Hi all.

I´m working in a project with VRV and want to specify a system with high COP values, and three issues surfaced....

1- Since there is no exact system specified in the ASHRAE 90.1 that matches the VRV system, I have been told to model the VRV system using the efficiencies in Table 6.8.1B. However these efficiencies are typically for full load operations, so it will not capture the advantage of the part load capability of the VRV systems. Therefore, the savings calculated will be typically conservative.

2- Can I compare a VRV with the effciency of a chilled water system?

3- Or do you think it is a good idea to at least use Table C-2 values from ASHRAE 189.1-2009, with higher COP values?

I want to include minimum COP values within the technical specifications. We are just indicating system size, capacity, etc, and no brands / models. Therefore, we want to make sure we get a system with high energy efficiency values. Any thoughts?