NC0063029_Performance Summary_19950726

NPDES DOCUMENT SCANNING COVER SHEET
NPDES Permit:
NC0063029
Camp Lejeune WWTP
Document Type:
Permit Issuance
Wasteload Allocation
Authorization to Construct (AtC)
Permit Modification
Complete File - Historical
Engineering Alternatives (EAA)
Performance Summary)
Instream Assessment (67b)
Speculative Limits
Environmental Assessment (EA)
Document Date:
July 26, 1995
Thies do eumeat ins printed oa reu.ine paper - ignore aay
coateat on the re'ernae Decide

LEJCORM.XLS
CAMP LEJEUNE OUTFALL: CORMIX2 RUNS, JULY 1995
Jim Blose 7-26-95
Runs use alternative ambient conditions.
All runs: Diffuser=36 port, staged. Port diam=4 in (.101 m). Diffuser length=107m. Discharge depth=.6m
Discharge=15MGD
ambient wind salinty I edge of dilution salinity plume width I distance distance
run name velocity speed depth deficit I NFR at NFR def at NFR at NFR I to 20:1 to 50:1
(m/s) (m/s) (m) (ppt) I (m) (ppt) (m) I (m) (m)
defunhom 0.075 2 1.83 20 9.15 28:1 0.705 136 4.5 -600
defunh3 0.05 1 1.83 20 9.15 23:1 0.871 165 <9.15 > 1000 (46:1 at 1000)
defunh2 0.025 2 1.83 20 313 34:1 0.581 158** 49.96 > 1000 (45:1 at 1000)
Iej07 0.025 0 1.83 20 313 34:1 0.581 158** 49.96 > 1000 (43.5:1 at 1000)
defunh5 0.075 2 1.83 12 9.15 28:1 0.423 136 4.5 -600
I008* 0.075 2 1.53 20 7.65 25:1 0.814 141 <7.65 -750
Iej09 0.075 2 2.13 20 10.65 32:1 0.623 132 <10.65 -406
" discharge depth= .5m
"' plume width at point of 20:1 dilution
Page 1

COMPUTER MODELING ANALYSIS
OF
PLANT OUTFALL
CAMP LEJEUNE, NORTH CAROLINA
MAY, 1995
REVISED JUNE, 1995

M
COMPUTER MODELING ANALYSIS
OF
PLANT OUTFALL
NEW RIVER BASIN
MARINE CORPS BASE
CAMP LEJEUNE, NORTH CAROLINA
CONSTRUCTION CONTRACT NO. N62470-94-B-4124
FY97 MCON PROJECT P-975
.6 PHASE II
Mgt
IM
Fill
RR
MI
WI
PIP
MAY, 1995
REVISED DUNE, 1995
DAVIS & FLOYD, INC.
6. GREENWOOD, SOUTH CAROLINA

GREENWOOD, SOUTH CAROLINA
TABLE OF CONTENTS
PAGE
INTRODUCTION 1
OUTFALL LINE HYDRAULICS 1-2
RIVER VELOCITY 2
INPUT DATA 3
�' DEFINITIONS 3-4
SIMULATIONS 5
pm SUMMARY 6
RECOMMENDATIONS 6
�' TABLE 1 7
WI
MR
RIVER STUDY
rm
LOCATION MAPS
GEOMETRIC DIAGRAMS
m,
OUTFALL AND DIFFUSER DETAILS
RUN DFUN23
RUN DFUN24
RUN DFUN25
RUN DFUN26
ow
RUN DFUN27
RUN DFUN28
wi, HYDRAULIC ANALYSES
OU'FFALL DIFFUSER SYSTEM
APPENDIXES
XI

CAMP LEJEUNE WASTEWATER TREATMENT PLANT
,., OUTFALL DIFFUSER SYSTEM
INTRODUCTION:
A 15 mgd advanced wastewater treatment is planned for Camp Lejeune. The treated effluent
will discharge to the New River. The discharge is approximately 1,600 feet offshore, just north
of Frenchs Creek. The New River is a small estuary that supports marine organisms. Sampling
by the Environmental Quality Analysis Section, ENV Compliance/Monitoring Branch of the
''M Environmental Management Department from 1992 to 1994.,showed considerable salinity
variation. However, salinity concentrations generally fell in the 20 ppt range. Discharge from
the proposed wastewater treatment is specified as a freshwater "pollutant". A study using the
software program "The Cornell Mixing Zone Expert system (CORMIX) was made to evaluate
1.' the potential impact the freshwater discharge would have on the New River in the vicinity of
Frenchs Creek.
The New River is a relatively shallow estuary with a depth of approximately 1.83 meters and a
relatively low river velocity at the point of discharge. There appears to be very little tidal
influence in the river.
OUTFALL LINE HYDRAULICS:
mat
Min
expected to occur during peaking events. Consequently, the outfall system must be designed to
handle a hydraulic flow of 30 mgd. On -site soil analyses indicate that large treatment plant
structures must be placed to a given depth to avoid the need for supporting piles. The soil
structure is not capable of supporting a net increase in soil pressure. Constructing the units to
greater depths, the heavier soils removed are replaced with the lighter concrete structures,
The proposed wastewater treatment plant is designed to treat a maximum flow of 15 mgd, an
average flow of 7.5 mgd and a minimum flow of 5 mgd. Hydraulic flows of 30 mgd are

Ing
Pzol
resulting in lower bearing loads on the underlying soils. Utilizing the construction method
eliminates the need for costly supporting piles.
Structural analyses of the units were made, and it was determined that a water surface elevation
of 17.6 (msl) in the final plant effluent structure was required to meet the soil bearing loads.
Pipe size, diffuser port size and the number of diffuser ports were hydraulically analyzed to
determine the optimum design. Port diameters of 3.5 inches, 3.75 inches, and 4 inches were
modeled. The calculated data is included in Appendix X. The table below is a compilation of
the data presented in Appendix X.
PORT DIAMETER
m
FIXED GRADE
Elevation
m3/s
FLOW
(mgd)
(inch)
0.101
(4)
17.6
1.39
(31.8)
0.095
(3.75)
17.6
1.26
(28.9)
0.0889
(3.5)
17.6
1.13
(25.9)
,ou, The calculations indicate that a 54 inch diameter diffuser, with 36 ports, and 4 inch diameter
ports would meet the hydraulic requirements for a flow of 30 mgd.
1.+ RIVER VELOCITY:
w*+ Prior to initiating the CORMIX2 program, a river study was made to determine the velocity of
the New River in the area of the proposed diffuser. The velocity at the time of the field
investigation averaged about 0.15 meters per second (m/s). The field investigation indicated an
unidirectional ebb flow during high and low tide. Field datum collected during the river velocity
study are shown in the section entitled, River Study.

CORMLX2 INPUT DATA:
The program was initiated using the following basic input datum:
Specified Pollutant: Freshwater with a 20 PPT salinity deficit.
(A 1 ppt salinity deficit is an appropriate measure for the exposure of marine
organisms to fresh water concentrations. This concentration of 1 ppt is within the
range of typical fluctuations resulting from stormwater runoffs in small eateries.)
Ambient Stream Velocity: 0.075 m/s.
Wind Velocity: 2m/s.
Stream Depth at Diffuser: 1.83 m.
Stream Average Depth Along Diffuser: 1.83 m.
River Ambient Surface and Bottom Density: 1018 kg/m3.
Darch - Weisbach Friction Factor: 0.04
DEFINITIONS:
The following definitions are used throughout the program evaluation:
Near Field: The region where initial jet characteristics of momentum flux, buoyancy
flux, and outfall geometry influence the jet trajectory and mixing.

RIM
Pag
Far Field: The region where the ambient environment controls trajectory dilution of the
turbulent plume through buoyant spreading and passive diffusion due to ambient
turbulence.
Regulatory Mixing Zone (RIVE): The region of receiving water where mixing zone
'm regulations are applied.
"" Beta: The angle measured either clockwise or counterclockwise from the average plan
Mr
Mg
Mull
MI
Fael
MI
WI
ral
project of the port centerline to the nearest diffuser axis. (See Figure C, D.)
Theta: The angle between the port centerline and the horizontal plane. (See Figure C.)
Gamma: The angle measured counterclockwise from the ambient current direction to the
diffuser axis. (See Figure C.)
Sigma: For unidirectional and staged diffusers only, the average horizontal angle of
discharge measured counterclockwise from the ambient current direction (x axis) to the
plan projection of the port centerlines (0 to 360 degrees). (See Figure C.)
Unidirectional Diffuser: A multi -port diffuser with all ports pointing to one side of the
diffuser line and all ports oriented more or less normally to the diffuser line.
Staged Diffuser: A multi -port diffuser where all ports point in one direction, generally
following the diffuser line.

r�1
SIMULATIONS:
Six simulations were run; DFUN23, DFUN24, DFUN25, DFUN26, DFUN27, DFUN28.
In all the simulations the Ambient Parameters were held constant. Ambient river velocity was
reduced from the field measured 0.15 m/s to a conservative 0.075 m/s. A low ambient wind
velocity of 2 m/s was programmed in all the simulations. The shallow depth at the point of
interest results in a uniform (STRCND) density.
In all simulations the data in the Discharge Parameters were held constant except for the
following:
Port Diameter (DO)
Total Discharge (QO)
9.1
Vertical Angle (THETA)
Port diameters were varied from 0.0889 m (3.5 inches) to 0.101 m (4.0 inches) at flows of 0.219
m3/s (5 mgd) and 0.657 m3/s (15 mgd) to analyze the effect of port change and discharge change.
Theta was held constant at 20 degrees for DFUN23, DFUN24, DFUN25, DFUN26, DFUN27.
Theta was set at 45 degrees for DFUN28.
arl
To address the required port horizontal discharge angle (SIGMA) proposed by NCDEM, a
Staged Diffuser system was used in the CORMIX2 analysis (see Figure C and definitions for
description of Staged Diffuser System). Spacing between risers was optimized at 3 m to insure
,,�, effective entrainment.

SUMMATION OF DATA:
MR
Table 1 provides a summation of the six simulations. In all cases the water quality standard
(WQS) of 1 PPT SAL -DEFICIT was achieved within close proximity of the diffuser. In
addition, the WQS was attained prior to a plume surface or bottom impact greater than the WQS.
IvEl
. RECOMMENDATIONS:
MI
fowl
PM
PIM
Based on the six simulations, excellent dilution of the 20 PPT - SALINITY - DEFICIT is
obtained using a 107 m diffuser with 36 - 0.101 m diameter ports and a theta of 20 ° .
The pipe material for the outfall will be specified as similar to those used in the Phase I portion
of the Basewide Waste Treatment Upgrade project. Once the outfall line reaches the edge of
New River Basin, the pipe material will be specified as polyethylene for the underwater section
of the outfall. This material is a heavy -wall conduit which exhibits excellent flow
characteristics, is rugged and requires virtually no maintenance and can be easily fabricated to
meet the specific job requirements.

TABLE 1
Run No.
Plant
Flow
NFR X
Location
NFR
Pollutant
Conc.
NFR
Plume
Thickness
WQS
X
Location
WQS
Pollutant
Conc.
WQS
Plume
Thickness
MGD
Meters
PPT
Meters
Meters
PPT
Meters
DFUN23
5
9.15
0.2859
1.83
1.79
1
0.39
DFUN24
15
9.15
0.669
1.83
4.03
1
0.83
DFUN25
5
9.15
0.2885
1.83
1.79
1
0.39
)DFUN26
15
9.15
0.705
1.83
4.54
1
0.93
DFUN27
15
9.15
0.705
1.83
4.54
1
0.93
DFUN28
5
9.15
0.2885
1.83
1.79
1
0.39
FM WQS = Water Quality Standard
X = Distance from Diffuser in the X Direction (Horizontal)
rim Plume Thickness Measured in Z Direction (Vertical)

APPENDIXES

I. RIVER STUDY
1
n
n

DAVIS & FLOYD INC.
FIELD MEMO
TO:Mr. PANNONE DATE:4-19-95
FROM:JOHN McMAHAN SERIAL NO:10094.JLM
SUBJECT:VELOCITY MEASUREMENTS JOB:10094.00
ON THE NEW RIVER FOR CAMP LEJEUNE
WTP OUTFALL
On April Ott and 5th velocity measurements were collected on
the New River. A site was chosen approximately 1600 feet from
the shoreline along the proposed outfall line for the new
waste treatment plant at Camp Lejeune, USMC
to measure the velocity of the river. This area was chosen
because the discharge would flow into the river from the
Mal outfall between 1300 ft.and 1900 ft. . A request was also
made for information on the direction the New river is flowing
at high and low tides. The velocity meter (Price AA current
PIR
meter) was also used to measure the direction of flow.
At low tide (1724 hr. on 4-4-95) the direction of flow was
downstream. The direction of flow at high tide ( 1114 hr. on
4-5-95) was also downstream.
Below is the data collected at the site:
FLOW DATA FOR 4-4-95 (LOW TIDE)
DISTANCE
FROM
TIME DEPTH FT. REV. SEC. SHORE FT. FLOW F.P.S
1356
1419
1426
1457
1610
1619
1639
1650
1700
2.0 9 40 1600 0. 51 1
3.0 8 40 1600 0.456
2.0 8 40 1600 0.456
3.0 6 40 1600 0.347
2.0 9 40 1600 0.511
3.0 7 40 1600 0.402
2.0 8 40 1900 0.456
3.0 6 40 1900 0.347
2.0 8 40 1600 0.456
3.0 7 40 1600 0.402
2.0 9 40 1600 0. 51 1
3.0 7 40 1600 0.402
2.0 8 40 1600 0.456
3.0 7 40 1600 0.402
2.0 11 40 1600 0.619
3.0 11 40 1600 0.619
2.0 10 40 1600 0.565
3.0 8 40 1600 0.456
FLOW DATA FOR 4-4-95 (LOW TIDE)

MIR
MIN
IMP
DISTANCE
FROM
TIME DEPTH FT. REV. SEC. SHORE FT. FLOW F.P. S
1710 2.0 10 40 1600 0.565
" 3.0 9 40 1600 0.511
1720 2.0 10 40 1600 0.565
" 3.0 8 40 1600 0.456
1725 2.0 10 40 1600 0.565
" 3.0 8 40 1600 0.456
1730 2.0 10 40 1600 0.565
" 3.0 7 40 1600 0.402
FLOW DATA FOR 4-5-95 (HIGH TIDE)
DISTANCE
FROM
MINTIME DEPTH FT. REV. SEC,. SHORE FT. FLOW F.P. S
a.a
own
P IO
ANN
PR
0930 3.0 7 40 1600 0.402
0934 3.0 6 40 1600 0.347
0940 3.0 6 40 1600 0.347
0950 3.0 7 40 1600 0.402
1000 3.0 7 40 1600 0.402
1010 3.0 6 40 1600 0.347
1020 3.0 8 40 1600 0.456
1030 3.0 10 40 1600 0.565
1040 3.0 7 40 1600 0.402
1050 3.0 6 40 1600 0.347
1100 3.0 5 40 1600 0.293
1 110 3.0 7 40 1600 0.402
1120 3.0 8 40 1600 0.456
1 130 3.0 8 40 1600 0.456
1140 3.0 6 40 1600 0.347
1150 3.0 7 40 1600 0.402
1200 3.0 7 40 1600 0.402
1210 3.0 6 40 1600 0.347
1220 3.0 7 40 1600 0.402
1230 3.0 7 40 1600 0.402
* DEPTH=measured from the surface down
* FPS = Feet Per Second
The velocity meter is a Price AA current meter with rating
limits of 0.25 FPS to 8.0 FPS
Equations: Less than 40 REVS= rev/time x 2.180 + 0.020 = FPS
Greater than 40 REVS= rev/time x 2.170 + 0.030 = FPS

LE. LOCATION MAPS

1
1
;foul
•
:Foul
FARNELL..,Pier
ti
`�.,.. BAY �2
'cb j� ti• j I
.?::Foul
2 !�
z
0
,\ Light
z
Blu
m = 9
s Dolo :.
Piling
A Daybeacon(C)
1 0
I �
Id
0
I
a
Tan
FP,g te,..43.----CaSSIC
Lfc.6� t��is'j 1:11
D ► F �st,,;;r
txi Ruins
350' 14151
J
CO
a
1
r
1
n
5
l I
/9 `
'
1' ,jam\`
3
Weil Pt
C1
FRENCHS CREEK WASTEWATER TREATMENT FACILITIES
CAMP LEJEUNE JACKSONVILLE, NORTH CAROLINA
1
■
TITLE:
OUTFACE TO NEW RIVER
ENGINEERS ARCHITECTS
PLANNERS SC[ENTISTS
PROJECT LOCATION CAMP LEJEUNE
SYSTEM: -
DRN. BY: J.W.A.
DATE: 4-27-95
CHK'D BY: B.V.P.
REV
x
CHARLESTON • GREENWOOD • COLUMBIA
DWG. No.: 1 OF 1
Figure A

9
-2r DIVISION
%BILLETING
AREA
HADN
POINT
ARE
EXISTING HADNOT POINT
WASTEWATER TREATMENT
FACILITIES
1SUTFALL 8 DIFFUSER
EE SHEET 2
LI
PRO' D FRENCHS CREEK
WA' Ek TER TREATMENT
F.4 ILI' ' ES
BASE SANITARY
LANDFILL
'
Cow heed
L.
0
COMBAT
TOWN
1000 0 2000 4000 6000
HMI I 1 I 1 I -1
GRAPHIC SCALE
s
WIC..iq AlCN[riCT1
►urxaa Aa:a�rar�
CAP LE.EUDE NORTH CAROLNA
FRENCHS CREEK WASTEWATER
TREATMENT FACILITIES
PHASED
PROPOSED WASTEWATER TREATMENT
FACILITY & OUTFALLINTO NEW RIVER
JUNE,1995 SHEET 1 OF 2

0
0
te
Q)
� I
N 330,420
-5.08
N 329,420 .4
-7.73
LLJ
N 328,420 m
0, 01 8.
T1 Q1 1 a1
O)
1 *I .4-1
N N N
W I WI W I
-7.75 0 -1.600 1
-6.48 4)- -1.68�
-9.34 ' -6.62
LLJ
z
N 327`420
-4.48 0
N 326,420 0
EDGE OF RIVER
350'
DIFFUSER
NOTES: 1
1.) VERTICAL DATUM; WATER SURFACE
(APPROXIMATE ELEV. 1.00 MSL)
2.) NEGATIVE NUMBERS INDICATE ACTUAL
DEPTH OF WATER
PROPOSED LOCATION
OF OUTFALL LINE
• _ FROM WASTEWATER
-4.36TREATMENT PLANT
-6.08 -6.23
m
-4.79 I -7.35 I
a 4
EDGE OF RIVER
-0.85
FRENCHS
CREEK
D
aw[Mss�� allOrI TUT.
► AMM. senrnsrs
emo....a....,. • MANY
NMI OWL.
CHAP LEJEUNE NORTH CAROLINA
FRENCHS CREEK WASTEWATER
TREATMENT FACILITIES
PHASE II
WASTEWATER TREATMENT PLANT
AND OUTFALL TO NEW RIVER
JUNE 1995 SHEET 2 OF 2
Figure C

