Document 7313011

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Transcript Document 7313011

Pipeline systems
Monroe L. Weber-Shirk
School of Civil and
Environmental Engineering
Pipeline systems
 Pipe
networks
 contain
pipe loops or parallel
pipes
 can have multiple sources
and sinks
 multiple paths for water to get between any two points
 Manifolds
 single
and diffusers
source
 multiple sinks along a single pipe (the manifold)
Manifolds
 Examples
 sprinkler
irrigation system
 wastewater discharge (multiport diffuser)
 Design
objectives
 distribute
a given discharge uniformly through
multiple ports
 choose pipe size given constraints of head loss,
flow distribution, and cost
Multiport Diffuser
 Objectives
 Minimize
detrimental
effects of the discharge
on the environment
 Maximize initial dilution
 Meet regulatory
requirements
 Pollutants
 treated

wastewater
BOD, N, P, metals
 Cooling
water from
power plant
 Heat
 Sites
 Rivers,
Oceans
Lakes,
Multiport Diffuser
energy grade line
hydraulic grade line
z=0
?
Remember Venturi
Representation of EGL and HGL for
multiport diffuser. Does it make sense?
What happens to HGL across the ports?
Multiport Diffuser:
Flow Calculations
piezometric ____
head
We will derive equations in terms of __________
p
because pressure controls the port flow
+z
g
 Port flow

energy equation
based on ______
 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
In diffuser
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

The Problem
 Given
a desired discharge
 Calculate
the head (pressure) required
 Calculate the flow from each port
 Develop
a strategy to solve this problem
A Simple Solution
 Constant
pressure in the diffuser pipe
 Each port is like an orifice
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

Port Flow
z = 0 at water surface
V p2
Va2 p p
 za 

 zp 
 hL

2g 
2g
pa
H
p
z

piezometric head
p
riser
Va  V p
Hd 
2
a
V
0V 2
 Hp 
2g
Hd 
Vp2
2g
port
Vp
p
2g
 hL
Vr
 hL
Va
Vd
diffuser pipe
Control volume?
Riser Head Loss
hL  hentrance  hriser  helbow  hcontraction
V

Lr
V
hL  K en  f
 K el   Kc

Dr
 2g
2g
2
r
Vr Dr2  V p Dp2
continuity
4
D p 
V  V  
Dr 
4

 V2



L
D
r
p
p
hL   K en  f
 K el 
 Kc 
 D 

 2g
D
 r 
r


2
r
2
p
hc  Kc
2
p
V p2
2g
Vr2
hel  K el
2g
Vp
p
hriser
Lr Vr2
f
Dr 2g
hen  K en
Vr2
2g
Riser Head Loss Coefficient
Hd 
Vp2
2g

 1 


 hL
 V2




L
D
 K  f r  K  p   K  p
Hd
el
c
 en



 2g
D
D

 r 
r

4

Lr
Dp 
(riser loss coefficient)
K r  1  K en  f
 K el    Kc

Dr
Dr 
Note that the riser
coefficient is a function
Vp2 
Reynolds number.
H d  Kr  
of ________
2g 
D p2 2 gH d Port velocity (or flow) given
2 gH d
Qp 
piezometric head in diffuser
Vp 
4
K r and a riser loss coefficient
Kr
4
Orifice equation!
Head Loss across Port
expansion
Flow ____________
 Same equation applies
as derived previously
 The velocities
upstream and
downstream from the
port are determined
from continuity

separation
Vi
Pressure
_________
applied over
entire cross
section
Vi+1
1
Momentum
___________
transferred
over smaller
area
2
hLi =
(Vi - Vi + 1 )
2g
2
HGL in Diffuser across Port
Vi  Vi 1 
hL 
2g
2
EGL
i

HGL
H from
pressure
recovery


Vi
Vi+1
1
2
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
increase
(HGL) will __________
(proof coming up)
HGL in Diffuser across Port
Vi 2
Vi 21
Hi 
 H i 1 
 hL
2g
2g
energy equation using
________
definition of piezometric head
2
H expansion
i
2
i 1
Vi V
 H i 1  H i 

 hL
2g 2g
i
Vi  Vi 1 
2
hL 
i
2g
Vi 2 Vi 21 Vi  Vi 1 



2g 2g
2g
2
H expansion
H expansion
i
i
Vi 1 Vi  Vi 1  pressure increase across abrupt expansion

