 0.79 MPa