I. GEOMETRIC DIAGRAMS

Pal
gag
PAIN
MO
net
A*
mai
-)
/ ly
ua
ws
Plan -View Cross -Section
DISTB
this-, ,-,,,,i4rrr4/144r4,4/4.
Nearest Bank
a) Definition Diagram CORMIX2 (Special case: HA =HD)
Z =hint
HO
— hint =0.9HD
-- l-Density profile
example
Range
of hint
— hint =0.4HD
'--"—ho=0.33H0
D Range
80 of h0
tho
frn�►,iv.�a Z = 0
D < HD/5 Range
of D
b) Limits of Applicability CORMIX2
CORMIX2 DISCHARGE GEOMETRY AND RESTRICTIONS•
Figure D

ono
ray
MIA
+�1
tat
all
411110
MO
fait
LD
UNIDIRECTIONAL DIFFUSER DESIGN
STAGED DIFFUSER DESIGNS
CONFIGURATIONS OF COMMON MULTIPORT DIFFUSER TYPES
Figure E

tr
W. OUTFALL AND DIFFUSER DETAILS
"4,

1 1 1 4 1 1 1 1 1 1 i 1 l 1 1 I 1 1 1
0
-10
-20
q
i
U V STRUCTURE
48"0
pPE
PLANT ENTRANCE ROAD
♦
♦
♦
♦
♦
48" 10 PIPE
PLAN
30.00
IsA
0 CO 200 300 400 cob600
H 1----1 1---1 I-1
14600
i
f OUT AT UV STRUCTURE
20 ;�:1.: JJ1�.. ;�JJ E». fT. 6t8.U. �tta ..;... aa .:... aa JJJ.,.,.t...t.- .a.W.GRORiOJE�O.CtE..tOv.w^ttr• +J.. tt ..t:...e..Lat •. a♦. :. R51F$1�• BDiin
.....,... ,...t .......� ....J-�teykV ER
. . .. J501
.. ...10 yr+ r„, • • J.:�• .1:.
.. ... ::t....:::.. .
0.00 5.00
10.00 15.00 20.00 25.00
PROFILE
30.00 35.00 1 40.00 44.00
20
10
0
-10
-20
DAiNS
SRSIRTZ'U 41101111110111
PLaNR,*a ICIIRTUt7
tttttt OM•ta,Mll'fi•tiR�11RL
t.,ORtY
CAP LE. EUNE NORTH CAROLINA
FRENCHS CREEK WASTEWATER
TREATMENT FACILITIES
PHASE 11
PROPOSED OUTFALL INTO NEW RIVER

l 1 1 1 1 1 1. 1 1 1 1 1 1 1 1 l 1 1
ij
w
OR
sr
APPRX WATER SURFACE
20° z-8x4 REDUCER
. RIVER BOTTOM
0
N
0~ rTT
"fri- L''TIE-L I
8" ID PIPE
SECTION
48" ID PIPE
8" PIPE
DIFFUSER DETAIL
NO SCALE
0
8" PIPE ALTERNATE
ROTATION ALONG CL
4\-48" ID PIPE
BLIND FLANGE
PLAN
36 DIFFUSERS ID 10.0' SPACING
10.0'
48" ID PIPE
ELEVATION
10.0'
2.6'
—I
BLIND FLANGE
DiWIS
mamma 1111310tun
11110111116
Mal MINIM •
CAMP LLEtR& NORTH CWiOLP A
FRENCHS CREEK WASTEWATER
TREATMENT FACILITIES
PHASE n
PLANT EFFLUENT DIFFUSER DETAIL

IV. RUN DFUN23

Met
CORMIX SESSION REPORT:
IYIII%XXXZIZIZXXI IIIBIIXXXXXXX XIXXXxIxxzIxmhxIIxI XXMIXXXXXXXX%%I
CORHII: CORNELL MIXING ZONE EXPERT SYSTEM
CORHIX v.3.10 June 1995
SITE NAME/LABEL: . CAMP LIMNS
DESIGN CASE:
FILE NAME:
'°'W Using subsystei COMM:
Start of session:
• 5 RGD STAGED 101 K DIFFUSER 36 PORTS
DFUN23
Submerged Multiport Diffuser Discharges.
06/08/95--22:35:36
:*ttt:*****t::tttt*:***********tt**:*:*ttt#t**********:*tithemt*****:t*****
SUMMARY OF INPUT DATA:
AMBIENT PARAMETERS:
Cross-section
Average depth
Depth at discharge
Ambient velocity
• Darcy-Keisbach friction
AMA
OMR
RNA
hind .velocity
Stratification Type
Surface density
Bottom density
HA
HD
UA
factor F
STRCND = U
RHOAS
RHOAB =
= unbounded
• 1.83 a
• 1,83 m
• 0.015 a/s
• 0.04
2 a/s
1018 kg/a"3
1018 kgla"3
DISCHARGE PARAMETERS:
Diffuser type
Diffuser length
Nearest bank
Diffuser endpoints
Number of openings
Submerged Multiport Diffuser Discharge
DITYPE = staged perpendicular
LD = 101 a
✓ left
Y81 = 450a; YB2= 557a
ROPER = 36
Spacing between risers/openings SPAC = 3.05 n
Port/Nozzle diaieter D0 = 0.0889 a
Equivalent slot width B0 - 0.0020 a
Total area of openings A0 0.0062 1"2
Discharge velocity. U0 - 0.98 a/s
Total discharge flowrate Q0 - 0.219 11"3/s
Discharge port height H0 - 0.6 m
Nozzle arrangement BETYPE = staged
Diffuser alignment angle GAMMA = 90 deg
Vertical discharge angle THETA = 20 deg
Horizontal discharge angle SIGMA = 210 deg
Relative orientation angle BETA = 0 deg
Discharge temperature (freshwater) - 22 deg
Corresponding density RH00 = 997.7714 kg/1"3
Density difference DRHO = 20.2285 kg/m43
Buoyant acceleration GPO - .1949 m/s"2
Discharge concentration CO - 20 PPT-SAL-DEFICIT
Surface heat exchange coeff. KS - 0 a/s
Coefficient of decay KD = 0 /s
FLUX VARIABLES PER UNIT DIFFUSER LENGTH:
Discharge (volume flux) q0 - 0.002047 1"2/8
""" Moaentum flux 10 - 0.002006 103/s"2
Buoyancy flux j0 = 0.000399 n"3/s"3
DISCHARGE/ENVIRONMENT LENGTH SCALES :
lq = 0.00 a la = 0.35 s 1M = 0.37 a
la' = 99999.0 a lb' = 99999.0 a la = 99999.0 a
(These refer to the actual discharge/environment length scales.)

lent
Nat
NOR -DIMENSIONAL PARAMETERS:
Slot .Froude nnaber FRO - - 48.58
Port/nozzle Froude muaber FRDO = 7.44
Velocity ratio R - 13.06
NIXING ZONE / TOXIC DILUTION ZONE / AREA OF INTEREST PARAMETERS:
Toxic discharge
later quality standard specified'
Water quality standard CSTD
Regulatory fixing zone
Region of interest
= no
= yes
= no
1 PPP -SAL -DEFICIT
1000.00 a downstreaa
!t****tttttt*tltt!!tt!lttt!**Wrtt*tt+ttt*lttttt*!tt*ttttt!tt*ttlttiMattttt
HYDRODYNANIC CLASSIFICATION:
+ . t
1 FLOW CLASS a NU6 1.
* • *
This flow configuration applies to a layer corresponding to the full water.
depth at the discharge site.
Applicable layer depth = water depth z 1.83 a
+tttt*tttttt******t*!**ttt***tt*tt**ttttttttttt+*t**t**tttttttt*tttttt**t*ttt
Amo NIXING ZONE EVALUATION (hydrodynaaic and regulatory unary):
Ise
X-Y-Z Coordinate systei:
Origin is located at the bottoi below the port center:
503.50 a frog the left bank/shore.
Nuaber of display steps NSW = 5 per module.
mum NEAR -FIELD REGION (NFR) CONDITIONS :
Note: The NFR is the zone of strong initial nixing. It has no regulatory
iaplication. However, this information 'ay be usefulfor the discharge
Anndesigner because the ailing in the NFR is usually sensitive to the
discharge design conditions.
Pollutant concentration at edge of NFR = .2859 PPT-SAL -DEFICIT
Dilution at edge of NFR = 69.9
NFR Location: x = 9.15 m
(centerline coordinates) y = -10.42 t
z= 1.83n
a.. NFR plate diaensions: half -width = 55.81 a
thickness = 1.83 a
Buoyancy assessment:
The effluent density is less than the surrounding aabient water
density at the discharge level.
Therefore, the effluent is POSITIVELY BUOYANT and will tend to rise towards
the surface.
Near -field instability behavior:
The diffuser flow will experience instabilities with full vertical airing
in the near -field.
There aay be benthic impact of high pollutant concentrations.
FAR -FIELD NIXING SUMMARY:
Plume becomes vertically fully aired WITHIN REAR -FIELD at .00 a
downstreaa, but RE -STRATIFIES LATER and is not aired in the far -field.
*t*****t**************t* TOXIC DILUTION ZONE SUMMARY ***********t**t*********
No TDZ was specified for this siaulation.

ttt*t**t*tt*******tt*t REGULATORY NIXING ZONE SUMMARY tt**ttttt*t*****tttttt*
No Minas been specified.
However:
The atbient water quality standard was encountered at the following
pluae position:
Water quality standard - 1 PPT-SAL-DEFICIT
Corresponding dilution - 20
Pluse location: x = 1.79 a
(centerline coordinates) y = 40.96 a
z= .66a
Flute diaensions: half -width = 10.98 a
thickness. = .39 a
********************* FINAL DESIGN ADVICE AND COMMENTS ***tttt********t******
CORMIX2 uses the TWO-DIMENSIONAL SLOT DIFFUSER CONCEPT to represent
the actual three-dieensional diffuser geosetry. Thus, it approxisates
the details of the aerging process of the individual jets frai each
port/nozzle.
In the present design, the spacing between adjacent ports/nozzles
(or riser asseablies) is of the order of, or less than, the local
water depth so that the slot diffuser appraxinatioa holds well.
Nevertheless, if this is a final design, the user is advised to use a
final CORED (single portdischarge) analysis, with discharge data
for an individual diffuser jet/pluae, in order to coapare to
the present near -field prediction.
REMINDER: The user lust take note that HYDRODYNAMIC MODELING by any known
technique is NOT AN EXACT SCIENCE.
Extensive caparison with field and laboratory data has shown that the
CORM% predictions on dilutions and concentrations (with associated
pluae geoaetries) are reliable for the aajority of cases and are accurate
to within about +-501 (standard deviation) .
As a further safeguard, CORM% will not give predictions whenever it judges
the design configuration as highly conplex and uncertain for prediction.
t*t*t**tt*****t**t*ttt********ttt***ttt*****tt*t Mtt***t*tttttit*tttttt M
DESIGN CASE: 5 MGD STAGED 107 M DIFFUSER 36 PORTS
FILE NAME: DFUN23
Subsystei CORMIX2: Subaerged Multiport Diffuser Discharges
END OF SESSION/ITERATION: 06/12/95--11:4S:40
%%%%%%%%%%%%%H%%%I%%%%%%%%%%%%%%%%%%%%%%%%%I%IIIII %%X%%%%MXIX%%%%%%I%%%%%

A�q
CORKIX2 PREDICTION FILE:
22222222222222222222222222222222222222222222222222222222222222222222222222222
CORNELL NIXING ZONE EXPERT SYSTEM
Subsystea CORKIX2: Subsystea version:
Subaerged Kultiport Diffuser Discharges CORKIX v.3.10 June 1995
CASK DESCRIPTION
Site naae/label:
Design case:
FILE HAKE:
Tile of Fortran run:
CAKP"LEJEUNE
5"KGD"STAGED"107"K"DIFFUSER"36"PORTS
coraixlsia\DFUN23 . cx2
06/08/95--22:42:56
ENVIRONMENT PARAKETERS (aetric units)
Unbounded section
HA = 1.83 HD : 1.83
UA = .015 F : .040 USTAR a .5303E-02
UN = 2.000 UWSTAR= .2198E-02
Unifora density environaent
STRCND: U RHOAK = 1018.0000
DIFFUSER :DISCHARGE PARAMETERS (aetric units)
Diffuser type: DITYPE: staged perpendicular
BANK : LEFT DISTB : 503.50 YB1 = 450.00 YB2 = 557.00
LD : 107.00 NOPEN = 36 SPAC : 3.06
D0 = .089 A0 = .006 H0 - .60
Nozzle/port arrangeaent: staged
GAKKA : 90.00 THETA = 20.00 SIGMA : 270.00 BETA = .00
U0 = .980 Q0 = .219 = .2190E+00
RH00 : 997.1114 DRH00 = .2023E+02 GPO = .1949E+00
CO = .2000E+02 CUNITS= PPT-SAL-DEFICIT
IPOLL = 1 KS = .0000E+00 KD :.0000E+00
FLUX VARIABLES - PER UNIT DIFFUSER LENGTH (aetric units)
q0 = .2047E-02 10 = .2006E-02 j0 = .3988E-03 SIGNJO= 1.0
Associated 2-d length scales (neters)
1Q=B = .0021K = .37 la - .36
lap = 99999.00 lbp = 99999.00 la = 99999.00
FLUX VARIABLES - ENTIRE DIFFUSER (aetric units)
Q0 = .2190E+00 K0 = .2146E+00 J0 = .4267E-01
Associated 3-d length scales (aeters)
LQ = .47 LK = 1.53 La : 6.18 Lb
Lep = 99999.00 Lbp
NON -DIMENSIONAL PARAKETERS
FRO = 48.58 FRDO = 7.44 R - 13.06
(slot) (port/nozzle)
FLOW CLASSIFICATION
222222222222222222222222222222222222222222
2 Flow class (CORKIX2) = KU6 2
2 Applicable layer depth HS = 1.83 2
222222222222222222222222222222222222222222
101.16
= 99999.00

Mgt
talgl
Mgt
MIXING ZONE / TOXIC DILUTION / REGION OF INTEREST PARAMETERS
CO a .2000E+02 CUBITS= PPT-SAL-DEFICIT
NTOX = 0
NSTD = 1 CSTD = .1000E+01
REGNZ = 0
XINT r 1000.00 IKAX = 1000.00
X-Y-Z COORDINATE SYSTEM:
ORIGIN is located at the bottom and the diffuser mid -point:
503.50 m from the LEFT bank/shore.
X-axis points downstream, Y-axis points to left, Z-axis points upvard.
NSTEP s 5 display intervals per module
BEGIN NOD202: DISCHARGE NODULE (STAGED DIFFUSER)
Due to complex near -field motions: EQUIVALENT SLOT DIFFUSER (2-D) GEOMETRY
Profile definitions:
BV m Gaussian 1/e (37t) half -width, in vertical plane normal to trajectory
BH s Gaussian 1/e (37%) half-vidth in horizontal plane normal to trajectory
S z hydrodynamic centerline dilution
C = centerline concentration (includes reaction effects, if any)
% Y Z S C BV BH
.00 53.50 .60 1.0 .200E+02 .04 .04
END OF K0D202: DISCHARGE MODULE (STAGED DIFFUSER)
"' BEGIN KOD215: STAGED PERPENDICULAR DIFFUSER IN STRONG CURRENT
ISNO
Because of the strong ambient current the diffuser plume of this crossfloving
discharge gets RAPIDLY DEFLECTED.
A sear -field zone is formed that is VERTICALLY FULLY NIXED over the entire
layer depth. Full nixing is achieved at a dovnstrean distance of about
five (5) layer depths.
Profile definitions:
BV = layer depth (vertically mixed)
BH = top -hat half -width, measured horizontally in y-direction
S = hydrodynamic average (bulk) dilution
C = average (bulk) concentration (includes reaction effects, if any)
mill
% Y Z S C BV BH
.00 53.50 .60 1.0 .199E+02 .04 .04
** WATER QUALITY STANDARD OR CCC HAS BEEN FOUND **
0•1 The pollutant concentration in the plume falls below water quality standard
or CCC value of .100E+01 in the current prediction interval.
This is the spatial extent of concentrations exceeding the vater quality
RIM standard or CCC value.
1.83 40.71 .66 31.8 .628E+00 .40 11.20
3.66 27.93 .73 44.6 .448E+00 .76 22.35
5.49 15.14 .79 54.4 .368E+00 1.12 33.51
7.32 2.36 .85 62.7 .319E+00 1.47 44.66
9.15 -10.43 .92 70.0 .286E+00 1.83 55.82
Cumulative travel time = 122. sec
END OF K0D275: STAGED PERPENDICULAR DIFFUSER I11 STRONG CURRENT
** End of NEAR -FIELD REGION (NFR) **

BEGIN MOD241: BUOYANT AMBIENT SPREADING
Mal
FOR
Profile definitions:
BY s top -hat thickness, aeasured vertically
BH = top -hat half -width, measured horizontally in y-direction
ZU = upper plume boundary (Z-coordinate)
ZL r lower pluce boundary (Z-coordinate)
S = hydrodynanic average (bulk) dilution
C = average (bulk) concentration (includes reaction effects, if any)
Pluae Stage 1 (not bank attached):
IYZS C BY BH ZU ZL
9.15 -10.43 1.83 70.0 .286E+00 1.83 55.82 1.83 .00
207.32 -10.43 1.83 93.3 .114E+00. .90 151.54 1.83 .93
405.49 _ -10.43 1.83 111.4 .180E+00 .74 219.67 1.83 1.09
603.66 -10.43 1.83 03.3 .150E+00 .70 276.71 1.83 1.13
801.83 -10.43 1.83 161.3 .124E+00 .72 327.32 1.83 1.11
1000.00 -10.43. 1..83 196.4 .102E+00 .77 373.75 1.83 1.06
Cuiulative travel tine = 13333. sec
Siiulation lint based on aaxiium specified distance = 1000.00 i.
This is the REGION OF INTEREST limitation.
END OF K0D241: BUOYANT AMBIENT SPREADING
nog CORMIX2: Subaerged Kultiport Diffuser Discharges Bad of Prediction File
22222222222222222222222222222222222222222222222222222222222222222222222222222
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CORHI%: CORRELL MIXING ZONE EXPERT SYSTEM
CORK! v.3.10 June 1995.
SITE NAME/LABEL: CAMP LEJEUNE
DESIGN CASE: 15 MGD STAGED 107 M DIFFUSER 36 PORTS
FILE NAME: DFUN24
Using . subsystem CORMIX2: Submerged Multipart Diffuser Discharges
Start of session: 06/08/95--22:53:28
****************************************************************************
SUMMARY OF INPUT DATA:
AMBIENT PARAMETERS:
Cross-section
Average depth
Depth at discharge
Ambient velocity
Darcy-Neisbach friction factor
Kind velocity
Stratification Type
Surface density
Bottom density
HA
BD
UA
F
UK STRCND = U
RHOAS =
RHOAB
= unbounded
= 1.83 a
• 1.83 n
• 0.075 m/s
= 0.04
2 m/s
1018 kg/1"3
1018 kg/n"3
DISCHARGE PARAMETERS:
Diffuser type
Diffuser length
Nearest bank
Diffuser endpoints
Number of openings
Spacing between risers/openings
Port/Nozzle diameter
Equivalent slot width
Total area of openings
Discharge velocity
Total discharge flowrate
Discharge port height
Nozzle arrangement
Diffuser alignment angle
Vertical discharge angle
Horizontal discharge angle
Relative orientation angle
Submerged Multipart Diffuser Discharge
DITYPE = staged perpendicular
LD = 107
• left
YB1 - 450a; YB2= 557a
ROPER
SPAC
D0
B0
A0
U0
Q0
H0
BETYPE
GAMMA
THETA
SIGMA
BETA
Discharge temperature (freshwater)
Corresponding density RH00
Density difference DRHO
Buoyant acceleration GPO
Discharge concentration CO
Surface heat exchange coeff. KS
Coefficient of decay KD
36
• 3.05 m
• 0.0889 a
• 0.0020 m
• 0.0062 m"2
= 2.94 m/s
• 0.657 11"3/s
0.6 a
• staged
90 deg
20 deg
210 deg
0 deg
22 deg
• 997.7714 kg/m"3
• 20.2285 kg/u"3
• .1949 1/102
20 PPT-SAL-DEFICIT
0m/s
0 /s
FLUX VARIABLES PER UNIT DIFFUSER LENGTH:
Discharge (volume flux) q0 = 0.006140 142/s
Momentum flux 10 = 0.018053 1143/8"2
Buoyancy flux j0 - 0.001196 m43/s"3
DISCHARGE/ENVIRONMENT LENGTH SCALES :
lq = 0.00 a la = 3.20 a 1M = 1.60 m
la' = 99999.0 n lb' = 99999.0 a la = 99999.0 n
(These refer to the actual discharge/environment length scales.)

