Very well sir.....
Please feel free to post your principles.
You didn't take the time to read Bernoulli so please post the research you have done.
For the record....I said Restricts.
Given the head pressure in the bowl, the size of the jet, and the pressure in the venturi......What do you think Restricts flow?
Bowl pressure should be atmospheric or there abouts.
Venturi pressure will be dependant on RPM but at WOT the venturi shape and size is fixed.
Now....put a bigger orifice in the mix......and what have you got?
Enrichment.
You didn't change the venturi size or the atmosperic pressure acting on the fuel in the bowl......
Wheres the restriction?
You're jumping all over the place here.
Your initial statement:
You will no doubt know that the main Jet acts as a restriction only at Wide Open Throttle.
Then this:
A certain diameter straw will in fact flow only so much liquid. eventually you reach a point at which no more fluid can flow regardless of the suction.
However the diameter of the straw (or jet) is in relation to the suction.
So at wide open throttle....the diameter of the jet (or straw) AND the suction determine the flow.
True, but not exclusive. At 50% throttle, the diameter of the main jet AND the suction play a major part in determining fuel flow. Same for 75%.
Rereading through all of this, I wonder if the initial statement you meant to make was:
You will no doubt know that the main Jet acts as the only restriction at Wide Open Throttle.
That would make sense, and render the previous several pages a semantic mistake.
Semantics aside, I did do some calculations for fun.
- Assuming a BSFC of 0.45, each main jet sees 59.15 cc/min of fuel flow at the horsepower peak.
- A #100 main jet has a diameter of 1.00mm (according to an old TT post)
- With a cross-sectional area of pi()*(0.05cm)^2 I estimate the free-stream fluid velocity to be 125.52 cm/s, or 1.25m/s
- I found all sorts of values for the kinematic viscosity of gasoline, from 0.46 to 0.88, all at 15.6 degrees C.
- With a v of 0.88 and density at 15.5 C of 700kg/m^3, the dynamic viscosity is u=6.16x10^-4
- The hydraulic diameter of the pipe is 0.001 m
This makes the Reynolds number 1420, which is well within the laminar flow range for the restricting section of the main jet, neglecting entrance and exit conditions, etc.
But at this point I'm assuming this whole thing was a semantic mistake.