Hi Rolphil,
I like your optimism with the way you modify bits "ad hoc"...
I prefer to take a more scientific approach - if I can find the information and make it work.
re:
"I haven't worked on the blower yet, but I tried opening the blower valve all the way, and I lost steam pressure as it vents faster than it can draft at full open. It also likes to gurgle and pulse every time I adjust it." - Well, all I can suggest is initially yo halve the cross-sectional area of the blower nozzle, and re-try. But also check the effect of the blower when you only have about 30psi, when first developing steam pressure. (I assume the engine is pretty useless below that?) - or at minimum engine functioning pressure. The intention of a good blower is:
- The blower will recover a freshly watered boiler and freshly fuelled fire when the old fire has burned too far down and pressure has dropped to the minimum where the engine is effective, so the regulator has been closed... On a loco, the fireman would be told by the driver the minimum pressure needed for each rise of the track on the route, so the fireman could learn when to get get the fire fuelled, and boiler watered, and still have enough steam so as not to stall on the hill. It may also be the lowest pressure where the injector functions adequately.
- The blower should not be too big, so forcing the fire to generate too much steam for the safety at fully open, when the regulator is fully closed.
So hopefully, half the CSA of your blower nozzle will be half "blower power". While this is a simple step for the "top pressure (safety blowing off) check, it may mean the blower is inadequate for the low pressure function? But a second point to determine what the boiler needs..... Call it "nozzle B"- added to your starting point information - "nozzle "A".
Depending on how the testing goes, you can do a nozzle "C" at either half way between nozzle "A" and "B", or half CSA of nozzle "B". - Then try again. (lots of fun!).
I hope this gives some direction to your "development method".
You could of course resort to calculations, but I feel you are not that sort of guy?
But regards your Safety Valve mods.
I have "played-about" and used some graphical indications to tweak some crude safety valves to be more "pop"-like.
A simple valve is like the "Big switch-back" shapes, the better "pop-type" (called "soft-pop" by the designer) is the flatter, smoother shape. Owing to the bits I am modifying, I can't always get close to the ideal ratios of cross-sectional area at the critical points through the valve, but the closer I can get the better the hysteresis (difference between opening and closing pressure... less than 4% is very good, more than 10% is harder to live with). The diameter you have reduced increases the cross-sectional area for steam to pass at the second graph point, so making the hysteresis worse, but action "softer" - so less likely to prime... But it may be very poor at closing. What happens is that the dynamic pressure on the valve is different to the static pressure. It needs static pressure in the boiler to open the valve, but then the steam passing through (plus condensate as it expands, plus carry-over priming water!) causes a dynamic pressure that is higher, thus keeping the valve open as the pressure drops lower. You are right in thinking that valve outside diameter is critical, but you may have gone too far....? Just a few thou at a time may have been better...?
I look forward to hearing of your further experiences and testing of this boiler.
Incidentally, the 125psi may be for an air compressor that works up to 8Bar...? = 5 psi opening over 120psi? Safety valves on air receivers do not experience much dynamic pressure for "water" in the exiting air... so generally are simpler (no "pop" action). And as they have electric motors and pressure cut-offs fitted, they usually stop pumping so the safety valve never operates...
Please feel free to ask when you need to. I am more of a "has been under pressure" ex-spurt than a "knowledgeable" Expert... but willing to throw in some ideas.
K2