29
Monroe L. Weber-Shir k S chool of Civil and Environmental Engi neering Pipeline systems

04 Manifold Hydraulics

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Page 2: 04 Manifold Hydraulics

Pipeline systems

Pipe networks contain pipe loops or parallel

pipes can have multiple

and multiple paths for water to get between any two points

Manifolds and diffusers single source multiple sinks along a single pipe (the manifold)

sourcessinks

Page 3: 04 Manifold Hydraulics

Manifolds

Examples sprinkler irrigation system wastewater discharge (multiport diffuser)

Design objectives distribute a given discharge through

multiple ports choose pipe size given constraints of head loss,

flow distribution, and cost

uniformly

Page 4: 04 Manifold Hydraulics

Multiport Diffuser

Objectives Minimize detrimental

effects of the discharge on the environment

Maximize initial Meet regulatory

requirements

Pollutants treated wastewater

Cooling water from

power plant

Sites Rivers, Lakes,

Oceans

dilution

BOD, N, P, metals

Heat

Page 5: 04 Manifold Hydraulics

Multiport Diffuserenergy grade linehydraulic grade line

z = 0?

Representation of EGL and HGL for multiport diffuser. Does it make sense?What happens to HGL across the ports?

Remember Venturi

Page 6: 04 Manifold Hydraulics

Multiport Diffuser:Flow Calculations

We will derive equations in terms of __________ ____ because pressure controls the port flow

Port flow based on ______ equation head loss through port (possibly including a riser)

Piezometric head change (H) across port flow expansion

Piezometric head change ( H) between ports Darcy-Weisbach and Swamee-Jain

energy

In diffuser

piezometric headp zg

+

Page 7: 04 Manifold Hydraulics

Port types

Nozzle riser diffuser can be buried nozzle can give direction to discharge

Port cast in wall of diffuser pipe can’t be used if diffuser pipe is buried generally not recommended

Page 8: 04 Manifold Hydraulics

The Problem

Given a desired discharge Calculate the head (pressure) required Calculate the flow from each port

Develop a strategy to solve this problem

Page 9: 04 Manifold Hydraulics

A Simple Solution

Constant pressure in the diffuser pipe Each port is like an orifice

Page 10: 04 Manifold Hydraulics

Strategy

The diffuser has many ports. If we can develop equations describing pressures and flows at one port we can then apply it to all of the ports.

We need equations describing Flow from a port as a function of pressure in the

diffuser Head loss (and pressure drop) in the diffuser Flow in the diffuser

Page 11: 04 Manifold Hydraulics

Port Flow

H

p

z

Vr

riser

port

diffuser pipe Vd

Lp

pa

d hg

VH

g

VH 22

22

Lp

ppa

aa h

gV

zp

gVzp

22

22

Hd

Vp2

2ghL

piezometric head

z = 0 at water surface

aV

pV

p

0pa VV

Control volume?

Page 12: 04 Manifold Hydraulics

Riser Head Loss

gVKh r

elel 2

2

hriserf Lr

Dr

Vr2

2g

VrDr2 VpDp

2

Vr

2 Vp2 Dp

Dr

4

continuity Vp

hL hentrance hriser helbowhcontraction

hL Ken f Lr

Dr Kel

Vr

2

2g Kc

Vp2

2g

g

VK

D

DK

D

LfKh p

c

r

pel

r

renL

2

24

hc Kc

Vp2

2g

g

VKh renen

2

2

p

Page 13: 04 Manifold Hydraulics

Riser Head Loss Coefficient

Hd Kr

Vp2

2g

r

dp

K

gHV

2

(riser loss coefficient)Note that the riser coefficient is a function of ________ number.Port velocity (or flow)

given piezometric head in diffuser and a riser loss coefficient

r

dpp

K

gHDQ

2

4

2

Hd

Vp2

2ghL

g

VK

D

DK

D

LfKH p

c

r

pel

r

rend

21

24

Kr 1 Ken f Lr

Dr Kel

Dp

Dr

4

Kc

Reynolds

Orifice equation!

Page 14: 04 Manifold Hydraulics

Head Loss across Port

_________ applied over entire cross section

___________ transferred over smaller area

Flow ____________ Same equation applies

as derived previously The velocities

upstream and downstream from the port are determined from continuity

( )21

2i

i iL

V Vh

g+-=

1 2

separation

Vi Vi+1

Pressure Momentum

expansion

Page 15: 04 Manifold Hydraulics

HGL in Diffuser across Port

Head loss occurs between section 1 and section 2 some distance downstream (~5 times the diameter of the diffuser)

We will treat this head loss as if it all occurred immediately after the port

Although there is head loss past the port the pressure (HGL) will __________ (proof coming up)

hLi

Vi Vi1 2

2g

H from pressure recovery

EGL

HGL

1 2

Vi Vi+1

increase

Page 16: 04 Manifold Hydraulics

HGL in Diffuser across Port

ii Lii

ii hgV

gVHHH

22

21

2

1expansion

gVVVH iii 11

expansion i

________ equation using definition of piezometric head

pressure increase across abrupt expansion

gVV

gV

gVH iiii

222

21

21

2

expansioni

hLi

Vi Vi1 2

2g

Li

ii

i hgVH

gVH

22

21

1

2 energy

1 ii VV

Page 17: 04 Manifold Hydraulics

HGL in Diffuser across Port

Vi Vi1

Qpi

Ad

gVVVH iii

i

11expansion

d

pi

gAQV

H i

i

1expansion

Vi1 Vi

Qpi

Ad

continuityHow can we find velocity downstream of port i? ___________

1 ipi QQQi

Now we have the velocity downstream of the next portAnd we can calculate the increase in HGL across the port