RAF
PAR
1
PER
PEA
PAR
PAg
1
FAR
Rap -DIMENSIONAL PARAMETERS:
Slot Fronde flusher FR0 - 145.76
Port/nozzle Fronde number FRDO = 22.33
Velocity ratio R - .39.20
MIXING ZONE / TOXIC DILUTION ' ZONE / AREA OF INTEREST PARAMETERS:
Toxic discharge = no
Water quality standard specified = yes
slater quality standard CSTD = 1 PPT-SAL-DEFICIT
Regulatory nixing zone - = no
Region of interest - 1000.00 a downstream
tttt:tttttttfMtttttttttttttttttttttttttttt:ttttttttttttttttttttttttttttttttt
HYDRODYNAMIC CLASSIFICATION:
t t
I FLOW CLASS = MU6 I
t t
This flow configuration applies to a layer corresponding to the full water
depth at the discharge site.
Applicable layer depth = water depth = 1.83 a
t:ttttttttttttttttt::ttt:ttttttttttttttttttttt:tttttttttttttttattt:ttttttt:tt
MIXING ZONE EVALUATION (hydrodynamic and regulatory summary):
X-Y-Z Coordinate system:
Origin is located at the bottom below the port center:
503.50 m from the left bank/shore.
Number of display steps NSTEP = 5 per module.
NEAR -FIELD REGION (NFR) CONDITIONS :
Note: The MIR is the zone of strong initial airing. It has no regulatory
implication. However, this information may be useful for the discharge
designer because the mixing in the NIR is usually sensitive to the
discharge design conditions.
Pollutant concentration at edge of NFR = .6690 PPT-SAL-DEFICIT
Dilution at edge of NFR - 29.8
NIR Location: x = 9.15 a
(centerline coordinates) y = -93.82 a
z = 1.83 m
NIR plume dimensions: half -width =. 71.54 n
thickness = 1.83 a
Buoyancy assessment:
The effluent density is less than the surrounding ambient water
density at the discharge level.
Therefore, the effluent is POSITIVELY BUOYANT and will tend to rise towards
the surface.
Near -field instability behavior:
The diffuser flow will experience instabilities with full vertical nixing
in the near -field.
There may be benthic impact of high pollutant concentrations.
FAR -FIELD, MIXING SUMMARY:
Plume becomes vertically fully aired WITHIN NEAR -FIELD at .00 n
downstream, but RE -STRATIFIES LATER and is not nixed in the far -field.
ttttttttttttttttttttttt: TOXIC DILUTION ZONE SUMMARY tttt:ttttttttttttttttttt
No TDZ was specified for this simulation.

Plq
************a********* REGULATORY MIRING ZONE SUMMARY **a***a*aa*******a****a
No RNZ has been specified.
However:
The aabient water quality standard was encountered at the following
plune position:
Hater quality standard - 1 PPT-SAL-DEFICIT
Corresponding dilution 20
Pluae location: x 4.03 a
(centerline coordinates) y z -11,51 a
z= .13a
Pluae diaensions: half -width = 31.59 a
thickness = .83 a
********************* FINAL DESIGN ADVICE AND CONVENTS **********************
CORMIB2 uses the TW0-DIMENSIONAL SLOT DIFFUSER CONCEPT to represent
the actual three -diaensional diffuser geotetry. Thus, it approxiaates
the details of the aerging process of the individual jets from each
port/nozzle.
In the present design, the spacing between adjacent ports/nozzles
(or riser asseablies) is of the order of, or less than, the local
water depth so that the slot diffuser approxiaation holds well.
Nevertheless, if this is a final design, the user is advised to use a
final CORMII1 (single port discharge) analysis, with discharge data
for an individual diffuser jet/pluae, in order to coapare to
the present near -field prediction.
REMINDER: The user oust take note that HYDRODYNAMIC MODELING by any known
Pal technique is HOT AN EXACT SCIENCE.
Extensive coaparison with field and laboratory data has shown that the
CORMII predictions on dilutions and concentrations (with associated
pluie geoeetries) are reliable for the aajority of cases and are accurate
to within about +-50% (standard deviation).
As a further safeguard, CORMII will not give predictions whenever it judges
the design configuration as highly coaplex and uncertain for prediction.
**********************a*******a*ataaaaa.a.aaaato*aaataa:aaaa.aaata*********aa
DESIGN CASE: 15 EGO STAGED 101 M DIFFUSER 36 PORTS
FILE NAME: DFUN24
A•+ Subsystea CORHII2: Subaerged Multipart Diffuser Discharges
END OF SESSION/ITERATION: 06/12/95--11:51:11
IIIIIIIIIIIIIIIIIIIIII%IIIIIIIIIIIIIIIIIIIIIIIIIIIIIIIIIIIIIIIIIIIIIIIIIIIIII

CORKII2 PREDICTION FILE:
22222222222222222222222222222222222222222222222222222222222222222222222222222
CORNELL NIXING ZONE EXPERT SYSTEM
Subsystem CORMIX2: Subsystem version:
Submerged Multipart Diffuser Discharges - CORNII v.3.10 June 1995
CASE DESCRIPTION
Site nanellabel:
Design case:
metFILE NAME:
Time of Fortran run:
CAXP"LEJEUNE
15AMGD"STAGED"107AKADIFFUSERA36"PORTS
coriizlsii\DFU124 . cx2
06/08/95--22:57:10
ENVIRONMENT PARAMETERS (metric units) •
"mq Unbounded section
HA : 1.83 HD : 1.83
UA = .075 F - .040 USTAR ..5303E-02
UN : 2.000 UNSTAR..2198E-02
Uniform density environment
STEIN U RHOAK : 1018.0000
F
DIFFUSER DISCHARGE PARAMETERS (metric units)
Diffuser type: DITYPE: staged perpendicular
BANK : LEFT DISTB : 503.50 YB1
Pal LD - 107.00 NOPEN : 36 SPAC
DO : .089 A0 = .006 H0
Nozzle/port arrangement: staged
GAMMA = 90.00 THETA : 20.00 SIGMA : 270.00
U0 - 2.940 00 : .657 ..6570E+00
RHOO : 997.7714 DRHOO ..2023E+02 GPO = .1949E+00
CO :.20008+02 CUBITS: PPP -SAL -DEFICIT
IPOLL : 1 KS ..0000E+00 KD = .0000E+00
450.00 YB2 : 557.00
3.06
.60
BETA = .00
FLUI VARIABLES - PER UNIT DIFFUSER LENGTH (metric units)
q0 ..6140E-02 m0 ..1805E-01 j0 ..1196E-02 SIGNJO= 1.0
Associated 2-d length scales (ieters)
1Q=B : .002 1M : 1.60 li : 3.21
pi; Imp : 99999.00 lbp : 99999.00 la : 99999.00
COM
FLUX VARIABLES ENTIRE DIFFUSER (aetric units)
Q0 6570E+00 KO ..1931E+01 JO ..1280E+00
Associated 3-d length scales (meters)
LQ - .47 LK 4.58 La : 18.53 Lb
Lip : 99999.00 Lbp
NON -DIMENSIONAL PARAMETERS
FRO : 145.76 FRDO : 22.33 R - 39.20
(slot) (port/nozzle)
FLOW CLASSIFICATION
222222222222222222222222222222222222222222
2 Flow class (CORMIX2) - KU6 2
2 Applicable layer depth HS = 1.83 2
222222222222222222222222222222222222222222
• 303.47
• 99999.00

PER
MIIING ZONE / TOIIC DILUTION / REGION OF INTEREST PARAMETERS
CO = .2000E+02 CUNITS: PPT-SAL-DEFICIT
NTOI = 0
NSTD = 1 CSTD = .1000E+01
REGKZ = 0
IINT = 1000.00 IMA% = 1000.00
%-Y-Z COORDINATE SYSTEM
ORIGIN is located at the bottom and the diffuser mid -point:
503.50 m from the LEFT bank/shore.
X-axis points downstream, Y-axis points to left, Z-axis points upward.
NSTEP = 5 display intervals per module
BEGIN K0D202: DISCHARGE MODULE (STAGED DIFFUSER)
Due to complex near -field motions: EQUIVALENT SLOT DIFFUSER (2-D) GEOMETRY
Profile definitions:
BV = Gaussian 1/e (31%) half -width, in vertical plane normal to trajectory
BH-= Gaussian 1/e (31%) half -width in horizontal plane normal to trajectory
S = hydrodynamic centerline dilution
C = centerline concentration (includes reaction effects, if any)
% Y Z S C BV BH
.00 53.50 .60 1.0 .200E+02 .04 .04
END OF KOD202: DISCHARGE MODULE (STAGED DIFFUSER)
BEGIN KOD275: STAGED PERPENDICULAR DIFFUSER IN STRONG CURRENT
Because of the strong ambient current the diffuser plume of this crossflowing
discharge gets RAPIDLY DEFLECTED.
A near -field zone is formed that is VERTICALLY FULLY NIXED over the entire
layer depth. Full mixing is achieved at a downstream distance of about
five (5) layer depths.
Profile definitions:
ran BV = layer depth (vertically mixed)
BH = top -hat half -width, measured horizontally in y-direction
S = hydrodynamic average (bulk) dilution
C = average (bulk) concentration (includes reaction effects, if any)
I Y Z S C BV BH
.00 53.50 .60 1.0 .200E+02 .04 .04
MEI
1.83 24.03 .66 13.9 .144E+01 .40 14.34
3.66 -5.43 .73 19.3 .104E+01 .76 28.64
** WATER QUALITY STANDARD OR CCC HAS BEEN FOUND **
The pollutant concentration in the plume falls below water quality standard
or CCC value of .100E+01 in the current prediction interval.
This is the spatial extent of concentrations exceeding the water quality
standard or CCC value.
5.49 -34.90 .79 23.4 .855E+00 1.12 42.94
7.32 -64.36 .85 26.8 .745E+00 1.47 57.24
9.15 -93.83 .92 29.9 , 669E+00 1.83 71.54
"NR Cumulative travel time = 122. sec
END OF K0D275: STAGED PERPENDICULAR DIFFUSER IN STRONG CURRENT

** End of NEAR -FIELD REGION (NFR) **
BEGIN KOD241: BUOYANT ANBIENT SPREADING
Profile definitions:
BV = top -hat thickness, aeasured vertically
BH = top -hat half-vidth, aeasured horizontally in y-direction
ZU = upper plum boundary (Z-coordinate)
ZL = lover pluie boundary (Z-coordinate)
S = hydrodynaaic average (bulk) dilution
C = average (bulk) concentration (includes reaction effects, if any)
Pluae Stage 1 (not bank attached):
I Y Z S C BV BH ZO ZL
9.15 -93.83 1.83 29.9 .669E+00 1.83 71.54 1.83 .00
207.32 -93.83 1.83 40.1 .499E+00 .83 211.64 1.83 1.00
405.49 -93.83 1.83 46.2 .433E+00 .66 307.90 1.83 1.17
603.66 -93.83 1.83 52.3 .382E+00 .59 386.90 1.83 1.24
Mr, 801.83 -93.83 1.83 59.5 .336E+00 .57 455.91 1.83 1.26
1000.00 -93.83 1.83 67.9 .295E+00 .57 518.35 1.83 1.26
Cumulative travel tine = 13333. sec
Siaulation lint based on aaziaua specified distance = 1000.00 a.
This is the REGION OF INTEREST liaitation.
END OF M0D241: BUOYANT AMBIENT SPREADING
CORKII2: Subaerged Multiport Diffuser Discharges End of Prediction File
22222222222222222222222222222222222222222222222222222222222222222222222222222
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CAM -LE EUNE
. COPML 2 Prediction
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1 1 1 1
200
r 1 1 -1 1 T 1 1 1
400 600 800
Plan Ui eu
i000
X (In)

1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1
CAMP " -LEJEUNE
COPMI X2 Prediction.
IG^MGD^STAGED^l. D7 All^DI FFUGGP^36^PDPTG File: si m DF UN24 . c =::
0
-
Ic\e"\
(PPT-sFL-DErI EI n x
-
a
c'o-
0-
0
-4--
Q-
0
dO. 0
I t I
1
1 ' 1 1 I I 1 I 1 i I
1.5 3.0 4.5 6.0 7.5
Concentration vs Downstream Distance
X f rn
9.0

1 1 ➢ 1 1 1 1 1 1 1 1 1 1
CAMP -\ LEJEUNE
COPNI '2 Prediction
i 5AMGOASTiGEO"i U7 ^11^UI FFU.SEP^3 ADOPTS File: si =.OF'UN24 . c .2.
io _
co-
-
NJ
0
200
Oi t or t i on = 318.225
rr:* Y Mi i
400 600 800 1000
X On) -4
Side LJi eta

VI. RUN DFUN25

CORMX: CORNELL MIXING• ZONE EXPERT SYSTEM
CORM% v.3.10 June 1995
SITE NAME/LABEL: CAMP LEJEUNE
DESIGN CASE: 5 KGD STAGED 107 a 36 0.101 a PORTS
PER FILE NAME: DFUN25
Using subsystem CORED: Subterged Multipart Diffuser Discharges
Start of session: 06/11/95--14:13:31
::ttttttttttttttttt•tttttttttttttttt:tttttttttttttttttttttttttttttttttttttttt
SUMMARY OF INPUT DATA:
AMBIENT PARAMETERS:
F41 Cross-section s unbounded
Average depth HA - 1.83 a
Depth at discharge HD - 1.83 a
WI Ambient velocity UA = 0.075 t/s
Darcy-Neisbach friction factor F = 0.04
Hind velocity UN - 2 a/s
Stratification Type STRCND = U
W' Surface density RHOAS = 1018 kg/143
Batton density RHOAB = 1018 kg/a43
p+ DISCHARGE PARAMETERS: Submerged Multipart Diffuser Discharge
Diffuser type DITYPE = staged perpendicular
Diffuser length LB = 107 1 •
Nearest bank = left
Falq
Diffuser endpoints YB1 - 450 a; YB2 = 557 a
Huber of openings OPEN = 36
Spacing between risers/openings SPAC = 3.05 a
'.' Port/Nozzle dianeter D0 - 0.101 n
Equivalent slot width B0 = 0.0026 a
Total area of openings AO - 0.0080 a42
gm Discharge velocity U0 - 0.75 als
Total discharge flowrate ¢0 = 0.219 t"3/s
Discharge port height H0 - 0.6 a
Nozzle arrangement BETYPE = staged
AMO' Diffuser alignment angle GAMMA = 90 deg
Vertical discharge angle THETA = 20 deg
Horizontal discharge angle SIGMA a 270 deg
smq Relative orientation angle BETA = 0 deg
Discharge temperature (freshwater) - 22 degC
Corresponding density RHOO = 997.7714 kg/143
pmDensity difference DRRO = 20.2285 kg/l"3
Buoyant acceleration GPO - .1949 042
Discharge concentration CO = 20 PPT-SAL-DEFICIT
Surface heat exchange coeff. KS - 0 a/s
tun Coefficient of decay KD - 0 /s
FLUX VARIABLES PER UNIT DIFFUSER LENGTH:
mim+ Discharge (volute flux) q0 - 0.002047 1142/s
Motentut flux 10 - 0.001554 243/s42
Buoyancy flux j0 - 0.000399 a43/643
DISCHARGE/ENVIRONMENT LENGTH SCALES :
lq 0.00 lt= 0.27 1M= 0.28 a
la' = 99999.0 n 1b' = 99999.0 t la = 99999.0 a
p'" (These refer to the actual discharge/environsent length scales.)

