Intake Manifold flow vs Head flow
Originally posted by Injuneer
I think you're just trying to confuse me....
I think you're just trying to confuse me....

-Mindgame
Originally posted by Injuneer
Trey:
I'm not sure what your point was.... are you agreeing, disagreeing, or just trying to confuse me
.?
The 2-3" pipes vs 1-4" pipe has been explained already. When comparing pipes of relatively similar size, a quickie method of comparing pressure drop, accounting for both cross-sectional area and wetted perimeter is to compare diameter to the 2.5 power, rather than squared. Using that approach puts 2-3's even closer to 1-4.
Who's common sense? The answer actually depends on how long the overall system is. If you had a very long system, and a length of 3" pipe in the center, assuming you used tapered transitions, rather than "butt" connections, the 4->3->4 would produce a greater flow for a given pressure drop, or a lower pressure drop for a given flow, than the same system utilizing all 3" pipe. Even without the tapered transitions, the 4-3-4 system will flow more for the same pressure loss.
In a very short system, the losses resulting from the "transitions" between diameters might be large enough to cause the "all 3" system to flow better. But in the length of the typical exhaust system, this isn't going to happen.
Huhh? what is the analogy to an exhaust system? You lost me.
If you merge the cars from two 3-lane roads into a single 3-lane road, the traffic on the single 3-lane road needs to move twice as fast as the traffic on the two 3-lane feeders, or there will be a huge backup. They will only need to travel 1.5 times as fast on the single 4-lane road. The faster the exhaust moves, the more pressure loss in the pipe. So the 2 3-lane into 1 4-lane exhaust pipe produces the least pressure loss.
I think you're just trying to confuse me....
Trey:
I'm not sure what your point was.... are you agreeing, disagreeing, or just trying to confuse me
.?The 2-3" pipes vs 1-4" pipe has been explained already. When comparing pipes of relatively similar size, a quickie method of comparing pressure drop, accounting for both cross-sectional area and wetted perimeter is to compare diameter to the 2.5 power, rather than squared. Using that approach puts 2-3's even closer to 1-4.
Who's common sense? The answer actually depends on how long the overall system is. If you had a very long system, and a length of 3" pipe in the center, assuming you used tapered transitions, rather than "butt" connections, the 4->3->4 would produce a greater flow for a given pressure drop, or a lower pressure drop for a given flow, than the same system utilizing all 3" pipe. Even without the tapered transitions, the 4-3-4 system will flow more for the same pressure loss.
In a very short system, the losses resulting from the "transitions" between diameters might be large enough to cause the "all 3" system to flow better. But in the length of the typical exhaust system, this isn't going to happen.
Huhh? what is the analogy to an exhaust system? You lost me.
If you merge the cars from two 3-lane roads into a single 3-lane road, the traffic on the single 3-lane road needs to move twice as fast as the traffic on the two 3-lane feeders, or there will be a huge backup. They will only need to travel 1.5 times as fast on the single 4-lane road. The faster the exhaust moves, the more pressure loss in the pipe. So the 2 3-lane into 1 4-lane exhaust pipe produces the least pressure loss.
I think you're just trying to confuse me....

and you basically agreed with me agreeing to you
And yes, the 4--->3--->4 would be a smooth transisiton, not a "butt" - i'm sure thre a bazillion variables we could include
so 4-------------->3--->4------------> will more than likely have more flow than
3 all the way acorss (but then there are issues with how the 3'' meets the 4'' and stuff.
and the highway was in agreement again with "duh think about it for half a second"
2 three inch collectors meeting a 3 inch catback vs 2 three inch collectors meeting a 4'' catback
my basic agreement point was "think about it for a second"
but guess it wasn't all that clear

Let me summerize-
I agree fred
Last edited by treyZ28; Jun 26, 2003 at 03:44 PM.
Originally posted by Mindgame
Tis the nature of confused people to confuse those around them.... this could become a real problem. And Albert Einstein is likely rolling in his grave 13.88 times a day.
-Mindgame
Tis the nature of confused people to confuse those around them.... this could become a real problem. And Albert Einstein is likely rolling in his grave 13.88 times a day.

-Mindgame
"Men who borrow their opinions can never repay their debts."---George Savile, 1633-1695
alright, enough picking on Trey here.
On the manifold topic, there is easily alot of power to be found in LT1's through the intake IMHO. I would easily take another 20cfm and longer runners on a LT1 vs another 20cfm, both would be even better. The TQ gain would be worth it more than the HP gain, but the additonal TQ you would really feel.
Bret
On the manifold topic, there is easily alot of power to be found in LT1's through the intake IMHO. I would easily take another 20cfm and longer runners on a LT1 vs another 20cfm, both would be even better. The TQ gain would be worth it more than the HP gain, but the additonal TQ you would really feel.
Bret
Originally posted by OldSStroker
Yep, flow varies by the square root of the pressure drop ratio. BTW, that's 117.5 isn't it? FWIW why was 28 " H2O selected as the de facto standard for comparing port flow?
Yep, flow varies by the square root of the pressure drop ratio. BTW, that's 117.5 isn't it? FWIW why was 28 " H2O selected as the de facto standard for comparing port flow?

