The best way to answer is in my opinion to recommend the best possible installation: two valves (one checkvalve and one emergency shutdown valve) that can work independently of each other, without the one or the other disturbing the function of the second.
You need:
a) To avoid slamming by pressure peaks:
A checkvalve that closes when delta p is zero, or more correctly spring operated closing, marginally before delta p is zero. Best choice: non-slam soft closing nozzle check valve. Or, second choice, but depending on size and pressure class: disc (not swing) check valve with spring. Both valvetypes from top quality manufacturors.
Another choice might be tilting disc with counterweight, with hydraulic piston damping.
This third alternative will require exact flow data (all possible situations!) at all times to dimension the solution. Same is valid for the two others, but with larger limits for accuracy.
b) An emergency shutdown valve with regulation (setting) possibillities for the closing down time stroke, preferably if large size: fast for (say) first 70-80%, slower for rest.
Dimensioning is necessary both for size and closing time (both for one and two-step closing) to prevent hammerblow pressurepeaks backpressure.
The whole piping construction need to be considered for correct dimensioning and placement of alll components.
Direct answer to your questions:
1. Yes, but only if dimensioned correct, mounted correct and best with spring assistance, and only under certain hydraulic conditions (flow amount) and limits. In practice it will more likely have a very good chance of closing with a 'bang'.
You will often see swing check valves damaged with pin and hinge or sealing problems. This is caused by one or more of following causes: bad/weak construction, wrong dimensioning or mounting (placement) causing sudden closing creating shockwaves and repeating hammerblow closing (or 'gulping'-opening closing rapidly ande repeatedly- if too large for flow or throtteled flow).
2. Yes, but see point 1.
Good luck!
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