RIM
NON -DIMENSIONAL PARAMETERS:
Slot Fronde amber FRO = 33.12
Port/nozzle Fronde number FRDO = 5.41
Velocity ratio R - 10.12
MIXING ZONE 1 TOXIC DILUTION ZONE / AREA OF INTEREST PARAMETERS:
Toxic discharge no
Water quality standard specified z yes
Water quality standard CSTD = • 1 PPT-SAL-DEFICIT
Regulatory nixing zone = no
Region of interest - 1000.00 a downstream
************t*t***tttata*att**t******t****a*t***tm**a*t****t***t***ttt*****
HYDRODYNAMIC CLASSIFICATION:
* *
FLOW CLASS = MU6 I
* *
This floe configuration applies to a layer corresponding to the full water
depth at the discharge site.
Applicable layer depth = water depth z 1.83 a
Fon *****tt****tMt********t*******t******tt*******tt************tt*****UM!**
arFas
MIXING ZONE EVALUATION (hydrodynamic and regulatory summary):
I-Y-Z Coordinate system:
Origin is located at the bottom below the port center:
503.50 a frog the left bank/shore.
Ruder of display steps NSTEP r 5 per nodule.
NEAR -FIELD REGION (NFR) CONDITIONS :
Note: The NFR is the zone of strong initial ailing. It has no regulatory
implication. However, this inforaation lay be useful for the discharge
designer because the ailing in the NFR is usually sensitive to the
discharge design conditions.
Pollutant concentration at edge of NFR r .2885 PPT-SAL-DEFICIT
Dilution at edge of NFR - 69.3
NFR Location: x = 9.15 a
(centerline coordinates) y = -8.07 n
z = 1.83 a
NFR pluse dimensions: half -width = 55.31 a
thickness = 1.83 n
Buoyancy assessaent:
The effluent density is less than the surrounding ambient water
density at the discharge level.
Therefore, the effluent is POSITIVELY BUOYANT and will tend to rise towards
the surface.
Near -field instability behavior:
The diffuser flow will experience instabilities with full vertical ailing
in the near -field.
There nay be beathic impact of high pollutant concentrations.
FAR -FIELD MIXING SUMMARY:
Plume becomes vertically fully nixed WITHIN NEAR -FIELD at .00 s
downstreas, but RE -STRATIFIES LATER and is not nixed in the far -field.
***********t************ TOXIC DILUTION ZONE SUMMARY m*t***a*ati******t**t*
No TDZ was specified for this simulation.

tttttt***tt*t*t*****tt REGULATORYMIXING ZONE SUMMARY *tttttt***********tit*!
No RKZ has been specified.
However:
The ambient water quality standard was encountered at the following
plume position:
Water quality standard - 1 PPT-SAL-DEFICIT
Corresponding dilution - 20
Plume location: x = 1.79 m
(centerline coordinates) y II 41.41 m
raw z= .66a
Plume dimensions: half -width = 10.89 m
thickness = .39 m
tttttt*****'**'tttttt FINAL DESIGN ADVICE AND COMMENTS ******************t*t*
`i' CORMIB2 uses the TKO -DIMENSIONAL SLOT DIFFUSER CONCEPT to represent
the actual three-dimensional diffuser geometry. Thus, it approximates
the details of the merging process of the individual jets from each
port/nozzle.
In the present design, the spacing between adjacent ports/nozzles
(or riser assemblies) is of the order of, or less than, the local
um, water depth so that the slot diffuser approximation holds well.
Nevertheless, if this is a final design, the user is advised to use a
final CORKIB1 (single port discharge) analysis, with discharge data
for an individual diffuser jet/plume, in order to compare to
the present near -field prediction.
REMINDER: The user must take note that HYDRODYNAMIC MODELING by any known
�.► technique is NOT AN EXACT SCIENCE.
Extensive comparison. with field and laboratory data has shown that the
CORKIB predictions on dilutions and concentrations (with associated
plume geometries) are reliable for the majority of cases and are accurate
rao
to within about +-50% (standard deviation) .
As a further safeguard, CORKIB will not give predictions whenever it judges
the design configuration as highly complex and uncertain for prediction.
ittttttttiti**********t*tttti****t*it*t*t*tit*tttt***tttttt*tttttt*tttitttt*t
DESIGN CASE: 5 KGB STAGED 107 m 36 0.101 a PORTS
FILE NAME: DFUN2S
Subsystem CORKIB2: Submerged Kultiport Diffuser Discharges
END OF SESSION/ITERATION: 06/12195--12:14:24
%BBB%BBB%BBB%%%BBB%B%B%BBI%%BBB%B%%BB%B%%BB%B%BBB%BBI%%%BB%BB%%BBB%BIB%%BBBB%
IOW

CORKED PREDICTION FILE:
22222222222222222222222222222222222222222222222222222222222222222222222222222
CORNELL NIXING ZONE EXPERT SYSTEM
PE, . Subsystei CORMII2: Subsystei version:
Subierged Multiport Diffuser Discharges CORMII v:3.10 June 1995
IMP
CASE DESCRIPTION
Site nacre/label:
Design case:
FILE NAME:
Tine of Fortran run:
CAMP"LEJEUNE
5"MGD"STAGED"107"1436"0.101"1"PORTS
coraixlsiiIDFUN25 . cx2
06/11/95--14:18:38
ENVIRONMENT PARAMETERS (ietric units)
Unbounded section
HA = 1.83 HD = 1.83
UA = .075 F - .040 USTAR = .5303E-02
UI = 2.000 UISTAR= .2198E-02
Unifora density enviroaient
STRCND= U RHOAM = 1018.0000
DIFFUSER DISCHARGE PARAMETERS (ietric units)
Diffuser type: DITYPE= staged perpendicular
BANK = LEFT DISTB = 503.50 YB1 = 450.00 YB2 = 557.00
LD = 107.00 ROPER = 36 SPAC = 3.06
D0 = .101 A0 = .008 H0 = .60
Nozzle/port arrangement: staged
GAMMA = 90.00 THETA = 20.00 SIGMA = 270.00 BETA = .00
U0 - .759 QO r .219 = .2190E+00
RH00 = 997.7714 DRH00 .2023E+02 GPO = .1949E+00
imp CO = .2000E+02 CUNITS= PPT-SAL-DEFICIT
IPOLL = 1 KS = .0000E+00 ID = .0000E+00
FLUI VARIABLES - PER UNIT DIFFUSER LENGTH (aetric units)
q0 = .2047E-02 10 = .1554E-02 j0 = .3989E-03 SIGNJO= 1.0
Associated 2-d length scales (aeters)
1Q=B = .003 111 = .29 la = .28
lip = 99999.00 lbp = 99999.00 la = 99999.00
FLUX VARIABLES - ENTIRE DIFFUSER (metric units)
Q0 = .2190E+00 MO = .1663E+00 JO = .4268E-01
Associated 3-d length scales (aeters)
LQ = .54 LM = 1.26 La = 5.44 Lb = 101.16
Lip = 99999.00 Lbp = 99999.00
NON -DIMENSIONAL PARAMETERS
FRO = 33.12 FRDO = 5.41 R = 10.12
(slot) (port/nozzle)
FLOW CLASSIFICATION
222222222222222222222222222222222222222222
2 Flow class (CORMIX2) = MI6 2
2 Applicable layer depth HS = 1.83 2
222222222222222222222222222222222222222222

mar
1.6
MIXING ZONE l TOXIC DILUTION l REGION OF INTEREST PARAMETERS
CO = .2000E+.02 CUBITS= PPT-SAL-DEFICIT
NTOX r 0
NSTD r 1 CSTD = .1000E+01
REM = 0
'INT = 1000.00 XMAx = 1000.00
X-Y-Z COORDINATE SYSTEM:
ORIGIN is located at the bottom and the diffuser aid -point:
503.50 i from the LEFT banklsbore.
If -axis points downstream, Y-axis points to left, Z-axis points upward.
NSW = 5 display intervals per module
Iso BEGIN K0D202: DISCHARGE MODULE (STAGED DIFFUSER)
NMI
01111
Due to complex near -field motions: EQUIVALENT SLOT DIFFUSER (2-D) GEOMETRY
Profile definitions:
BV r Gaussian lle (371) half -width, in vertical plane normal to trajectory
BH = Gaussian lle (371) half -width is horizontal plane aortal to trajectory
S = hydrodynamic centerline dilution
C = centerline concentration (includes reaction effects, if any)
X Y Z S C BV BH
.00 53.50 .60 1.0 .200E+02 .05 .05 ,
END OF K0D202: DISCHARGE MODULE (STAGED DIFFUSER)
BEGIN MOD275: STAGED PERPENDICULAR DIFFUSER IN STRONG CURRENT
Because of the strong ambient current the diffuser pluae of this crossflowing
discharge gets RAPIDLY DEFLECTED.
A near -field zone is formed that is VERTICALLY FULLY MIXED over the entire
layer depth. Full mixing is achieved at a downstream distance of about
five (5) layer depths.
Profile definitions:
BV = layer depth (vertically mixed)
BH = top -hat half -width, measured horizontally in y-direction
S = hydrodynamic average (bulk) dilution
C = average (bulk) concentration (includes reaction effects, if any)
1 Y Z S C BV BH
.00 53.50 .60 1.0 .199E+02 .05 .05
** WATER QUALITY STANDARD OR CCC HAS BEEN FOUND
The pollutant concentration in the plume falls below water quality standard
►�+ or CCC value of .100E+01 is the current prediction interval.
This is the spatial extent of concentrations exceeding the water quality
standard or CCC value.
1.83 41.18 .66 31.6 .634E+00 .41 11.10
3.66 28.87 .73 44.2 .452E+00 .76 22.15
5.49 16.55 .79 53.9 .371E+00 1.12 33.21
7.32 4.24 .85 62.1 .322E+00 1.47 44.26
A"" 9.15 -8.08 .92 69.3 , 289E+00 1.83 55.31
Cumulative travel time = 122. sec

POP
ANN
POI
i.a
iaaNO
PIM
END OF M0D275: STAGED PERPENDICULAR DIFFUSER IN STRONG CURRENT
** End of NEAR -FIELD REGION (NFR) **
BEGIN MOD241: BUOYANT AMBIENT SPREADING
Profile definitions:
BV = top -hat thickness, measured vertically
BH = top -bat half -width, measured horizontally in y-direction
ZU = upper plume boundary (Z-coordinate)
ZL = lower plume boundary (Z-coordinate)
S = hydrodynamic average (bulk) dilution
C = average (bulk) concentration (includes reaction effects, if any)
Plume Stage 1 (not bank attached):
I Y Z S C BV BB ZU ZL
9.15 -8.08 1.83 69.3 .289E+00 1.83 55.31 1.83 .00
207.32 -8.08 1.83 92.6 .216E+00 .89 151.23 1.83 .94
405.49 -8.08 1.83 110.6 .181E+00 .74 219.39 1.83 1.09
603.66 -8.08 1.83 132.5 .151E+00 .70 276.43 1.83 1.13
801.83 -8.08 1.83 160.4 .125E+00 .72 327.05 1.83 1.11
1000.00 -8.08 1.83 195.5 .102E+00 .76 373.46 1.83 1.07
Cumulative travel time = 13333. sec
Simulation limit based an maximum specified distance = 1000.00 i.
This is the REGION OF INTEREST limitation.
END OF MOD241: BUOYANT AMBIENT SPREADING
CORMII2: Submerged Multipart Diffuser Discharges End of Prediction File
22222222222222222222222222222222222222222222222222222222222222222222222222222

l 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 11
CA P'-LEJEUNE
5A Y1GO \STAGE ^L. O AmA,a6AO,, i Oi Am' POPTS
0
NM
•
0
0
COPML 2 Prediction
File: sin .OFUN26 .cx2
I.
I.f..:7;ii.
fii
li
•
:•
I.
0
Ji torticr = 313.221
200 400 600
Side LJi eu
800
1
1000
X (m) ---i.
.0114

i I 1 I I 1• $ 1 1 11 1 1 1 1
CA: P +••.LEJ EUNE
COPMIX2 Prediction
5"11GD"STAOEO^ . 07 ^rn^36^0n i 0l ^m^POPT0 File: sir=..QFUN2S . c =::2
as. • A• • 1y'• •iAirA Y Y
r
LO !
r --� 1=, -
0
!1
I -
r
r 11 •M
iM3 i
~~ fiiiiiiiiiiiiiii$11111111111iiiiii11$111111111P111111P111111Piiiiiiiii1i1iiiiiiii11111111111111111iiiiiiiiiiii•ii1111111
r�-
a
:l �t t pan = 0.63
1 I f 1
200 400 600 800 • 1000
Plan Uieu

1 1 1 1 1 1 1 1 1 1 1 I 1 1 1 1 1 1 1
C 'MP --.-LE EUNE
6' MGD^CTAD D^1 D7'\m'D 'D. 1 Di m"PDPTS
(PINT-SfL-DEFICIT) x
•
•
•
•
•
:.............
COPMIX2 Prediction.
File: si m =..DFUN25 . c 2
1J. 0
1.5 3.0
4.5 6.0
Concentration vs Dounst r- earn Distance.

VII. RUN DFUN 26

a£ IxfIi ,tilfixxxxxxxxxlmmulaxxxxxxxxxxxxxxxxxxxxxxxxxxxxxxxxix
011
CORMIX: CORNELL MIXING ZONE EXPERT SYSTEM
£ORRIX v, 3,10 June 1995
SITE HAKE/LABEL: CAMP LEJEUNE
set DESIGN CASE: 15 MGD STAGED 107 n 36 0.101 a PORTS
FILE NAME: • DFUN26
Using subsystea CORHIX2: Subaerged Multipart Diffuser Discharges
Start of session: 06/11/95--14:25:31
r
atttttttttattttt*ttta*ttttttta*tttattttt*ttattatttttt:ttttatattttt:ttattttttt
SUMMARY OF INPUT DATA:
AMBIENT PARAMETERS:
Cross-section = unbounded
• Average depth HA - 1.83 a
Depth at discharge HD - 1.83 a
Aabient velocity - UA - 0.075 a/s
Darcy-Neisbach friction factor F - 0.04
hind .velocity UN - 2 a/s
'"" Stratification Type STRCND = U
Surface density RHOAS = 1018 kg/a"3
Batton density RHOAB 1018 kg/a"3
DISCHARGE PARAMETERS: Subaerged Multipart Diffuser Discharge
Diffuser type DITYPE = staged perpendicular
Diffuser length LD = 107 a
Nearest bank = left
Diffuser endpoints YB1 - 450 n; YB2 = 557 a
Number of openings ROPER = 36
"" Spacing between risers/openings SPAC = 3.05 a
Port/Nozzle diaaeter D0 - 0.101 n
Equivalent slot width B0 - 0.0026 a
Total area of openings A0 - 0.0080 1"2
Discharge velocity U0 - 2.27 a/s
Total discharge flovrate gO - 0.657 a"3/s
Discharge port height H0 = 0.6 a
1114 Nozzle arrangement BETYPE = staged
Diffuser alignment angle GAMMA = 90 deg
Vertical discharge angle THETA = 20 deg
Horizontal discharge angle SIGMA = 270 deg
Relative orientation angle BETA = 0 deg
Discharge teaperature (freshwater) - 22 degC
Corresponding density RH40 = 997.7714 kg/aA3
Density difference DUO = 20.2285 kg/n"3
Buoyant acceleration GPO - .1949 n/s"2
Discharge concentration CO - 20 PPP -SAL -DEFICIT
mow Surface heat exchange coeff. KS - 0 a/s
Coefficient of decay KD - 0 /s
n.n FLUX VARIABLES PER UNIT DIFFUSER LENGTH:
Discharge (volune flux) q0 - 0.006140 1"21s
Mantua flux a0 - 0.013986 n"3/s"2
Buoyancy flux j0 - 0.001196 a"3/s"3
DISCHARGE/ENVIRONMENT LENGTH SCALES :
lq = 0.00 m la = 2.48 a 1K = 1.24 a
le' . 99999.0 a lb' = 99999.0 n la = 99999.0 n
(These refer to the actual discharge/environment length scales.)

NON -DIMENSIONAL PARAMETERS:
so Slot Froude number FRO - 99.37
Port/nozzle Fronde nuaber FRDO = 16.23
Velocity ratio R - 30.37
MIXING ZONE / TOXIC DILUTION ZONE / AREA OF INTEREST PARAMETERS:
Toxic discharge = no
Water quality standard specified = yes
Water quality standard CSTD = 1 PPT-SAL-DEFICIT
Regulatory mixing zone = no
Region of interest = 1000.00 m downstreaa
Mttttttt:ttttttttt:ttttttttttttttttttttttttttttttttt}ttttttt:ttttt:tttttttt
HYDRODYNAMIC CLASSIFICATION:
+.. FLOW CLASS = MU6 I
t t
This flow configuration applies to a layer corresponding to the full Water
depth at the discharge site.
Applicable layer depth = water depth = 1.83 m
tttttttttttttttttttttMtttttttttttttt:tttttttttttttttttttt:tt+tttttrntttttt
MIXING ZONE EVALUATION (hydrodynaaic and regulatory summary):
X-Y-Z Coordinate systea:
Origin is located at the bottom below the port center:
503.50 a frog the left bank/shore.
Number of display steps NSTEP = 5 per nodule.
NEAR -FIELD REGION (NFR) CONDITIONS
Note: The NFR is the zone of strong initial nixing. It has no regulatory
implication. However, this inforaation may be useful for the discharge
designer because the airing in the NFR is usually sensitive to the
discharge design conditions.
Pollutant concentration at edge of NFR = .7050 PPT-SAL-DEFICIT
Dilution at edge of NFR - 28.3
NFR Location: x = 9.15 a
(centerline coordinates) y = -72.68 a
z = 1.83 a
NFR plume dimensions: half -width = 67.90 a
thickness = 1.83 n
Buoyancy assessaent:
The effluent density is less than the surrounding anbient water
density at the discharge level.
Therefore, the effluent is POSITIVELY BUOYANT and will tend to rise towards
the surface.
Near -field instability behavior:
The diffuser flow will experience instabilities with full vertical mixing
in the near -field.
There nay be benthic impact of high pollutant concentrations.
FAR -FIELD MIXING SUMMARY:
Pluae becomes vertically fully nixed WITHIN NEAR -FIELD at .00 n
downstream, but RE -STRATIFIES LATER and is not nixed in the far -field.
tttttttttttt******tttttt TOXIC DILUTION ZONE SUMMARY tttttt"ttttttttttt+tttt
No TDZ was specified for this simulation.

