Hi Andrew,
I have only recently found this thread on your musings about injectors and applaud your inquisitive approach. It might already be known, but the only way you will really understand is to question things and work it out.
Way back you asked about the reason for a particular divergent angle on the steam cone. The answer is to be found in the simple truth:
"Accelerating fluid flow is easy, Decelerating fluid flow is damned difficult."
I have spent a working life in fluid dynamics finding that one out.
More specifically, in a conical diffuser once you reach a certain cone angle you will get flow separation – the boundary layer start to detach at some point downstream of the throat. This is precisely the same effect that causes a wing to stall at too steep an incidence. Initially you will get instability (buffeting) followed by complete BL detachment (stall). Obviously, in a cone of fixed angle you don't have the option of pushing the stick forward to get out of it. What you can do is keep the cone angle below about 10 – 12 degree included angle. Less than this angle and you will get a reasonably controlled (and hence efficient) reduction in flow velocity, turning the velocity energy back into pressure energy. There are charts published of loss coefficients Vs. geometry which show the detail of this effect.
I quite liked your explanation of why a steam nozzle must be convergent – divergent to extend the choking point. You are actually using Bernoulli's theorem to drop the exit static pressure at the throat, hence increasing the p1/p2 ratio which extends the sub-sonic flow regime. Not my specialism, but I hope this provides an alternative way of looking at it.
I have recently been looking at draughting, which is another application of the jet pump (and another area that everybody knows everything about because Kank and Snart said so in 1834). Anyway, one of the more reliable papers indicated that for good cavitation performance the area for the entrained fluid inlet was critical, which translates to radial gap between steam cone and mixing cone, plus axial standoff between same. This makes sense because the lowest pressure area is exactly there. You are trying to entrain water into a jet of steam moving at silly velocity and if you drop the static pressure below vapour pressure, cavitation (and hence loss of performance) will follow. This also explains why lifting injectors or hot water injectors are a *** to design because these areas will be critical.
By the way, I think you need to uplift your design water flow. You have not allowed for cylinder condensation which is likely to put up the water demand by another 50% or so, even allowing for steam jacketed cylinders. See the paper by Bill Hall "Measuring Steam Engine Performance"
Keep up the good work and the analytical approach. I copped out on injector building, there is a unit by Terry Baxter's old firm (He of "Injector Man" fame in another place) which is the vicar's knickers. Works beautifully and is encased in a lost wax casting which is a dead ringer for a Gresham & Craven vertical injector as used on tractions.
Best Wishes,
Martin