Page 18: 04 Manifold Hydraulics

HGL between Ports

HGL is parallel to EGL so H = E between diffusers

E = -hf and is due to friction loss (major losses)

2

9.0Re

74.5

7.3log

25.0

D

f

Re

VD

hf f LD

V2

2g

Page 19: 04 Manifold Hydraulics

Multiport Diffuser: Solution The diffuser number, spacing, and jet velocity would be

determined in part by the mixing required in the ambient water (Environmental Fluid Mechanics)

Available head and total flow would be determined by the water source hydraulics

A criteria may also be established for uniformity of flow from the ports

Alternate design criteria may dictate different solution methods

Page 20: 04 Manifold Hydraulics

Multiport Diffuser: Solution Given total discharge, pipe

diameter, port size... Calculate the piezometric

head (measured from the water surface) required to give the necessary discharge in the first port loss coefficient for port head required to get desired

flow from port

r

dpp

K

gHDQ

2

4

2

Hd

Kr

2g4Qp

Dp2

2

Kr 1 Ken f Lr

Dr Kel

Dp

Dr

4

Kc

Page 21: 04 Manifold Hydraulics

Multiport Diffuser: Solution

Starting with the first port and proceeding to the last port ... Calculate the discharge from port i Calculate velocity change in

diffuser past port i Calculate the piezometric head

increase across port i Calculate the piezometric head

decrease between ports i and i+1 Calculate the piezometric head at

port i+1

d

pi

gA

QVH i

i

1expansion

Vi1 Vi

Qpi

Ad

Hpipe f L

Dd

Vi12

2g

iiii pipedd HHHH expansion1

r

dpp

K

gHDQ i

i

2

4

2

Page 22: 04 Manifold Hydraulics

Multiport Diffuser: Solution

Vi

r

dpp

K

gHDQ i

i

2

4

2

Vi1 Vi

Qpi

Ad

HGL1

5

g

V

D

LfH i

d

pipe2

21

3

2

4

(_________ in pressure)

(__________ in pressure)

idH

d

pi

gA

QVH i

i

1expansion

iiii pipedd HHHH expansion1

Known from previous step

increase

decrease

Page 23: 04 Manifold Hydraulics

Multiport Diffuser: Solution

Calculate the total discharge from the ports Compare with design discharge Adjust the _________ ____ at first port to give design

discharge (use goal seeking, solver, or trial and error on spreadsheet). Alternately, set velocity past last port = 0 by changing piezometric head at first port.

It may be necessary to adjust diffuser or port diameter. It will likely be possible to decrease the size of the

diffuser pipe as the flow decreases. This may also help increase the discharge uniformity of the ports.

piezometric head

Page 24: 04 Manifold Hydraulics

Multiport Diffuser: Solution

total flow (Q) 2.5port velocity (Vp) 3port diameter (Dp) 0.230port area (Ap) 0.04number of ports 20port flow (Qp) 0.13terminal piezometric head (H) 0.8distance between ports (L) 4pipe roughness () 0diffuser diameter (Dd) 1

0

0.2

0.4

0.6

0.8

1

1.2

1.4

0 20 40 60 80distance along diffuser (m)

(m)

EGLHGL

SI units

Page 25: 04 Manifold Hydraulics

Multiport Diffuser: Solution

00.5

11.5

22.5

33.5

44.5

5

0 20 40 60 80distance along diffuser (m)

(m)

EGLHGL

total flow (Q) 2.5port velocity (Vp) 3port diameter (Dp) 0.230port area (Ap) 0.04number of ports 20port flow (Qp) 0.13terminal piezometric head (H) 1.2distance between ports (L) 4pipe roughness () 0diffuser diameter (Dd) 0.63

SI units

Page 26: 04 Manifold Hydraulics

Design Guidelines The port discharge velocity should be _______ to achieve

good mixing with the ambient water. The sum of all port areas must be less than the diffuser pipe

area. The best area ratio (port area/diffuser area) is usually between 1/3 and 2/3.

The effects of pipe friction and pressure recovery will tend to cancel when Ld is the total length of the diffuser pipe and the friction factor, f, is

obtained by iteration since it is a function of the pipe diameter. If the diffuser area obtained using this method is less than 1.5 x

port area then this design criteria can not be used.

3d

dfLD

~3 m/s

Page 27: 04 Manifold Hydraulics

Multiport Diffuser:Thought Experiments

What happens to the uniformity of flow rates from the ports as the size of the diffuser pipe decreases? (Assume the pressure in the feeder pipe is varied to maintain constant flow while the port size remains the same.) ______________

What happens to the uniformity of flow rates from the ports as the size of the ports decreases? ______________

If the goal is uniform flow distribution why not use very small ports? ____________________

Which port will have the highest flow rate? _____________

First or last!

Energy requirements

More Uniform

Less Uniform

Page 28: 04 Manifold Hydraulics

Diffuser Homework

Hometown WWTP

300 m 95 m

20 ports

Page 29: 04 Manifold Hydraulics

Wastewater Diffuser in Cayuga Lake

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