**t***************t*t* REGULATORY MIXING ZONE SUMMARY t*tt******t*t**********
No RMI has been specified.
However:
The ambient water quality standard was encountered at the following
plume position:.
Water quality standard - 1 PPT-SAL-DEFICIT
Corresponding dilution 20
Plume location: x = 4.54 m
(centerline coordinates) y = -9.14 a
z= .75a
Plume dimensions: half -width = 33.73 a
thickness . .93 a
*******************t* FINAL DESIGN ADVICE AND COMMENTS t******t****tt*i******
COMM uses the TWO-DIMENSIONAL SLOT DIFFUSER CONCEPT to represent
the actual three-dimensional diffuser geometry. Thus, it approximates
the details of the merging process of the individual jets from each
�.. port/nozzle.
In the present design, the spacing between adjacent ports/nozzles
(or riser assemblies) is of the order of, or less than, the local
water depth so that the slot diffuser approximation bolds well.
Nevertheless, if this is a final design, the user is advised to use a
final COMM (single port discharge) analysis, with discharge data
for an individual diffuser jet/plume, in order to compare to
the present near -field prediction.
REMINDER: The user must take note that HYDRODYNAMIC MODELING by any known
110 technique is NOT AN gIACT SCIENCE.
Extensive comparison with field and laboratory data has shown that the
CORMIM predictions on dilutions and concentrations (with associated
plume geometries) are reliable for the majority of cases and are accurate
to within about +-501 (standard deviation) .
As a further safeguard, CORM will not give predictions whenever it judges
the design configuration as highly complex and uncertain for prediction.
ask *tttt*t*t***********t*****t*********m tart:*t*tt***tt*ttt*tttt*t*tttttt*tt
DESIGN CASE: 15 MGD STAGED 107 m 36 0.101 m PORTS
FILE NAME: DFUN26
Subsystem CORMIX2: Submerged Hultiport Diffuser Discharges
END OF SESSION/ITERATION: 06/12/95--12:20:04
II%IIIIXXIXXXXXXXXIxxgXXXx!XIIIIxxIXXIIIIIIIXIIIIIIIXIII III IIXXIXIIIyXIIIXIIB
Oft
IMP
a■a
ar►

OM
CORHII2 PREDICTION FILE:
22222222222222222222222222222222222222222222222222222222222222222222222222222
CORNELL NIXING ZONE EXPERT SYSTEM
Subsystem CORHII2: Subsystem version:
Submerged Hultiport Diffuser Discharges CORHII v.3.10 June 1995
CASE DESCRIPTION
Site name/label:
Design case:
FILE NAME:
Time of Fortran run:
CAHP"LEJEUNE
15"MGD"STAGED"107"m" 36"0.101 "m"PORTS
cormixlsialDFUN26 . cx2
06/11/95--14:29:42
ENVIRONMENT PARAMETERS (metric units)
Unbounded section
HA = 1.83 HD = 1.83
UA = .075 F - .040 USTAR = .5303E-02
UN a 2.000 UWSTAR= .2198E-02
Uniform density environment
STRCND= U RROAH = 1018.0000
DIFFUSER DISCHARGE PARAMETERS (metric units)
Diffuser type; BITYPB= staged perpendicular
BANK = LEFT DISTB s 503.50 YB1 s 450.00 YB2 = 557.00
LD - 107.00 NOPEN _ 36 SPAC = 3.06
D0 = .101 AO = .008 H0 - .60
Nozzle/port arrangement: staged
GAMMA = 90.00 THETA = 20.00 SIGMA = 270.00 BETA = .00
U0 - 2.278 Q0 = .657 = .6570E+00
air RH00 = 997.7714 DRHOO s .2023E+02 GPO = .1949E+00
CO = .2000E+02 CUNITS= PPT-SAL-DEFICIT
IPOLL = 1 KS = .0000E+00 KD = .0000E+00
FLUI VARIABLES - PER UNIT DIFFUSER LENGTH (metric units)
q0 = .6140E-02 10 = .1399E-01 j0 = .1197E-02 SIGNJO= 1.0
Associated 2-d length scales (neters)
�• 1Q=B = .0031K = 1.24 in = 2.49
lap = 99999.00 lbp = 99999.00 la = 99999.00
osit
poi
FLU VARIABLES - ENTIRE DIFFUSER (metric units)
Q0 = .6570E+00 HO = .1497E+01 JO = .1280E+00
Associated 3-d length scales (meters)
LQ - .54 LM - 3.78 La - 16.31 Lb = 303.47
Lip = 99999.00 Lbp = 99999.00
NON -DIMENSIONAL PARAMETERS
FRO = 99.37 FRDO = 16.23 R = 30.37
(slot) (port/nozzle)
FLOW CLASSIFICATION
222222222222222222222222222222222222222222
2 Flov class (CORHII2) = HU6 2
2 Applicable layer depth NS = 1.83 2
222222222222222222222222222222222222222222

Oa
MIXING ZONE 1 TOXIC DILUTION 1 REGION OF INTEREST PARAMETERS
CO = .2000E+02 CURITS= PPT-SAL-DEFICIT
NTOI=0
NSTD = 1 CSTD = .1000E+01
REGMZ = 0
XINT = 1000.00 IMAI = 1000.00
I-Y-Z COORDINATE SYSTEM:
ORIGIN is located at the bottoa and the diffuser aid -point:
503.50 a frog the LEFT bank/shore.
I -axis points downstreaa, Y-axiS points to left{ Z-axis points upward.
NSTEP = 5 display intervals per nodule
BEGIN M0D202: DISCHARGE MODULE (STAGED DIFFUSER)
Due to cotplex near -field Rations: EQUIVALENT SLOT DIFFUSER (2-D) GEOMETRY
Profile definitions:
BV = Gaussian lie (31%) half -width, in vertical plane norual to trajectory .
BH = Gaussian Ile (37%) half -width in horizontal plane norsal to trajectory
S = hydrodynaaic centerline dilution
C = centerline concentration (includes reaction effects, if any)
X Y Z S C BV BH
.00 53.50 .60 1.0 .200E+02 .05 .05
END OF MOD202: DISCHARGE MODULE (STAGED DIFFUSER)
BEGIN MOD275: STAGED PERPENDICULAR DIFFUSER IN STRONG CURRENT
Because of the strong asbient current the diffuser plute of this crossflowing
discharge gets RAPIDLY DEFLECTED.
A near -field zone is forted that is VERTICALLY FULLY MIXED over the entire
layer depth. Full sizing is achieved at a downstreaa distance of about
five (5) layer depths.
Profile definitions:
BV = layer depth (vertically aired)
BH = top -hat half -width, seasured horizontally in y-direction
S = hydrodynaaic average (bulk) dilution
C = average (bulk) concentration (includes reaction effects, if any)
I Y Z S C BV BH
.00 53.50 .60 1.0 .200E+02 .05 .05
1.83 28.26 .66 13.2 .151E+01 .41 13.62
3.66 3.02 .73 18.3 .109E+01 .76 27.19
* * WATER QUALITY STANDARD OR CCC HAS BEEN FOUND **
The pollutant concentration in the pluse falls below water quality standard
or CCC value of .100E+01 in the current prediction interval.
This is the spatial extent of concentrations exceeding the water quality
standard or CCC value.
""'' 5.49 -22.21 .19 22.2 .901E+00 1.12 40.76
7.32 -47.45 .85 25.5 .185E+00 1.47 54.33
9.15 -12.69 .92 28.4 .705E+00 1.83 67.90
04 Cuaulative travel tile = 122. sec
END OF MOD275: STAGED PERPENDICULAR DIFFUSER IN STRONG CURRENT
** End of NEAR -FIELD REGION (NFR) **

BEGIN K0D241: BUOYANT ABBIENT SPREADING
Profile definitions:
BV : top -hat thickness, measured vertically.
BH.: top -hat half -width, measured horizontally in y-direction
OM` ZU : upper plume boundary (Z-coordinate)
EL = lover plume boundary (Z-coordinate)
S = hydrodynamic average (bulk) dilution
mat C : average (bulk) concentration (includes reaction effects, if any)
Plume Stage 1 (not bank attached):
01.0 8. Y Z S C BV BH ZU EL
9.15 -72.69 1.83 28.4 .705E+00 1.83 67.90 1.83 .00
207.32 -72.69 1.83 38.5 .520E+00 .80 209.50 1.83 1.03
405.49 -72.69 1.83 44.4 .451E+00 .64 305.92 1.83 1.19
603.66 -72.69 1.83 50.4 .397E+00 .57 384.87 1.83 1.26
801.83 -72.69 1.83 57.4 .348E+00 .55 453.76 1.83 1.28
1000.00 -72.69 1.83 65.7 .304E+00 .56 516.07 1.83 1.27
alo Collative travel tine r 13333. sec
Simulation licit based on mint specified distance : 1000.00 1.
This is the REGION OF INTEREST limitation.
END OF 80D241: BUOYANT AMBIENT SPREADING
CORHIZ2: Submerged 8ultiport Diffuser Discharges End of Prediction File
22222222222222222222222222222222222222222222222222222222222222222222222222222

1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1
CAMP LEJEUNE
15' MGOASTAOEOM 0 AwN36 \O■ 1 O1 "m"POP T S
co-
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0 200 400 600 800 1000
X On)
Side Uieu
Distortion = 317.121

1
1 l I 1 I 1 1 I I I I 1 l 1 1 1
CAMP-\LEJEUNE
COPML 2 Prediction
15^M OOAOTAOEO O7 Arnr\O6^O, 1 OVrn' POPTS File: sir =•.OFUN26 , c =.2
r
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400
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600
800
1000
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I 1 I I 1 1 I 1 1 1 I I l 1 1 1 1 I I
CFMP LEjEUNE
COPNIX2 Prediction
15"MGDACTAOED'\107 `t A36A0. 10Vrnn' POPTS File: si m =.DFUN26 . c-
0
D
(PPT-Sf1L-DEFICIT) x
1)
0
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0
co—
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1.5 3.0 4.5 15.0 7.5
r 1 1 ' 1
Concentration vs Downstream Distance
9, 0
X (m) --4

ViII. RUN DFUN27
n

Awn
CORM: CORNELL MIXING ZONE EIPERT SYSTEM
CORKII v.3.10 June 1995
"" SITE NAME/LABEL: CAMP LEJEURE
ORIGINAL design case: 5 KGD STAGED 107 a 36 PORTS 0.1011 D0.101
ORIGINAL file nate: DFUN25
n.q Start of aain session: 06/11/95--13:44:18
DESIGN ITERATION nuaber:
NEW DESIGN CASE:
NEW FILE NAME:
Using subsystea CORMII2:
Start of iteration session:
3
15 MGD STAGED 101 a 36 0.101 PORTS Tbt 45
dfun27
Subaerged Kultiport Diffuser Discharges
06111/95--14:39:13
tit!thrntilt*t****t****t*t*********:**!*t**!t!*!!!!!! !!t!******Mt*!***:**:
SUMMARY OF INPUT DATA:
AMBIENT PARAMETERS:
Cross-section
Average depth
Depth at discharge
me" Aabient velocity
Darcy-Weisbach friction factor
Wind velocity
Stratification Type
Surface density
Bottaa density
HA
HD
DA.
F
UV
= unbounded
• 1.83 a
• 1.83 fl
• 0.075 a1s
• 0.04
2m/s
STRCND = U
RHOAS
RHOAB =
1018 kgla"3
1018 kg/103
DISCHARGE PARAMETERS: Subaerged Kultiport Diffuser Discharge
Diffuser type DITYPE s staged perpendicular
Diffuser length LD = 107 a
Awl Nearest bank s left
Diffuser endpoints YB1 - 450 n, YB2 = 551 a
Huber of openings ROPER
SIP Spacing between risers/openings SPAC
Port/Nozzle diateter
Equivalent slot width
Total area of openings
Discharge velocity
Total discharge flovrate
Discharge port height
sum Nozzle arrangeaent
Diffuser alignaent angle
Vertical discharge angle
Horizontal discharge angle
xam
Relative orientation angle
36
3.05 a
D0 - 0.101 a
B0 - 0.0026 a
A0 - 0.0080 a"2
U0 - 2.27 a/s
Q0 - 0.657 a"3/s
H0 - 0.6
BETYPE = staged
GAMMA
THETA
SIGMA
BETA
Discharge teaperature (freshwater)
Corresponding density
Density difference
Buoyant acceleration
Discharge concentration
__ Surface heat exchange coeff.
Coefficient of decay
PIM
RHOO
DRHO
GPO
CO
KS
KD
90 deg
45 deg
270 deg
0 deg
22 degC
• 997.7714 kgla"3
• 20.2285 kg/103
• .1949 1/s"2
20 PPT-SAL-DEFICIT
0 n/s
0 /s
FLUX VARIABLES PER UNIT DIFFUSER LENGTH:
Discharge (volute flux) q0 -
Komentua flux 110 Buoyancy flux j0 =
0.006140 11"2/s
0.013986 103/s"2
0.001196 1"3/8"3

DISCHARGE/ENVIRONMENT LENGTH SCALES :
lq = 0.00 a la = 2.48 a iM = 1.24 a
la' = 99999.0 a lb' = 99999.0 m la = 99999.0 a
(These refer to the actual discharge/environment length scales.)
NON -DIMENSIONAL PARAMETERS:
+� Slot Froude number FRO = 99.37
Port/nozzle Fronde number FRDO = 16.23
Velocity ratio R - 30.37
MIXING ZONE / TOXIC DILUTION ZONE / AREA OF INTEREST PARAMETERS:
Toxic discharge = DO
Water quality standard specified = yes
Water quality standard CSTD = 1 PPT-SAL-DEFICIT
Regulatory mixing zone = no
Region of interest - 1,, ,, ,, .00 a downstream
:f!lttattattttttattttaataatatltrtttlttaatta:ttttttt!lattttaltattttatiMflt:tilt
HYDRODYNAMIC CLASSIFICATION:
! r
I FLOW CLASS = MU6 I
* . *
This flow configuration applies to a layer corresponding to the full water
depth at the discharge site.
am Applicable layer depth = water depth = 1.83 a
1111.4
MIMI
SIP
tiltattt IMMtttt:atilt:tttttttt::tact!!!!!!!titMtttttltttttttttalttlrrlrlt
MIXING ZONE EVALUATION (hydrodynamic and regulatory summary):
X-Y-Z Coordinate system:
Origin is located at the bottom below the port center:
503.50 a from the left bank/shore.
Number of display steps NSTEP = 5 per module.
NEAR -FIELD REGION (NFR) CONDITIONS :
Note: The NFR is the zone of strong initial mixing. It has no regulatory
implication. However, this information may be useful for the discharge
designer because the mixing in the NFR is usually sensitive to the
discharge design conditions.
Pollutant concentration at edge of NFR = .7050 PPT-SAL-DEFICIT
Dilution at edge of NFR = 28.3
NFR Location: x = 9.15 a
(centerline coordinates) y = -72.68 a
z= 1.83m
NFR plume dimensions: half -width = 67.90 a
thickness = 1.83 a
Buoyancy assessment:
The effluent density is less than the surrounding ambient water
density at the discharge level.
Therefore, the effluent is POSITIVELY BUOYANT and will tend to rise towards
the surface.
Near -field instability behavior:
The diffuser flow will experience instabilities with full vertical mixing
in the near -field.
There may be benthic impact of high pollutant concentrations.
FAR -FIELD MIXING SUMMARY:
— Plume becomes vertically fully nixed WITHIN NEAR -FIELD at .00 a
downstream, but RE -STRATIFIES LATER and is not mixed in the far -field.
************************ TOXIC DILUTION ZONE SUMMARY !!!*!!!!!!!!!!$!!!!!!!!!
No TDZ vas specified for this simulation.

********************** REGULATORY MIXING BONE SUMMARY *********************"
No RKZ has been specified.
ramHowever:
The aabient water quality standard was encountered at the following
pluae position:
Water quality standard s 1 PPT-SAL-DEFICIT
41" Corresponding dilution - 20
Plume location: x r 4.54 a
(centerline coordinates) y = -9.14 a
z.75a
Plate digensions: half -width = 33.73 a
thickness z .93 a
********************* FINAL DESIGN ADVICE AND COMMENTS **********************
CORMIX2 uses the TWO-DIMENSIONAL SLOT DIFFUSER CONCEPT to represent
the actual three-dimensional diffuser geometry. Thus, it approxigates
the details of the gerging process of the individual jets frou each
port/nozzle. •
In the present design, the spacing between adjacent ports/nozzles
(or riser assemblies) is of the order of, or less than, the local
water depth so that the slot diffuser approximation holds well.
• Nevertheless, if this is a final design, the user is advised to use a
final CORMIXI (single port discharge) analysis, with discharge data
for an individual diffuser jetlpluae, in order to compare to
the present near -field prediction.
REMINDER: The user gust take note that HYDRODYNAMIC KODELING by any known
►•: technique is NOT AN EXACT SCIENCE.
Extensive comparison with field and laboratory data has shown that the
CORM predictions on dilutions and concentrations (with associated
plum geogetries) are reliable for the gajority of cases and are accurate
to within about +-50I (standard deviation).
As a further safeguard, CORMIX will not give predictions whenever it judges
the design configuration as highly cogplex and uncertain for prediction.
*******:*********:***********************************************************
DESIGN CASE: 15 KGD STAGED 107 a 36 0.101 PORTS Tht 45
FILE NAME: dfun27
Subsystem CORKIX2: Submerged Multiport Diffuser Discharges
END OF SESSION/ITERATION: 06/11/95--14:47:46
XXXIIIXXXXXXXXXXXXXXXXXXIXXXYXXXXXXXXXXXXXXIIXXXXIXXXXXXXXXXXXIXXXIXXXXXXXXXX
RIM

oat
CORKII2 PREDICTION FILE:
22222222222222222222222222222222222222222222222222222222222222222222222222222
CORNELL KIXING ZONE EXPERT SYSTEM
Subsystea CORMII2: Subsystel version:
Subaerged Multipart Diffuser Discharges CORKII v.3.10 June 1995
CASE DESCRIPTION
Site naae/label:
Design case:
FILE NAME:
Tim of Fortran run:
CAKP"LEJEUNE
15 "KGD"STAGED"107"a"36 "0.101 "PORTS"Tht"4
coraixlsialdfun27 . cx2
06/11/95--14:42:48
ENVIRONMENT PARAMETERS (aetric units)
"" Unbounded section
HA - 1.83 HD = 1.83
UA = .075 F = .040 USTAR = .5303E-02
UN = 2.000 UNSTAR= .2198E-02
Unifor& density enviranaent
STRCRD= U RHOAK = 1018.0000
+®a
DIFFUSER DISCHARGE PARAMETERS (aetric units)
Diffuser type: DITYPE= staged perpendicular
BANK = LEFT DISTB = 503.50 YB1
LD - 107.00 ROPEN = 36 SPAC =
D0 = .101 A0 = .008 H0 =
Nozzle/port arrangeaent: staged
GAMMA = 90.00 THETA = 45.00 SIGMA
U0 = 2.278 Q0 - .657
MOO = 997.7714 DRHOO = .2023E+02 GPO
CO = .2000E+02 CUNITS= PPT-SAL-DEFICIT
450.00 YB2 = 557.00
3.06
.60
• 270.00 BETA = .00
• .6570E+00
.• 1949E+00
IPOLL = 1 KS = .m0E+00 KD = .0000E+00
FLUX VARIABLES - PER UNIT DIFFUSER LENGTH (eetric units)
q0 = .6140E-02 a0 = .1399E-01 j0 = .1197E-02 SIGNJO= 1.0
Associated 2-d length scales (eeters)
1Q=B = .003 1K = 1.24 le - 2.49
lap = 99999.00 lbp = 99999.00 la = 99999.00
FLUX VARIABLES - ENTIRE DIFFUSER (aetric units)
QO = .6570E+00 KO = .1497E+01 JO = .1280E+00
MOa Associated 3-d length scales (*eters)
LQ = .54 LK = 3.78 Le = 16.31 Lb = 303.47
Lip = 99999.00 Lbp = 99999.00
SIM
PER
NON -DIMENSIONAL PARAMETERS
FRO = 99.37 FRDO = 16.23 R = 30.37
(slot) (port/nozzle)
FLOW CLASSIFICATION
222222222222222222222222222222222222222222
2 Flov class (CORHIX2) = HU6 2
2 Applicable layer depth HS = 1.83 2
222222222222222222222222222222222222222222

