I have an some API 12D tanks (10,000 barrels). According to API 12D, the design pressure of the tank is 3 oz., and the allowable emergency relieving pressure is 4.5 oz.
When it comes to vacuum, API 12D is not so clear. It states that the design vacuum is 0.5 oz., but unlike the pressure...
I am designing a NGL processing facility and need some help with the vent system design. Since the facility is essentially liquid packed, purge gas is not available to keep a positive pressure on the vent system to prevent air ingress. The only time the vent system will see a flow is in the...
I am looking for help designing a gas sweetening plant. We're just in the conceptual stage right now. The flow rate is about 15 MMSCFD of gas with 20 ppm H2S and 4% CO2. I'm familiar with amine units from a process flow standpoint having worked at a gas plant that had one specifically for CO2...
