Aggieengineerrmb,
the pressure in a vacuum system is the result of an equilibrium between the leakage (intrusions from outside and/or through the valve seat) and the pumping system capability to remove the flow resulting from leakage itself.
Soo it seems correct to define fixed and repeatable test parameters, and also to distinguish between external tightness (regarding leakage through packing, body flanges, etc. or so-called fugitive emissions) and seat tightness.
For example, when testing for fugitive emissions with "hood technique" (as per Shell MESC SPE 77/307 Specification and/or ASME CODE: see below), we can easily reach in a few hours and maintain a pressure level below 0.1 mbara (= 10-4 bara) within valves up to 24", even with our laboratory vacuum pumps. This is called a "medium vacuum grade" and it covers almost all the usual industrial vacuum applications (higher vacuum grades are used in Laboratories and special applications).
The allowable leaks are expressed in the same terms as other fugitive emissions tests (see Threads on this subject within this Forum and Shell MESC SPE 77/312), i.e. in terms of mbar*l/s (or equivalent flow rate units) measured by a mass spectrometer.
I would suggest to take a look at ASME BOILER & PRESSURE VESSEL CODE, Section V "Nondestructive Examination", Article 10 "Leak Testing", Appendix IX "Hood Technique".
The simplest way to measure seat tightness, instead, may be to establish a certain vacuum grade on a side of the closed valve, a certain pressure on the other, exclude the vacuum pump and then see how much time is needed for pressure in the vacuum side to increase; that is to measure the vacuum seat leakage in terms of "pressure recovery rate".
For example: you may say that your valve passes the test if it maintains a 100 mbara vacuum against atmospheric pressure (or more) for at least 10 min.
For more severe service conditions and requirements, the above mentioned "hood technique" may be adapted for seat leakage testing too.
Hope this helps, 'NGL