NIXING ZONE / TOXIC DILUTION / REGION OF INTEREST PARAMETERS
CO = .2', ,, E+02 CUNITS= PPT-SAL-DEFICIT
mum
NTOX = 0
NSTD = 1 CSTD = .1000E+01
REGKZ = 0
XINT = 1000.00 XMAI = 1000.00
X-Y-Z COORDINATE SYSTEM:
pun ORIGIN is located at the bottot and the diffuser aid -point:
503.50 t froa the LEFT bank/shore.
X-axis points downstreaa, Y-axis points to left, Z-axis points upward.
NSTEP = 5 display intervals per nodule
BEGIN KOD202: DISCHARGE NODULE (STAGED DIFFUSER)
Due to complex near -field notions: EQUIVALENT SLOT DIFFUSER (2-D) GEOMETRY
Profile definitions:
BV = Gaussian 1/e (37%) half -width, in vertical plane normal to trajectory
BH = Gaussian lie (37%) half -width in horizontal plane aortal to trajectory
S = hydrodynamic centerline dilution
C = centerline concentration (includes reaction effects, if any)
X Y Z S C BV BH
.00 53.50 .60 1.0 .200E+02 .05 .05
END OF K0D202: DISCHARGE MODULE (STAGED DIFFUSER)
BEGIN KOD275: STAGED PERPENDICULAR DIFFUSER IN STRONG CURRENT
�•, Because of the strong anbient current the diffuser pluae of this crossflowing
discharge gets RAPIDLY DEFLECTED.
A near -field zone is formed that is VERTICALLY FULLY MIXED over the entire
layer depth. Full miring is achieved at a downstream distance of about
five (5) layer depths.
Profile definitions:
BV = layer depth (vertically nixed)
BH = top -hat half -width, neasured horizontally in y-direction
S = hydrodynamic average (bulk) dilution
mai C = average (bulk) concentration (includes reaction effects, if any)
X Y 2 S C BV BB
.00 53.50 .60 1.0 .200E+02 .05 .05
1.83 28.26 .66 13.2 .151E+01 .41 13.62
3.66 3.02 .73 18.3 .109E+01 .76 27.19
** MATER QUALITY STANDARD OR CCC HAS BEEN FOUND "
The pollutant concentration in the plane falls below water quality standard
or CCC value of .100E+01 in the current prediction interval.
This is the spatial extent of concentrations exceeding the water quality
„R standard or CCC value.
5.49 -22.21 .79 22.2 .901E+00 1.12 40.76
7.32 -47.45 .85 25.5 .785E+00 1.47 54.33
9.15 -72.69 .92 28.4 .705E+00 1.83 67,90
Cunulative travel tiae = 122. sec
NMI
END OF K0D275: STAGED PERPENDICULAR DIFFUSER IN STRONG CURRENT
** End of NEAR -FIELD REGION (NFR) **

BEGIN N0D241: BUOYANT ANBIENT SPREADING
Profile definitions:
BV = top -hat thickness, aeasured vertically
BH r top -hat half -Width, measured horizontally in y-direction
imp ZU = upper plume boundary (Z-coordinate)
ZL = lower plune boundary (Z-coordinate)
S = hydrodynamic average (bulk) dilution
C = average (bulk) concentration (includes reaction effects, if any)
Pluae Stage 1 (not bank attached):
1 Y Z S C BV BH ZU ZL
9.15 -72.69 1.83 28.4 .705E+00 1.83 67.90 1.83 .00
207.32 -72.69 1.83 38.5 .520E+00 .80 209.50 1.83 1.03
405.49 -72.69 1.83 44.4 .451E+00 .64 305.92 1.83 1.19
603.66 -72.69 1.83 50.4 .391E+00 .57 384.87 1.83 1.26
801.83 -72.69 1.83 57.4 .348E+00 .55 453.76 1.83 1.28
1000.00 -72.69 1.83 65.7 .304E+00 .56 516.07 1.83 1.27
Cuaulative travel tiae = 13333. sec
PAM
NMI
gni
NMI
Siaulation limit based on maximum specified distance = 1000.00 a.
This is the REGION OF INTEREST limitation.
END OF H0D241: BUOYANT AMBIENT SPREADING
N.' COMM Submerged Multipart Diffuser Discharges End of Prediction File
22222222222222222222222222222222222222222222222222222222222222222222222222222

I I 1 I I I I I I 1 I I 1 1 I I I I 1
CAMP' \LEJEUNE COPMIX2 Prediction
15A11COASTr;GEOAI O ^m/\36AO, L 5I APOPTSATM A4 File: r i m\df un27 . cx2 •
0-
0
C1
0
I Y Y
f 1E
f Z}:
f
:eeee:eeee eeee:ear:eaeeeeeeeeeeeeee1eeeeeeeeeeeeeeee:eeeeeeeeseeeeeeeeeeeeeeeeseIceMeeeeeeeeeeeneeeeeeeeeeeeeeeeeeeeeeeeeeeeeeee
4•y+
200 400 .500 800 1000
X m 3.
Plan Uieu
Distortion = 0.522

1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1
C(MP' L JDUND COPMI 2 Prediction
15f MCD"DTnDDD"1.D. 'w"D6"Cl. 1 D1 "POPTS"Tht A4 File: si m\dt un27 _ rx2
0
_\
0 _ \ • f1
rti
10 4 - \
. \
cr - y
CO
i 2i\
a 0
o- \
0
0
J
i 1 I ' 1 lilt 1 i 1 T 1 i I I 1
1.5 3.0 4.5 6.0 7.5 9.0
x rn)
Concentration vs Dounst rr eam Distance

1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1
CAMP' -Lr JEUNE OOPf1I 2 Prediction
15AMGOASTAGEO^t O7 m/\36^0. t Off. POPTS"Th : ^4 File. i m\df un27 . c 2
O
w—
r
•
O-
O
• 0
O
Distortion = 317.121
200
400
Side Uieu
boo
800
err
1000

n
IX. RUN DFUN28
fl

l$iKiffi%%%%%%%%%%%%g%%%%%%%%%%%%%%%%%%%%%%%%g%%%%%%%%%%%%xxx%%%
CORHIK: CORNELL HIKING ZONE EXPERT SYSTEM
CORMIX v.3.10 June 1995
SITE NAME/LABEL: CAMP LEJEUNE
ORIGINAL design case: 5 KGD STAGED 107 a 36 PORTS 0.101a D0.101
ORIGINAL file naae: DFUN25
Flog Start of Rain session: 06/11/95--13:44:18
DESIGN ITERATION nunber:
NEW DESIGN CASE:
NEW FILE NAME:
Using subsystea CORKIX2:
Start of iteration session:
4
5 KGD STAGED 107 a 36 0.101 PORTS Tbt 45
DFUN28
Subaerged Multiport Diffuser Discharges
06/11/95--14:56:42
:::::**:******************************************************:*:**:****:****
SUMMARY OF INPUT DATA:
AMBIENT PARAMETERS:
Cross-section
Average depth
Depth at discharge
Aabient velocity
Darcy-Neisbach friction factor
Wind velocity
Stratification Type
Surface density
Bottom density
= unbounded
HA - 1.83 n
HD 1.83 a
UA - 0.075 n/s
F - 0.04
Ui1 - 2 a/s
STRCND = U
RHOAS
RHOAB
1018 kgla"3
1018 kgla"3
DISCHARGE PARAMETERS:
Diffuser type
Diffuser length
Nearest bank
Diffuser endpoints
Nuaber of openings
ing Spacing between risers/openings
Port/Nozzle diaaeter
Equivalent slot width
Total area of openings
Discharge velocity
Total discharge flowrate
Discharge port height
Nozzle arrangeaent
Diffuser alignlent angle
Vertical discharge angle
Horizontal discharge angle
Relative orientation angle
Sublerged Multiport Diffuser Discharge
DITYPE : staged perpendicular
LD : 107 R
. left
YB1 : 450 n; YB2 = 557 a
NOPEN = 36
SPAC : 3.05 a
0.101 a
0.0026 a
0.0080 1A2
0.75 als •
0.219 R"3/s
0.6 a
D0 -
B0 -
A0 -
U0 Q0
H0 -
BETYPE = staged
GAMMA
THETA
SIGMA
BETA
Discharge teaperature (freshwater)
Corresponding density RHO@
""' Density difference DRHO
Buoyant acceleration GPO
Discharge concentration CO
Surface heat exchange coeff. KS
Coefficient of decay KD
90 deg
45 deg
270 deg
0 deg
22 degC
• 997.7714 kg/RA3
• 20.2285 kg/e"3
• .1949 a/s"2
20 PPT-SAL-DEFICIT
0 a/s
0 1s
FLUX VARIABLES PER UNIT DIFFUSER LENGTH:
Discharge (volune flux) q0
Moaentua flux a0 Buoyancy flux j0 -
0.002047 a"2/s
0.001554 1"3/sA2
0.000399 a"3/s"3

DISCHARGE/ENVIRONMENT LENGTH SCADS : .
lq = 0.00. a la = 0.27 a 1M 0.28
la' = 99999.0 a 1b' = 99999.0 a - la = 99999.0 a
(These refer to the actual discharge/environment length scales.)
AmM NON -DIMENSIONAL PARAMETERS:
Slot Froude number FRO = 33.12
Port/nozzle Froude nuaber FRDO = 5.41
Velocity ratio R = 10.12
NIXING ZONE / TOXIC DILUTION ZONE / AREA OF INTEREST PARAMETERS:
Toxic discharge = no
Rater quality standard specified = yes
Rater quality standard CSTD = 1 PPT-SAL-DEFICIT
Regulatory fixing zone = no
,am Regionof interest = 1000.00 a downstreaa
ttlltttt!!!t!ltlttltltt!llttttttt!!:t!!t!t!!!!t!!t!ltttltltllttttttttttttlttt
HYDRODYNAMIC CLASSIFICATION:
t t
I FLOW CLASS = KU6 I
t !
This flow configuration applies to a layer corresponding to the full water
mom depth at the discharge site.
Applicable layer depth = Water depth = 1.83 e
PPR
t!lttttttttt!!!ttltttt!lttttttttlt!!!ttlttttllttttltlltltltt!!t!lttt!!tt!!tt!
MIXING ZONE EVALUATION (hydrodynaiic and regulatory suaaary):
X-Y-Z Coordinate system
Origin is located at the bottoa below the port center:
503.50 a frog the left bank/shore.
Huber of display steps NSTEP = 5 per aodule.
miq NEAR -FIELD REGION (NFR) CONDITIONS :
Note: The NFR is the zone of strong initial nixing. It has no regulatory
iaplication. However, this inforaation tay be useful for the discharge
designer because the airing in the NFR is usually sensitive to the
discharge design conditions.
Pollutant concentration at edge of NFR = .2885 PPP -SAL -DEFICIT
Dilution at edge of NFR - 69.3
NFR Location: x = 9.15 a
(centerline coordinates) y = -8.07 a
z= 1.83a
NFR plum dimensions: half -width = 55.31 a
thickness = 1.83 a
amp
Buoyancy assessaent:
The effluent density is less than the surrounding aabient water
density at the discharge level.
Therefore, the effluent is POSITIVELY BUOYANT and will tend to rise towards
the surface.
Hear -field instability behavior:
The diffuser flow will experience instabilities with full vertical nixing
in the near -field.
There nay be benthic iapact of high pollutant concentrations.
"i' FAR -FIELD MIXING SUMMARY:
Pluae becoaes vertically fully aixed WITHIN NEAR -FIELD at .00 a
dowastrean, but RE -STRATIFIES LATER and is not aired in the far -field.
A.
tttttlttttttttttttlltltt TOXIC DILUTION ZONE SUMMARY tttllttttttttttt:ttltttt
No TDZ was specified for this siaulation.

tttttttttttttttttlttt► REGULATORY MIXING ZONE SUMMARY ltttttttttttt►►tttltltt
r�r
No Rid has been specified.
However:
The aabient water quality standard was encountered at the following
plane position:
Water quality standard - 1 PPT-SAL-DEFICIT
Corresponding dilution - 20
Plume location: x = 1.79 a
(centerline coordinates) y = 41.41 n
z= .66a
Pluae diaensions: half -width = 10.89 a
thickness = .39 m
t!tlt►►tt!!tltttltltt FINAL DESIGN ADVICE AND COMMENTS ttltttt!!t*ltttttttttt
•C0RHIX2 uses the TWO-DIMENSIONAL SLOT DIFFUSER CONCEPT to represent
the actual three-dimensional diffuser pantry. Thus, it approximates
the details of the merging process of the individual jets froi each
port/nozzle.
In the present design, the spacing between adjacent ports/nozzles
(or riser assemblies) is of the order of, or less than, the local
water depth so that the slot diffuser approximation holds well.
Nevertheless, if this is a final design, the user is advised to use a
final CORHIX1 (single port discharge) analysis, with discharge data
for an individual diffuser jet/plume, in order to compare to
the present near -field prediction.
REMINDER: The user gust take note that HYDRODYNAMIC MODELING by any known
technique is NOT AN EIACT SCIENCE.
Extensive coaparison with field and laboratory data has shown that the
CORHII predictions on dilutions and concentrations (with associated
plume geometries) are reliable for the majority of cases and are accurate
to within about +-50% (standard deviation) .
As a further safeguard, CORHIX will not give predictions whenever it judges
the design configuration as highly complex and uncertain for prediction.
!!!t!tlttttttttttt IMIIltltttttttlttt!!lfiatttttltttttttlt!►ttttt MiltMiltt
DESIGN CASE: 5 HGD STAGED 107 a 36 0.101 PORTS Tht 45
FILE MANE: DFUN28
Subsystea CORHIX2: Submerged Multipart Diffuser Discharges
END OF SESSION/ITERATION: 06/11/95--15:01:07
XXXXXXXIZIIIIIXIXX XXXXXXXIXIIIXIIXXBXgIXXXXIIIIXXIIXIIIIXIIIXZIIIIXIIXIXIII

CORNIX2 PREDICTION FILE:
22222222222222222222222222222222222222222222222222222222222222222222222222222
CORNELL NIXING ZONE EXPERT SYSTEM
Subsystea CORNIX2: Subsystea version:
Subaerged Multipart Diffuser Discharges CORMIX v.3.10 June 1995
CASE DESCRIPTION
Site naae/label:
Design case:
FILE NAME:
Tine of Fortran run:
CANP"LEJEUNE
51GD"STAGED"107"a"36"0.101"FORTS"Tht"45
cornizlsialDFUN28 .cx2
06/11/95--15:00:17
ENVIRONMENT PARAMETERS (aetric units)
'am: Unbounded section
HA - 1.83 HD = 1.83
UA - .075 F - .040 USTAR :.5303E-02
UM - 2.000 UWSTAR:.2198E-02
Unifora density.environaent
STRCND: U RHOAN : 1018.0000
DIFFUSER DISCHARGE PARAMETERS (aetric units)
Diffuser type: DITYPE= staged perpendicular
BANK z LEFT DISTB = 503.50 YB1 : 450.00 YB2 : 557.00
LD - 107.00 NOPEN : 36 SPAC = 3.06
D0 - .101 AO : .008 H0 : .60
Nozzle/port arrangeaent: staged
GAMMA = 90.00 THETA = 45.00 SIGMA = 270.00 BETA : .00
U0 - .759 00 - .219 = .2190E+00
RHOO s 997.7714 DRHOO = .2023E+02 GPO :.1949E+00
CO = .2000E+02 CUNITS= PPT-SAL-DEFICIT
o• IPOLL s 1 KS = .0000E+00 KD :.0000E+00
FLUX VARIABLES - PER UNIT DIFFUSER LENGTH (aetric units)
q0 :.20418-02 10 :.1554E-02 j0 = .3989E-03 SIGNJO: 1.0
Associated 2-d length scales (neters)
1Q:B : .003 1K - .29 In : .28
lap : 99999.00 lbp = 99999.00 la = 99999.00
FLUX VARIABLES - ENTIRE DIFFUSER (aetric units)
QO :. 2190E+00 K0 ..1663E+00 JO :. 4268E-01
°" R Associated 3-d length scales (aeters)
LQ = .54 LK : 1.26 La : 5.44 Lb - 101.16
Lap = 99999.00 Lbp : 99999.00
NON -DIMENSIONAL PARAMETERS
FRO : 33.12 FRDO : 5.41 R - 10.12
(slot) (port/nozzle)
FLOW CLASSIFICATION
222222222222222222222222222222222222222222
2 Flo class (CORMIX2) - NU6 2
2 Applicable layer depth HS = 1.83 2
222222222222222222222222222222222222222222

aim
fallt
MIXING ZONE / TOXIC DILUTION / REGION OF INTEREST PARAMETERS
CO = .2000E+02 CUNITS= PPT-SAL-DEFICIT
NTOI = 0
NSTD = 1 CST!) = .1000E+01
REGNZ = 0
XINT = 1000.00 %MAI = 1000.00
X-Y-Z COORDINATE SYSTEM:
ORIGIN is located at the bottom and the diffuser aid -point:
503.50 a from the LEFT bank/shore.
X-axis points downstreaa, Y-axis points to left, 2-axis points upward.
NSTEP = 5 display intervals per nodule
BEGIN MOD202: DISCHARGE NODULE (STAGED DIFFUSER)
Due to complex near -field motions: EQUIVALENT SLOT DIFFUSER (2-D) GEOMETRY
Profile definitions:
,a, BV = Gaussian 1/e (37%) half -width, in vertical plane normal to trajectory
BH = Gaussian 1/e (371) half -width in horizontal plane aortal to trajectory
S = hydrodynamic centerline dilution
C = centerline concentration (includes reaction effects, if any)
X Y Z S C BV BH
.00 53.50 .60 1.0 .200E+02 .05 .05
END OF M0D202: DISCHARGE MODULE (STAGED DIFFUSER)
BEGIN NOD275: STAGED PERPENDICULAR DIFFUSER IN STRONG CURRENT
Because of the strong ambient current the diffuser plume of this crossflowing
discharge gets RAPIDLY DEFLECTED.
A near -field zone is forced that is VERTICALLY FULLY MIXED over the entire
layer depth. Full mixing is achieved at a downstream distance of about
five (5) layer depths.
Profile definitions:
BV = layer depth (vertically mixed)
BH top -hat half -width, neasured horizontally in y-direction
S = hydrodynamic average (bulk) dilution
C = average (bulk) concentration (includes reaction effects, if any)
2 Y Z S C BV BH
.00 53.50 .60 1.0 .199E+02 .05 .05
mot ** WATER QUALITY STANDARD OR CCC HAS BEEN FOUND **
The pollutant concentration in the plune falls below water quality standard
or CCC value of .1008+01 in the current prediction interval.
This is the spatial extent of concentrations exceeding the water quality
standard or CCC value.
1.83 41.18 .66 31.6 .634E+00 .41 11.10
3.66 28.81 .13 44.2 .452E+00 .76 22.15
5.49 16.55 .19 53.9 .371E+00 1.12 33.21
7.32 4.24 .85 62.1 .322E+00 1.41 44.26
9.15 -8.08 .92 69.3 .289E+00 1.83 55.31
PER Cumulative travel tine = 122. sec
END OF MOD275: STAGED PERPENDICULAR DIFFUSER IN STRONG CURRENT
** End of NEAR -FIELD REGION (NFR) "

