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Do distillation towers operated under vacuum require safety valves?

2018-12-09View Original

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As the title says. According to fire safety regulations, it seems unnecessary to install one, but there is a reboiler at the bottom of the tower. In the event of condensation at the top of the tower or an interruption in the reflux flow, or in case of a fire, could pressure build up? Overpressure protection should be installed, right? What do everyone do? I checked, and it seems that some have it while others don’t. Security is very strict these days; will there be problems if it’s not set up?
Reply #22018-12-09
For the abnormal situations you mentioned, it is safer to install a safety valve.
Reply #32018-12-10
It is not necessary to include it, but from a technical perspective, it is better to have it.
Reply #42018-12-10
It should be installed if there is a possibility of overpressure occurring during the production process and if that overpressure could cause damage; otherwise, it is not necessary to install it.
Reply #52018-12-11
I think a safety valve should be installed; the reboiler that provides the heat source is itself a pressure vessel; Secondly, during operation, there may be interruptions in the cooling water supply or failures of the vacuum pump; such situations can cause a sharp rise in pressure. Since distillation towers are usually designed with low pressures, this can easily lead to safety accidents.
Reply #62018-12-11
Safety considerations focus not only on normal operating conditions but also, to a greater extent, on abnormal operating conditions. If it exists, then it needs to be set up
Reply #72018-12-11
This statement is absolutely correct! !
Reply #82019-11-22
If it needs to be set, is the leakage rate calculated based on cooling water failures? In other words: is the discharge volume the maximum amount of steam that enters the condenser under normal operating conditions?
Reply #92019-11-23
It can be considered to be located at the highest point of the gas pipeline; sometimes, leakage inside the condenser is taken into account, as well as the excessive pressure resulting from the sudden vaporization of the cold medium. A burst disc will suffice; the possibility of overpressure is not high either. I don’t think overpressure is likely in other cases, as long as the gas pipes are all straight.

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