I too would love to see some standardized detector placement criteria. A lot of individual judgement is required. Strong opinions likely exist among the critics of your plan.
I doubt that the power plant is using sour gas for fuel. Obtain process stream data that identifies the streams that likely contain hydrogen sulfide in excess of about 20 ppm. Identify other potential sources such as sumps, drains, dikes etc. where heavy gas could collect due to other orgainic processes.
Most people use point H2S gas detectors placed within about 0.5 meter above the grade within less than 15 meters of the likely sources. Fifteen foot might be better. Apply more in the predominent downwind direction than upwind. Many suppliers are proven for this. Frequent testing is required, quarterly minimum and monthly checking common. These detectors can drift. Different sensors are better for wet or dry areas. New technologies include open path detection using tunable laser diode analytical techniques. Few suppliers are ready for the industry.
If a serious hazard exists require the employees to wear personal detectors and to carry evac masks.
Codes and standards include the following:
API RP 55 Oil and Gas Operations,
ISA 92.0.01, 92.0.02, 92.2.21,
NACE MRO103
EPA Method 11 for H2S in fuel and Performance Spec 7 for H2S in the CEMS monitoring
OSHA limits
29 CFR 1910.1000
Texas Railroad Commission Rule 3.36