The brewery I am modeling has large percentage of energy consumption associated with the process load. From past posts I understand I need to write a thorough narrative explaining the standard practive baseline and the stategy for energy savings of process load for the Proposed Case.

We have the energy data of MBTUs/barrel from World Breweries Energy Benchmarking and MBTU/barrel calculated from another very similar brewery of the same company in another location. My questions are:

1. Can I use this MBTUs/barrel comparison to demonstrate the savings of process load of the Proposed Case from the Baselin Case for this project (by applying a percentage of process load to the total consummption)?
2. I am using Trane Trace for energy modeling. The process load added in the energy model is typically just a number under "Base Utilities". I am thinking using a total number for both baseline and proposed case based on MBUTs/barrel and the barrel production of this new brewary. Is that enough?
3. There are many chillers associated with only the process load . Should I model it in my energy model? (e.g. selecting chiller types, assign capacity and efficiency, etc) or just take them as a part of the lump sum number of process load?