All experience will be related to all details of application and flow conditions, installation, pipeline layout, and of course all details of type, construction, accuracy and quality, including details on geometry, sealing and frequency of operation, and flow variation. No waterhammer or gulping presumed, as this is a sign of wrongly selected layout and dimensioning.
Failure by startup is more than 95% failure to pick right type by all criteria, wrongly mounted or adjusted, damaged products (wrongly produced or damaged, scratched sealings mostly).
All that said and 'in order' for the type you have selected, your failure rate could be 'almost zero'. If not so critical operation: keep one or two complete in reserve, recommended with mounted and adjusted extra equipment (limit switches, counterweights, damping devices etc, if any). The most exposed position will be likely to fail first, or by unfortunate circumstances one damaged or failing by startup, say guesstimate one in 10 to 100. Expected lifetime: guesstimate five to twentyfive years.
If critical operation: select non slam soft closing nozzle check valve instead. (There exists a range of constructions from your type, up to nozzle check that generally will perform better, but not implying that the choice you mention is not satisfactorily)