I have no idea where the standard of 28" H20 comes from, but it's damn close to 1 PSI so I imagine that has something to do with it. Either that, or the first flowbench designer had a broken-off yardstick sitting around.
Isn't the LTX manifold's short runners the tuning problem for rpm below 7k+?
Why would you want to slow exhaust down with larger pipes? Doesn't that mean that the pressure would rise per Bernoulli? My take is that to keep exhaust flow somewhat steady, the cross-section of the system should steadily decrease as the flow temp and therfore volume decreases.
You did ask for opinions.
Originally posted by Eric Bryant
It's not that I want to slow down the exhaust gases; it's that they're naturally going to loose velocity as they cool, and therefore they're going to require a larger cross-sectional area. At least that's the way I understand it; hopefully someone can correct me if I'm wrong.
It's not that I want to slow down the exhaust gases; it's that they're naturally going to loose velocity as they cool, and therefore they're going to require a larger cross-sectional area. At least that's the way I understand it; hopefully someone can correct me if I'm wrong.
I don't think Bernoulli is relavent to this.... isn't that the theory that tells you the pressure perpendicular to flow direction is reduced as velocity increases.... not a "pressure drop" issue?
I always go back to George's car.... 1,125HP, Hooker LT's into a 3" Y-pipe into a 4" Mufflex cat-back, with a single 4" pipe out of the exhaust. But George likes the "stock" look, so he cuts the little tiny tip off the 30th SS's original SLP 2OTL exhaust and welds it to the end of the 4" pipe out of the muffler. Looks stock. Still make good HP. But it also pushed the gas velocity way up, as demonstrated here.
From what you said Trey, it seemed like you read it completely backwards. A 3" pipe is going to provide more resistance than a 4" pipe, so even if a 3" coupler in the midst somewhere , the rest of the exaust at least is free flowing.
What I think Fred was getting at though, is if we are using a Hooker LT example, you have two 3" collectors going into a hopefully dual 3" to 4" Y pipe hooked up to your 4" exaust.
What I think Fred was getting at though, is if we are using a Hooker LT example, you have two 3" collectors going into a hopefully dual 3" to 4" Y pipe hooked up to your 4" exaust.
Originally posted by Dr.Mudge
From what you said Trey, it seemed like you read it completely backwards. A 3" pipe is going to provide more resistance than a 4" pipe, so even if a 3" coupler in the midst somewhere , the rest of the exaust at least is free flowing.
What I think Fred was getting at though, is if we are using a Hooker LT example, you have two 3" collectors going into a hopefully dual 3" to 4" Y pipe hooked up to your 4" exaust.
From what you said Trey, it seemed like you read it completely backwards. A 3" pipe is going to provide more resistance than a 4" pipe, so even if a 3" coupler in the midst somewhere , the rest of the exaust at least is free flowing.
What I think Fred was getting at though, is if we are using a Hooker LT example, you have two 3" collectors going into a hopefully dual 3" to 4" Y pipe hooked up to your 4" exaust.
I just re-read what i wrote-
I thought 4-3-4 > 3-3-3 but for some reason i wrote will NOT flow as well
now i see where all the confusion is coming from (and jokes at my expense
) I re-read it twice quickly but i guess i read what i thought i wrote over again, not the actual words.I was sitting here trying to figure out why everyone was disagreeing. I just couldn't picture the 3-3-3 flowing as well as a 4-3-4
I REALLY need to be more careful and I feel rather stupid right about now...
my appologies
Last edited by treyZ28; Jun 27, 2003 at 12:05 PM.
Originally posted by Gripenfelter
Is there a way of measuring velcocity of air after it goes through the cylinder head and into the chamber? I don't mean cfm. Maybe Swirl Velocity or Swirl RPM??
Is there a way of measuring velcocity of air after it goes through the cylinder head and into the chamber? I don't mean cfm. Maybe Swirl Velocity or Swirl RPM??
Bret
Originally posted by OldSStroker
Yep, flow varies by the square root of the pressure drop ratio. BTW, that's 117.5 isn't it? FWIW why was 28 " H2O selected as the de facto standard for comparing port flow?
Yep, flow varies by the square root of the pressure drop ratio. BTW, that's 117.5 isn't it? FWIW why was 28 " H2O selected as the de facto standard for comparing port flow?

Originally posted by Mindgame
"Only two things are infinite, the universe and human stupidity, and I'm not sure about the former." - Albert Einstein
-Mindgame
"Only two things are infinite, the universe and human stupidity, and I'm not sure about the former." - Albert Einstein

-Mindgame
Originally posted by arnie
My understanding gives credit for this std. (28") to S. Yunick. The reasoning was that using this std. to compare head port flow, would result in a more accurate comparo to actual/usable gains experienced on a dyno.
My understanding gives credit for this std. (28") to S. Yunick. The reasoning was that using this std. to compare head port flow, would result in a more accurate comparo to actual/usable gains experienced on a dyno.
Also, 28 in H2O is just about 1 psi, which is near what a max. performance engine pulls around hp peak.
Thread
Thread Starter
Forum
Replies
Last Post
chevroletfreak
LT1 Based Engine Tech
202
Jul 4, 2005 05:00 PM