Vi  Vi 1
g
HGL in Diffuser across Port
H expansion
i
Vi 1 Vi  Vi 1 

g
How can we find velocity downstream
continuity
of port i? ___________
Qi  Qp  Qi 1
i
Vi  Vi1 
Qp
Vi 1  Vi 
Qp
H expansion 
i
i
Ad
Now we have the velocity
downstream of the next port
i
Ad
Vi 1Q p
gAd
i
And we can calculate the increase
in HGL across the port
HGL between Ports
parallel to EGL so H = E
between diffusers
 E = -hf and is due to friction loss (major
losses)
 HGL is
Re 
VD

f 
0.25
  
5.74 


log
0.9 
  3.7 D Re 
2
L V2
hf  f
D 2g
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

Multiport Diffuser: Solution
Given total discharge, pipe
4
diameter, port size...
D

Lr
 p 

   Kc
K

1

K

f

K
en
el
 Calculate the piezometric r

Dr
Dr 
head (measured from the
water surface) required to
2

D
2 gH d
give the necessary discharge
p
Qp 
in the first port
4
Kr
 loss coefficient for port
 head required to get
2
desired flow from port
K 4Q 

Hd 
p
2
p


2g D 
r
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
Qp 
i
D p2
2 gH d
4
Kr
Vi 1  Vi 
Qp
i
Ad
H expansion 
i
H pipe
i
Vi 1Q p
i
gAd
2
L Vi1
 f
D d 2g
H di 1  H di  H expansion i  H pipei
Multiport Diffuser: Solution
1
HGL
Qp 
i
4
D p2
2 gH d
4
Kr
L Vi 21
H pipe   f
Dd 2 g
i
decrease in pressure)
(_________
3
Vi 1Q p
H expansion 
gAd
i
i
increase in pressure)
(__________
Vi
H di
Known from previous step
2
Qp
Vi 1  Vi 
Ad
5 H d  H d  H expansion  H pipe
i
i 1
i
i
i
Multiport Diffuser: Solution
Calculate the total discharge from the ports
 Compare with design discharge
piezometric ____
head at first port to give design
 Adjust the _________
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.

Multiport Diffuser: Solution
SI units
EGL
HGL
1.2
1
(m)
total flow (Q)
2.5
port velocity (Vp)
3
port d iam eter (Dp)
0.230
port area (Ap)
0.04
nu m ber of ports
20
port flow (Qp)
0.13
term inal piezom etric head (H )
0.8
d istance betw een ports (L)
4
pipe rou ghness (e)
0
d iffu ser d iam eter (Dd )
1
1.4
0.8
0.6
0.4
0.2
0
0
20
40
60
distance along diffuser (m)
80
Multiport Diffuser: Solution
SI units
EGL
HGL
4.5
4
3.5
3
(m)
total flow (Q)
2.5
port velocity (Vp)
3
port d iam eter (Dp)
0.230
port area (Ap)
0.04
nu m ber of ports
20
port flow (Qp)
0.13
term inal piezom etric head (H )
1.2
d istance betw een ports (L)
4
pipe rou ghness (e)
0
d iffu ser d iam eter (Dd )
0.63
5
2.5
2
1.5
1
0.5
0
0
20
40
60
distance along diffuser (m)
80
Design Guidelines
~3 m/s to achieve
The port discharge velocity should be _______
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
fLd
D

d
to cancel when

3
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.

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
Less Uniform
remains the same.) ______________
 What happens to the uniformity of flow rates from
the ports as the size of the ports decreases?
______________
More Uniform
 If the goal is uniform flow distribution why not
Energy requirements
use very small ports? ____________________
 Which port will have the highest flow rate?
_____________
First or last!

Diffuser Homework
20 ports
Hometown WWTP
300 m
95 m
Wastewater Diffuser in Cayuga
Lake
Installation of Wastewater outfall diffuser in Cayuga Lake