NMI
AIM
w.a
BEGIN HOD241: BUOYANT AMBIENT SPREADING
Profile definitions:
BV z top -hat thickness, measured vertically
BB = top -hat half -width, measured horizontally in y-direction
ZU = upper pluae boundary (Z-coordinate)
ZL = lower plune boundary (Z-coordinate)
S = bydrodynaaic average (bulk) dilution
C = average (bulk) concentration (includes reaction effects, if any)
Pluae Stage 1 (not bank attached):
I Y Z S C BV BB ZU ZL
9.15 -8.08 1.83 69.3 .289E+00 1.83 55.31 1.83 .00
207.32 -8.08 1.83 92.6 .216E+00 .89 151.23 1.83 .94
405.49 -8.08 1.83 110.6 .181E+00 .74 219.39 1.83 1.09
603.66 -8.08 1.83 132.5 .151E+00 .70 276.43 1.83 1.13
801.83 -8.08 1.83 160.4 .125E+00 .72 327.05 1.83 1.11
1000.00 -8.08 1.83 195.5 .102E+00 .76 373.46 1.83 1.07
Cuiulative travel time = 13333. sec
Siaulation limit based on naziaum specified distance = 1000.00 a.
This is the REGION OF INTEREST limitation.
END OF HOD241: BUOYANT AMBIENT SPREADING
CORHII2: Subaerged Kultiport Diffuser Discharges End of Prediction file
,,,, 22222222222222222222222222222222222222222222222222222222222222222222222222222

1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1
CAMP �• EJEUNE COPMIX2 Prediction
6AMG O/ T AGE0^t O A A36AO= 1 Ot'\pOpTSATht r`45 File: si m\.OFUN2S . C: =:2
nal
0_
T1
M00
wMW.wryy`a./an
M YVMa•
f1i
rf 1
ri
.ti
1
i�4•���Y4•�u"4.�
T- I 1
0
Distortion = 0.636
' 1 ' 1 1 1 1
200 400 600
Plan Uieu
•
' 1 '
800
amonmillib
woo
X n) ----- .

1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1
GAMP :- LEJ EUNE COPM1 '2 Prediction
D^ DD^DTADDD^1 D7 ^m^36^0. i Dl POPTD^Tht ^4D File: si m DFUN28 . c
colo
•
r\j1 1
o
-+ c‘i ;
Q .--------
co • a f
• i C =
O v /
cr
-*
/
r!
1/
J
f/
J
sf
iD ? "�6 0 200 406
}M}��.y AY.�r. IJ.
E0 •. . -M
Distortion = 313.221
Side CJieu
600
800
1000
X On) —*

1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1
CA P "`'LEJEUNE
COPNI 2 Prediction
GA GDASTAGEDAL D7 ^r'IA,3. 6A0. L DL ^PORTS^Thy: ^4G File: si m\:.DFUNI° . c =:"
0
(PPT-SAL-DEFICIT) x
0
-
r
0
O-
0
'-
0
0
do•V
I 1 1 T 1 1
1.5 3.0 4.5 6.0 7.5
Concentration vs Dounst r- earn Di at ance
I 1
X (in)

X. HYDRAULIC ANALYSES OUTFALL DIFFUSER SYSTEM
aim

DATE = June 10.1995 PAGE NO. 1 •
JOB NAME = Cup Lejeune Diffuser 36 Ports 3.5 inch Ports '30 MGD
amp
FLORAS IS EXPRESSED IN GPM AND PRESSURE IN PSIG
A SUMMARY , OF THE ORIGINAL DATA FOLLOWS
PIPE NO. NODE NOS. LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED GRADE
(FEET) (INCHES)
1 0 1 4300.0 51.2 120.0 1.00 17.60
2 1 2 6.0 8.0 120.0 1.80
3 2 0 1.0 3.5 120.0 3.00 1.00
4 1 3 10.0 51.2 120.0 .50
5 3 4 6.0 8.0 120.0 1.80
6 4 0 1.0 3.5 120.0 3.00 1.00
1 3 5 10.0 51.2 120.0 .50
8 5 6 6.0 8.0 120.0 1.80
9 6 0 1.0 3.5 120.0 3.00 1.00
10 5 7 10.0 51.2 120.0 .50
11 7 8 6.0 8.0 120.0 1.80
12 8 0 1.0 3.5 120.0 3.00 1.00
13 7 9 10.0 51.2 120.0 .50
14 9 10 6.0 8,0 120.0 1.80
15 10 0 1.0 3.5 120.0 3.00 1.00
16 9 11 10.0 51.2 120.0 .50
17 11 12 6.0 8.0 120.0 1.80
18 12 0 1.0 3.5 120.0 3.00 1.00
19 11 13 10.0 51.2 120.0 .50
20 13 14 6.0 8.0 120.0 1.80
21 14 0 1.0 3.5 120.0 3.00 1.00
22 13 15 10.0 51.2 120.0 .50
23 15 16 6.0 8.0 120.0 1.80
24 16 0 1.0 3.5 120.0 3.00 1.00
25 15 17 10.0 51.2 120.0 .50
26 17 18 6.0 8.0 120.0 1.80
27 18 0 1.0 3.5 120.0 3.00 1.00
28 17 19 10.0 51.2 120.0 .50
29 19 20 6.0 8.0 120.0 1.80
30 20 0 1.0 3.5 120.0 3.00 1.00
31 19 21 10.0 51.2 120.0 .50
32 21 22 6.0 8.0 120.0 1.80
33 22 0 1.0 3.5 120.0 3.00 1.00
34 21 23 10.0 51.2 120.0 .50
35 23 24 6.0 8.0 120.0 1.80
36 24 0 1.0 3.5 120.0 3.00 1.00
37 23 25 10.0 51.2 120.0 .50
38 25 26 6.0 8.0 120.0 1.80
39 26 0 1.0 3.5 120.0 3.00 1.00
40 25 27 10.0 51.2 120.0 .50

DATE = June 10 1995 PAGE KO. 2
JOB RAKE = Camp Lejeune Diffuser 36 Ports 3.5 inch Ports 30 KGD
MCI
41 27 28 6.0 8.0 120.0 1.80
42 28 0 1.0 3.5 120.0 3.00 1,00
43 27 29 10.0 51.2 120.0 .50
44 29 30 6.0 8.0 120.0 1.80
45 30 0 1.0 3.5 120.0 3.00 1.00
46 29 31 10.0 51.2 120.0 .50
47 31 32 6.0 8.0 120.0 1.80
mon 48 32 0 1.0 3.5 120.0 3.00 1.00
49 31 33 10.0 51.2 120.0 .50
50 33 34 6.0 8.0 120.0 1.80
51 34 0 1.0 3.5 120.0 3.00 1.00
52 33 35 10.0 51.2 120.0 .50
53 35 36 6.0 8.0 120.0 1.80
54 36 0 1.0 3.5 120.0 3.00 1.00
55 35 37 10.0 51.2 120.0 .50
56 37 38 6.0 8.0 120.0 1.80
57 38 0 1.0 3.5 120.0 3.00 1.00
mop 58 37 39 10.0 51.2 120.0 .50
59 39 40 6.0 8.0 120.0 1.80
60 40 0 1.0 3.5 120.0 3.00 1.00
61 39 41 10.0 51.2 120.0 .50
62 41 42 6.0 8.0 120.0 1.80
63 42 0 1.0 3.5 120.0 3.00 1.00
64 41 43 10.0 51.2 120.0 .50
65 43 44 6.0 8.0 120.0 1.80
66 44 0 1.0 3.5 120.0 3.00 1.00
67 43 45 10.0 51.2 120.0 .50
68 45 46 6.0 8.0 120.0 1.80
nen
69 46 0 1.0 3.5 120.0 3.00 1.00
10 45 47 10.0 51.2 120.0 .50
11 41 48 6.0 8.0 120.0 1.80
72 48 0 1.0 3.5 120.0 3.00 1.00
73 41 49 10.0 51.2 120.0 .50
74 49 50 6.0 8.0 120.0 1.80
75 50 0 1.0 3.5 120.0 3.00 1.00
76 49 51 10.0 51.2 120.0 .50
77 51 52 6.0 8.0 120.0 1.80
78 52 0 1.0 3.5 120.0 3.00 1.00
19 51 53 10.0 51.2 120.0 .50
80 53 54 6.0 8.0 120.0 1.80
81 54 0 1.0 3.5 120.0 3.00 1.00
82 53 55 10.0 51.2 120.0 .50
83 55 56 6.0 8.0 120.0 1.80
84 56 0 1.0 3.5 120.0 3.00 1.00
ism 85 55 51 10.0 51.2 120.0 .50
86 57 58 6.0 8.0 120.0 1.80
87 58 0 1.0 3.5 120.0 3.00 1.00
88 57 59 10.0 51.2 120.0 .50
89 59 60 6.0 8.0 120.0 1.80
90 60 0 1.0 3.5 120.0 3.00 1.00
91 59 61 10.0 51.2 120.0 .50
�a 92 61 62 6.0 8.0 120.0 1.80
93 62 0 1.0 3.5 120.0 3.00 1.00
94 61 63 10.0 51.2 120.0 .50
95 63 64 6.0 8.0 120.0 1.80

DATE s June 10 1995 PAGE NO. 3
JOB KAKI z Caip Wane Diffuser 36 Ports 3.5 inch Ports 30 NGD
NMI
96 64 0 1.0 3.5 120.0 3.00 1.00
91 63 65 10.0 51.2 120.0 .50
98 65 66 6.0 8.0 120.0 1.80
99 66 0 1.0 3.5 120.0 3.00 1.00
100 65 67 10.0 51.2 120.0 .50
101 67 68 6.0 8.0 120.0 1.80
102 68 0 1.0 3.5 120.0 3.00 1.00
103 67 69 10.0 51.2 120.0 .50
104 69 70 6.0 8.0 120.0 1.80
105 10 0 1.0 3.5 120.0 3.00 1.00
106 69 71 10.0 51.2 120.0 .50
107 71 72 6.0 8.0 120.0 1.80
108 72 0 1.0 3.5 120.0 3.00 1.00
JUNCTION NUMBER DEMAND ELEVATION CONNECTING PIPES
1 .00 1.00 1 • 2 4
2 .00 1.00 2 3
qmq
3 .00 .00 4 5 7
4 .00 .00 5 6
5 .00 .00 1 8 10
mil 6 .00 .00 8 9
1 .00 .00 10 11 13
8 .00 .00 11 12
9 .00 .00 13 14 16
pm
10 .00 .00 14 15
11 .00 .00 16 17 19
12 .00 .00 17 18
1° 13 .00 .00 19 20 22
14 .00 .00 20 21
15 .00 .00 22 23 25
mo 16 .00 .00 23 24
17 .00 .00 25 26 28
18 .00 .00 26 21
19 .00 .00 28 29 31
MIR
20 .00 .00 29 30
21 .00 .00 31 32 34
22 .00 .00 32 33
"m 23 .00 .00 34 35 31
24 .00 .00 35 36
25 .00 .00 31 38 40
,®, 26 .00 .00 38 39
27 .00 .00 40 41 43
28 .00 .00 41 42
29 .00 .00 43 44 46
'imp 30 .00 .00 44 45
31 .00 .00 46 41 49
32 .00 .00 47 48
+a 33 .00 .00 49 50 52
34 .00 .00 50 51
35 .00 .00 52 53 55
36 .00 .00 53 54
mmi
37 .00 .00 55 56 58
38 .00 .00 56 51
39 .00 .00 58 59 61

DATE - June 10 1995 PAGE RO. 4
JOB RARE r Caap Lejeune Diffuser 36 Ports 3.5 inch Ports 30 MGD
40 .00 .00 59 60
41 .00 .00 61 62 64
42 .00 .00 62 63
43 .00 .00 64 65 67
44 .00 .00 65 66
45 .00 .00 67 68 70
46 .00 .00 68 69
47 .00 .00 70 71 73
48 .00 .00 71 72
49 .00 .00 73 74 76
50 .00 .00 74 75
51 .00 .00 76 77 19
52 .00 .00 77 78
53 .00 .00 79 80 82
54 .00 .00 80 81
-55 .00 .00 82 83 85
56 .00 .00 83 84
57 .00 .00 85 86 88
58 .00 :00 .86 87
59 .00 .00 88 89 91
60 .00 .00 89 90
61 .00 .00 91 92 94
62 .00 .00 92 93
63 .00 .00 94 95 97
64 .00 .00 95 96
65 .00 .00 97 98 100
66 .00 .00 98 99
61 .00 .00 100 101 103
68 .00 .00 101 102
69 .00 .00 103 104 106
70 .00 .00 104 105
11 .00 .00 106 107
72 .00 .00 107 108
OUTPUT SELECTION: ALL RESULTS ARE OUTPUT EACH PERIOD
THIS SYSTEM HAS 108 PIPES WITH 12 JUNCTIONS , 0 LOOPS AND 37 FGNS
THE RESULTS ARE OBTAINED AFTER 4 TRIALS WITH AN ACCURACY = .00455
PIPE NO. NODE NOS. FLOWRATE HEAD LOSS PUMP HEAD MINOR LOSS VELOCITY HL/1000
1 0 1 18020.46 2.29 .00 .12 2.81 .53
2 1 2 510.87 .04 .00 .30 3.26 6.11
3 2 0 510.87 .34 .00 13.52 17.03 342.22
4 1 3 17509.59 .01 .00 .06 2.73 .50

DATE . June 10 1995 PAGE NO. 5
q., JOB NAME = Cup Lejeune Diffuser 36 Ports 3.5 inch Ports 30 MGD
5 3 4 509..73 .04 .00 .30 3.25 6.08
6 4 0 509.13 .34 .00 13.46 17.00 340.81
7 3 5 16999.86 .00 .00 .05 2.65 .48
mai 8 5 6 508.66 .04 .00 .29 3.25 6.06
9 6 0 508.66 .34 .00 13.40 16.96 339.48
10 5 7 16491.20 .00 .00 .05 2.57 .45
11 7 8 507.65 .04 .00 .29 3.24 6.04
12 8 0 507.65 .34 .00 13.35 16.93 338.23.
13 7 9 15983.55 .00 .00 .05 2.49 .43
14 9 10 506.69 .04 .00 .29 3.23 6.02
15 10 0 506.69 .34 .00 13.30 16.90 337.05
16 9 11 15476. 86 .00 .00 .05 2.41 .40
11 11 12 505.80 .04 .00 .29 3.23 6.00
18 12 0 505.80 .34 .00 13.25 16.87 335.95
19 11 13 14911.06 .00 .00 .04 2.33 .38
20 13 14 504..96 .04 .00 .29 3.22 5.98
21 14 0 504.96 .33 .00 13.21 16.84 334.92
22 13 15 14466.10 .00 .00 .04 2.25 .35
23 15 16 504.17 .04 .00 .29 3.22 5.96
24 16 0 504.11 .33 .00 13.16 16.81 333.95
25 15 17 13961.93 .00 .00 .04 2.18 .33
26 17 18 503.44 .04 .00 .29 3.21 5.94
21 18 0 503.44 .33 .00 13.13 16.79 333.06
ror, 28 17 19 13458.49 .00 .00 .03 2.10 .31
29 19 20 502.76 .04 .00 .29 3.21 5.93
30 20 0 502.76 .33 .00 13.09 16.76 332.22
31 19 21 12955.74 .00 .00 .03 2.02 .29
min 32 21 22 502.12 .04 .00 .29 3.20 5.92
33 22 0 502.12 .33 .00 13.06 16.74 331.44
34 21 23 12453. 61 .00 .00 .03 1.94 .27
35 23 24 501.54 .04 .00 .29 3.20 5.90
36 24 0 501.54 .33 .00 13.03 16.72 330.73
37 23 25 11952.08 .00 .00 .03 1.86 .25
38 25 26 501.00 .04 .00 .29 3.20 5.89
39 26 0 501.00 .33 .00 13.00 16.71 330.07
40 25 27 11451.08 .00 .00 .02 1.78 .23
41 27 28 500.50 .04 .00 .29 3.19 5.88
42 28 0 500.50 .33 .00 12.97 16.69 329.46
43 27 29 10950.58 .00 .00 .02 1.11 .21
44 29 30 500.04 .04 .00 .28 3.19 5.87
mn 45 30 0 500.04 .33 .00 12.95 16.67 328.91
46 29 31 10450.54 .00 .00 .02 1.63 .19
47 31 32 499.63 .04 .00 .28 3.19 5.86
48 32 0 499.63 .33 .00 12.93 16.66 328.40
fie' 49 31 33 9950.91 .00 .00 .02 1.55 .18
50 33 34 499.25 .04 .00 .28 3.19 5.85
51 34 0 499.25 .33 .00 12.91 16.65 321.94
52 33 35 9451.65 .00 .00 .02 1.47 .16
53 35 36 498.91 .04 .00 .28 3.18 5.85
54 36 0 498.91 .33 .00 12.89 16.64 327.53
,,,e 55 35 37 8952.74 .00 .00 .02 1.40 .15
56 37 38 498.61 .04 .00 .28 3.18 5.84
57 38 0 498.61 .33 .00 12.88 16.63 327.16
58 37 39 8454.14 .00 .00 .01 1.32 .13
OM' 59 39 40 498.33 .03 .00 .28 3.18 5.83

