Classification issue of methanol-rich equipment
Thread Content
I have been working on ammonia synthesis equipment recently, and I came across tanks filled with methanol-rich medium. The basic details are as follows: 1. Operating pressure of 2.2 MPa, operating temperature of -47.35°C, and volume of 2.5 m3. There is no gas phase space in the operating state. 2. Rich methanol contains 0.067% H2S (mole percentage), 1.02% CO2 (mole percentage), a small amount of water, and the remainder is methanol. 3. The boiling point of methanol is higher than 60°C. So does this device need to be planned according to capacity? Seek solutions and discussions.
It’s hard to ensure that there is no gas phase space in ordinary containers, right? However, since this container is relatively small, if there is no level gauge, it should be taken into account that it may not be fully filled during operation, making it impossible to press down on it.
Thank you; it’s actually a filter, and there shouldn’t be any gas phase