Hi friends,
This query is just for educational purpose. Suppose a natural gas processing plant consisting of sweetening(amine), dehydration(JT) and sulfur recovery(Claus) units are designed for a turndown capacity of 40% feed gas. During the course of gas extraction, the pressure and flowrate of the raw gas gradually decreases and at some point reaches the design turndown value. what should be the changes and troubleshooting to be done for the plant if the gas feed rate is below the design turndown?
Regards