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This post was last edited by lihaiyong826 on 2018-2-7 at 10:53. According to SYT0511.1-2010, there are 5 levels for the opening pressure of breathing valves, with the maximum value being 1765 Pa. Of course, manufacturers can customize the exhaust pressure of breathing valves according to actual needs, but it will not exceed 50 kPa in any case. In this sense, a breathing valve can also be considered a safety pressure relief valve, only with a lower set pressure. At the same time, according to those who conduct Hazop analyses, breathing valves are considered process valves, and their opening and closing fall within the scope of normal process operations; just as adjusting the degree of opening of control valves is not regarded as a safety measure. Safety valves are different; they serve as a protective measure. When a safety valve activates, it indicates that there is an abnormality in the process, and urgent release is necessary. (I personally disagree.) In such a situation, where there is a atmospheric-pressure storage tank that requires nitrogen sealing, and a self-acting nitrogen supply valve as well as a nitrogen release valve are installed, the nitrogen release valve is not capable of handling the required discharge volume during a fire scenario. Then, should this atmospheric-pressure storage tank be equipped with a vent valve or a safety valve? It is often thought that it is unnecessary to install safety valves on atmospheric pressure tanks; if pressure is relieved using a breathing valve (single-acting valve), I believe this is also feasible from a safety perspective. What are everyone’s opinions?
In a situation like the one you described, the nitrogen-sealing indicator’s nitrogen supply valve and nitrogen release valve function as breath valves in the process, while the single exhaust valve acts as a safety valve for emergency release. Don’t focus on the literal name; consider the purpose and use.
A breathing valve controls pressure within a certain range, while a safety valve prevents overpressure. Both functions are needed.
It’s simple – let the software calculate the parameters for the various valve options you mentioned. Do you think the calculations for the nitrogen seal valve, nitrogen release valve, and breather valve are the same? Also, are the discharge volume calculations for the one-way valve and the safety valve the same? Such a comparison is enough to convince people, isn’t it?
A breather valve can be considered a process valve. To ensure ultimate pressure relief, a pressure relief manhole can be considered.
At the same time, according to those who conduct Hazop analyses, breathing valves are considered process valves, and their opening and closing fall within the scope of normal process operations; just as adjusting the degree of opening of control valves is not regarded as a safety measure. Safety valves are different; they serve as a protective measure. When a safety valve activates, it indicates that there is an abnormality in the process, and urgent release is necessary. There should be no problem with this. Atmospheric pressure storage tanks are equipped with self-acting control valves to supply nitrogen as a safety measure. The nitrogen relief valve is installed to prevent the storage tank from overpressuring, and it also serves as a safety measure. Why mention safety valves? Is it to prevent excessive pressure in the tank in case the material inside catches fire and cannot be released? Why do atmospheric-pressure storage tanks experience overpressure? Material properties? So now, many storage tanks in those tank farms are equipped only with breather valves, or rather with nitrogen filling + nitrogen release systems.
A breather valve is a control measure used to regulate the pressure inside the tank; it is not a safety measure
I see that some atmospheric pressure tanks these days are equipped both with a nitrogen seal and a vent valve
Atmospheric and low-pressure storage tanks are essential equipment in petrochemical plants. At normal and low pressures, storage tanks often experience gas expansion or contraction within them due to changes in the liquid level inside the tank or fluctuations in external temperatures. As a result, the pressure of the gas phase in the tank also fluctuates. Such fluctuations in gas pressure can easily lead to overpressure or vacuum conditions in the tank; in severe cases, this may cause the tank to burst under overpressure or to collapse under low pressure. To prevent the storage tank from reaching unstable conditions such as overpressure or underpressure, process design typically involves installing a vent valve on the top of the tank in order to maintain pressure balance. This helps to protect the tank from damage in cases of overpressure or vacuum, ensures its safety, and reduces the volatilization and loss of materials within the tank, thereby contributing to both safety and environmental protection.
A breather valve is an important accessory for ensuring the safety of oil tanks; it is installed on the top of the tank and consists of a pressure valve and a vacuum valve. Its function is, under normal circumstances, to maintain the integrity of the oil tank and to reduce oil evaporation losses to a certain extent. And when necessary, it can automatically regulate ventilation to balance the pressure inside and outside the oil tank, thereby ensuring its safety. A safety valve is a valve used for safety protection; its operating element remains in a closed state under external forces. When the pressure of the medium inside a device or pipeline rises above the specified value, the valve opens automatically, allowing the medium to be released outside the system in order to prevent the pressure from exceeding that specified level. Safety valves belong to the category of automatic valves and are primarily used in boilers, pressure vessels, and pipelines to ensure that pressure does not exceed specified levels, thereby playing a crucial role in protecting both human safety and the proper operation of equipment