Calculation of startup and shutdown costs for the facility
Thread Content
Cost calculation for shutdown and startup of a plant, for a standard hydrogenation plant. The supervisor notified that work must be halted, and there is no need to replace the air with nitrogen; work can resume once the supervisor gives another instruction. How is the cost of this process calculated, not including labor costs? ； The plant scale is calculated at 500,000 tons per year ；
What you’re saying is too general; it’s difficult to calculate.
First, a parking plan needs to be developed; only with such a plan can costs be estimated. Otherwise, it’s like building something in the air. Additionally, there is the issue of labor costs during the parking period
It’s not explained in detail; if the catalyst is replaced, there are more steps involved. Normal maintenance is straightforward