DATE . June 10 1995 PAGE NO. 6
JOB NAME . Canp Lejeune Diffuser 36 Ports 3.5 inch Ports 30 MGD
60 40 0 498.33 .33 .00 12.86 16.62 326.82
61 39 41 7955.80 .00 .00 .01 1.24 .12
62 41 42 498.09 .03 .00 .28 3.18 5.83
63 42 0 .498.09 .33 .00 12.85 16.61 326.53
64 41 43 7457.71 .00 .00 .01 1.16 .10
65 43 44 497.88 .03 .00 .28 3.18 5.82
66 44 0 497.88 .33. .00 12.84 16.60 326.27
67 43 45 6959.84 .00 .00 .01 1.08 .09
68 45 46 497.69 .03 .00 .28 3.18 5.82
69 46 0 497.69 .33 .00 12.83 16.60 326.05
10 45 47 6462.15 .00 .00 .01 1.01 .08
71 41. 48 497.53 .03 .00 .28 3.18 5.82
72 48 0 497.53 .33 .00 12.82 16.59 325.85
73 47 49 5964.61 .00 .00 .01 .93 .01
74 49 50 497.39 .03 .00 .28 3.17 5.81
75 50 0 497.39 .33 .00 12.81 16.59 325.69
76 49 51 5467.22 .00 .00 .01 .85 ' .06
71 51 52 497.28 .03 .00 .28 3.17 5.81
78 52 0 497.28 .33 .00 12.81 16.58 325.55
19 51 53 4969.94 .00 .00 .00 .77 .05
80 53 54 497.18 .03 .00 .28 3.17 5.81
81 54 0 497.18 .33 .00 12.80 16.58 325.43
82 53 55 4472.76 .00 .00 .00 .70 .04
83 55 56 497.11 .03 .00 .28 3.17 5.81
84 56 0 497.11 .33 .00 12.80 16.58 325.34
85 55 57 3975.65 .00 .00 .00 .62 .03
86 57 58 497.05 .03 .00 .28 3.17 5.80
87 58 0 497.05 .33 .00 12.79 16.57 325.26
88 57 59 3478.60 .00 .00 .00 .54 .03
89 59 60 497.00 .03 .00 .28 3.17 5.80
90 60 0 497.00 .33 .00 12.79 16.57 325.21
91 59 61 2981.60 .00 .00 .00 .46 .02
92 61 62 496.97 .03 .00 .28 3.17 5.80
93 62 0 496.97 .33 .00 12.79 16.57 325.17
94 61 63 2484.63 .00 .00 .00 .39 .01
95 63 64 496.94 .03 .00 .28 3.17 5.80
96 64 0 496.94 .33 .00 12.79 16.57 325.14
97 63 65 1987.69 .00 .00 .00 .31 .01
98 65 66 496.93 .03 .00 .28 3.17 5.80
99 66 0 496.93 .33 .00 12.79 16.57 325.12
100 65 67 1490.76 .00 .00 .00 .23 .01
101 67 68 496.92 .03 .00 .28 3.17 5.80
102 68 0 496.92 .33 .00 12.79 16.57 325.11
103 67 69 993.84 .00 .00 .00 .15 .00
104 69 70 496.92 .03 .00 .28 3.17 5.80
105 70 0 496.92 .33 .00 12.79 16.57 325.11
106 69 11 496.92 .00 .00 .00 .08 .00
107 71 72 496.92 .03 .00 .28 3.17 5.80
108 72 0 496.92 .33 .00 12.79 16.57 325.11
JUNCTION NUMBER DEMAND GRADE LINE ELEVATION PRESSURE
1 .00 15.19 1.00 6,15
2 .00 14.86 1.00 6.01
3 .00 15.13

DATE = June 10 1995 PAGE NO. 7
JOB NAME = Caip Lejeune Diffuser 36 Ports 3.5 inch Ports 30 MGD
4 .00 14.80
5 .00 15.07
6 .00 14.74
7 .00 15.01
8 .00 14.68
9 .00 14.96
10 .00 14.63
11 .00 14.91
12 .00 14.59
13 .00 14.87
14 .00 14.54
15 .00 14.82
16 .00 14.50
17 .00 14.78
18 .00 14.46
19 .00 14.75
20 .00 14.42
21 .00 14.71
22 .00 14.39
23 .00 14.68
24 .00 14.36
25 .00 14.65
`m 26 .00 14.33
27 .00 14.62
28 .00 14.30
29 .00 14.60
30 .00 14.28
31 .00 14.58
,.R 32 .00 14.26
33 .00 14.56
34 .00 14.24
35 .00 14.54
won 36 .00 14.22
37 .00 14.52
38 .00 14.20
Pal 39 .00 14.51
40 .00 14.19
41 .00 14.49
amp42 .00 14.18
43 .00 14.48
44 .00 14.16
45 .00 14.47
46 .00 14.15
47 .00 14.46
48 .00 14.15
p., 49 .00 14.45
50 .00 14.14
51 .00 14.45
52 .00 14.13
53 .00 14.44
54 .00 14.13
55 .00 14.44
56 .00 14.12
57 .00 14.44
58 .00 14.12

DATE = June 10 1995 PAGE NO. 8
JOB NAME = Caip Lejeune Diffuser 36 Ports 3.5 inch Ports 30 KGD
59 .00 14.43
60 .00 14.12
61 .00 14.43
62 .00 14.12
63 .00 14.43
64 .00 14.11
65 .00 14.43
66 .00 14.11
67 .00 14.43
68 .00 14.11
69 .00 14.43
70 .00 14.11
71 .00 14.43
72 .00 14.11
THE NET SYSTEM DEMAND = .00
SUMMARY OF INFLONS(+) AND OUTFLOWS(-) FROM FIXED GRADE NODES
PIPE NUMBER FLONRATE
1 18020.46
3-510.87
6-509.73
9-508.66
12-507.65
15-506.69
18-505.80
21-504.96
24-504.17
27-503.44
30-502.76
33-502.12
36-501.54
39-501.00
42-500.50
45-500.04
48-499.63
51-499.25
54-498.91
57 -498.61
60-498.33
63-498.09
66-497.88
69-497.69
72-497.53
75-497.39
78-497.28
81 497.18
84-497.11
87-497.05
90-497.00
93-496.97
96-496.94
99-496.93
102-496.92

DATE = June 10 1'995 PAGE NO. 9
JOB HARE = Caap Lejeune Diffuser 36 Ports 3.5 inch Ports' 30 HGD
105
-496.92
108-496.92
THE NET FLOW INTO THE SYSTEH FROM FIXED GRADE NODES = 18020.46
THE NET FLOW OUT OF THE SYSTEM INTO FIXED GRADE NODES =-18020.47

DATE = June 10 1995 • PAGE KO. 1
JOB NAME II Carp Lejeune Diffuser 36 Ports 3.75 inch Ports 30 KGD
Inel
IOW
FLOWRATE IS EXPRESSED IN GPM AND PRESSURE IN PSIG
1°'" A SUMMARY OF THE ORIGINAL DATA FOLLOWS
PIPE NO. NODE NOS. LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED GRADE
(FEET) (INCHES)
1 0 1 4300.0 51.2 120.0 1.00 17.60
2 1 2 6.0 8.0 120.0 1.80
3 2 0 1.0 3.8 120.0 3.00 1.00
4 1 3 10.0 51.2 120.0 .50
5 3 4 6.0 8.0 120.0 1.80
6 4 0 1.0 3.8 120.0 3.00 1.00
7 3 5 10.0 51.2 120.0 .50
8 5 6 6.0 8.0 120.0 1,80
9 6 0 1.0 3.8 120.0 3.00 1.00
10 5 7 10.0 51.2 120.0 .50
11 7 8 6.0 8.0 120.0 1.80
12 8 0 1.0 3.8 120.0 3.00 1.00
13 7 9 10.0 51.2 120.0 .50
14 9 10 6.0 8.0 120.0 1.80
15 . 10 0 1.0 3.8 120.0 3.00 1.00
16 9 11 10.0 51.2 120.0 .50
11 11 12 6.0 8.0 120.0 1.80
18 12 0 1.0 3.8 120.0 3.00 1.00
19 11 13 10.0 51.2 120.0 .50
20 13 14 6.0 8.0 120.0 1.80
21 14 0 1.0 3.8 120.0 3.00 1.00
22 13 15 10.0 51.2 120.0 .50
23 15 16 6.0 8.0 120.0 1.80
A., 24 16 0 1.0 3.8 120.0 3.00 1.00
25 15 17 10.0 51.2 120.0 .50
26 17 18 6.0 8.0 120.0 1.80
27 18 0 1.0 3.8 120.0 3.00 1.00
28 17 19 10.0 51.2 120.0 .50
29 19 20 6.0 8.0 120.0 1.80
30 20 0 1.0 3.8 120.0 3.00 1.00
31 19 21 10.0 51.2 120.0 .50
32 21 22 6.0 8.0 120.0 1.80
33 22 0 1.0 3.8 120.0 3.00 1.00
34 21 23 10.0 51.2 120.0 .50
35 23 24 6.0 8.0 120.0 1.80
36 24 0 1.0 3.8 120.0 3.00 1.00
37 23 25 10.0 51.2 120.0 .50
38 25 26 6.0 8.0 120.0 1.80
39 26 0 1.0 3.8 120.0 3.00 1.00
40 25 27 10.0 51.2 120.0 .50

DAM r June 10 1995 PAGE NO. 2
JOB NAME r Cup Lejeune Diffuser 36 Ports 3.75 inch Ports 30 HD
41 27 28 6.0 8.0 120.0 1.80
42 28 0 1.0 3.8 120.0 3.00 1.00
43 21 29 10.0 51.2 120.0 .50
44 29 30 6.0 8.0 120.0 1.80
45 30 0 1.0 3.8 120.0 3.00 1.00
46 29 31 10.0 51.2 120.0 .50
47 31 32 6.0 8.0 120.0 1.80
48 32 0 1.0 3.8 120.0 3.00 1.00
49 31 33 10.0 51.2 120.0 50
50 33 34 6.0 8.0 120.0 1.80
51 34 0 1.0 3.8 120.0 3.00 1.00
52 33 35 10.0 51.2 120.0 . .50
53 35 36 6.0 8.0 120.0 1.80
54 36 0 1.0 3.8 120.0 3.00 1.
55 35 37 10.0 51.2 120.0 .50
56 37 38 6.0 8.0 120.0 1.80
57 38 0 1.0 3.8 120.0 3.00 1.00
58 37 39 10.0 51.2 120.0 .50
59 39 40 6.0 8.0 120.0 1.80
60 40 0 1.0 3.8 120.0 3.00 1.00
61 39 41 10.0 51.2 120.0 .50
62 41 42 6.0 8.0 120.0 1.80
63 42 0 1,0 3.8 120.0 3.00 1.00
64 41 43 10.0 51.2 120.0 .50
65 43 44 6.0 8.0 120.0 1.80
66 44 0 1.0 3.8 120.0 3.00 1.00
67 43 45 10.0 51.2 120.0 .50
68 45 46 6.0 8.0 120.0 1.80
69 46 0 1.0 3.8 120.0 3.00 1.00
70 45 47 10.0 51.2 120.0 .50
71 47 48 6.0 8.0 120.0 1.80
12 48 0 1.0 3.8 120.0 3.00 1.00
73 47 49 10.0 51.2 120.0 .50
14 49 50 6.0 8.0 120.0 1.80
75 50 0 1.0 3.8 120.0 3.00 1.00
76 49 51 10.0 51.2 120.0 .50
77 51 52 6.0 8.0 120,0 1.80
18 52 0 1.0 3.8 120.0 3.00 1.00
79 51 53 10.0 51.2 120.0 .50
80 53 54 6.0 8.0 120.0 1.80
81 54 0 1.0 3.8 120.0 3.00 1.00
82 53 55 10.0 51.2 120.0 .50
83 55 56 6.0 8.0 120.0 1.80
84 56 0 1.0 3.8 120.0 3.00 1.00
85 55 57 10.0 51.2 120.0 .50
86 57 58 6.0 8.0 120.0 1.80
87 58 0 1.0 3.8 120.0 3.00 1.00
88 57 59 10.0 51.2 120.0 .50
89 59 60 6.0 8.0 120.0 1.80
90 60 0 1.0 3.8 120.0. 3.00 1.00
91 59 61 10.0 51.2 120.0 .50
92 61 62 6.0 8.0 120.0 1.80
93 62 0 1.0 3.8 120.0 3.00 1.00
94 61 63 10.0 51.2 120.0 .50
95 63 64 6.0 8.0 120.0 1.80

DATE = June 10 1995 PAGE NO. 3
JOB NAME = Cup Lejeuae Diffuser 36 Ports 3.75 inch Ports 30 MGD
GIN
POIR
PEI
96 64 0 1.0 3.8 120.0 3.00 1.00
97 63 65 10.0 51.2 120.0 .50
98 65 66 6.0 8.0 120.0 1.80
99 66 0 1.0 3.8 120.0 3.00 1.00
100 65 67 10.0 51.2 120.0 .50
101 67 68 6.0 8.0 120.0 1.80
102 68 0 1.0 3.8 120.0 3.00 1.00
103 67 69 10.0 51.2 120.0 .50
104 69 70 6.0 8.0 120.0 1.80
105 70 0 1.0 3.8 120.0 3.00 1.00
106 69 71 10.0 51.2 120.0 .50
107 71 72 6.0 8.0 120.0 1.80
108 72 0 1.0 3.8 120.0 3.00 1.00
JUNCTION NUMBER DEMAND ELEVATION CONNECTING PIPES
1 .00 1.00 1 2 4
2 .00 1.00 2 3
3 .00 .00 4 5 7
4 .00 .00 5 6
5 .00 .00 7 8 10
6 .00 .00 8 9
1 .00 .00 10 11 13
8 .00 .00 11 12
9 .00 .00 13 14 16
"'°' 10 .00 .00 14 15
11 .00 .00 16 17 19
12 .00 .00 11 18
Aft 13 .00 .00 19 20 22
14 .00 .00 20 21
15 .00 .00 22 23 25
16 .00 .00 23 24
17 .00 .00 25 26 28
18 .00 .00 26 27
19 .00 .00 28 29 31
am 20 .00 .00 29 30
21 .00 .00 31 32 34
22 .00 .00 32 33
amn 23 .00 .00 34 35 37
24 .00 .00 35 36
25 .00 .00 37 38 40
26 .00 .00 38 39
°mpi 27 .00 .00 40 41 43
28 .00 .00 41 42
29 .00 .00 43 44 46
30 .00 .00 44 45
31 .00 .00 46 47 49
32 .00 .00 47 48
33 .00 .00 49 50 52
pm
34 .00 .00 50 51
35 .00 .00 52 53 55
36 .00 .00 53 54
""' 37 .00 .00 55 56 58
38 .00 .00 56 57
39 .00 .00 58 59 61

DATE a June 10 1995 PAGE NO. 4
JOB NAME a Capp Lejeune Diffuser 36 Ports 3.75 inch Ports 30 KGD
40 .00 .00 59 60
41 .00 .00 61 62 64
42 .00 .00 62 63
43 .00 .00 64 65 67
44 .00 .00 65 66
45 .00 .00 67 68 10
46 .00 .00 68 69
41 .00 .00 70 71 73
48 .00 .00 71 72
49 .00 .00 73 74 76
50 .00 .00 14 75
51 .00 .00 16 77 79
52 .00 .00 17 78
53 .00 .00 79 80 82
54 .80 .00 80 81
55. .00 .00 82. 83 85
56 .00 .00 83 84
51 .00 .00 85. 86 88
58 .00 .00 86 87
59 .00 .00 88 89 91
60 .00 .00 89 90
61 .00 .00 91 92 94
62 .00 .00 92 93
63 .00 .00 94 95 91
64 .00 .00 95 96
65 .00 .00 97 98 100
66 .00 .00 98 99
67 .00 .00 100 101 103
68 .00 .00 101 102
69 .00 .00 103 104 106
70 .00 .00 104 105
71 .00 .00 106 107
72 .00 .00 107 108
OUTPUT SELECTION: ALL RESULTS ARE OUTPUT EACH PERIOD
THIS SYSTEM HAS 108 PIPES WITH 72 JUNCTIONS , 0 LOOPS AND 37 YGSS
THE RESULTS ARE OBTAINED AFTER 4 TRIALS WITH AN ACCURACY = .00268
PIPE NO. NODE NOS. YLONRATE HEAD LOSS PUMP HEAD MINOR LOSS VELOCITY HLl1000
1 0 1 20106.69 2.80 .00 .15 3.13 .65
2 1 2 573.48 .05 .00 .37 3.66 7.57
3 2 0 573.48 .30 .00 12.92 16.66 302.95
4 1 3 19533.20 .01 .00 .07 3.04 .62

DATE = June 10 1995 . PAGE NO. 5
JOB KAKB = Catp Lejeune Diffuser 36 Ports 3.75 inch Ports .30 KGD
PEN
gib
5 3 4 571.84 .05 .00 .37 3.65 7.53
6 4 0 571.84 .30 .00 12.85 16.61 301.34
1 3 5 18961. 37 .01 .00 .07 2.95 .58
8 5 6 570,28 ,04 .00 .37 3.64 7.49
9 6 0 570.28 .30 .00 12.78 16.56 299.82
10 5 7 18391.09 .01 .00 .06 2.87 .55
11 7 8 568.81 .04 .00 .37 3.63 7.45
12 8 0 568.81 .30 .00 12.72 16.52 298.39
13 7 9 17822.28 .01 .00 .06 2.78 .52
14 9 10 567.43 .04 .00 .37 3.62 7.42
15 10 '0 567.43 .30 .00 12.65 16.48 297.05
.m 16 9 11 11254.85 .00 .00 .06 2.69 .49
17 11 12 566.13 .04 .00 .36 3.61 7.39
18 12 0 566.13 .30 .00 12.60 16.44 295.79
19 11 13 16688.73 .00 .00 .05 2.60 .46
20 13 14 564.91 .04 .00 .36 3.61 7.36
21 14 0 564.91 .29 .00 12.54 16.41 294.61
22 13 15 16123.82 .00 .00 .05 2.51 .43
23 15 16 563.76 .04 .00 .36 3.60 7.33
24 16 0 563.76 .29 .00 12.49 16.38 293.51
25 15 11 15560.06 .00 .00 .05 2.42 .41
Am26 17 18 562.70 .04 .00 .36 3.59 7.30
27 18 0 562.70 .29 .00 12.44 16.34 292.49
28 11 19 14997.36 .00 .00 .04 2.34 .38
29 19 20 561.71 .04 .00 .36 3.59 7.28
30 20 0 561.71 .29 .00 12.40 16.32 291.53
31 19 21 14435.65 .00 .00 .04 2.25 .35
32 21 22 560.79 .04 vi .36 3.58 1.26
Am 33 22 0 560.79 .29 .00 12.36 16.29 290.64
34 21 23 13874.86 .00 .00 .04 2.16 .33
35 23 24 559.93 .04 .00 .36 3.57 7.24
36 24 0 559.93 .29 .00 12.32 16.26 289.83
Am
37 23 25 13314.92 .00 .00 .03 2.07 .30
38 25 26 559.15 .04 .00 .36 3.57 7.22
39 26 0 559.15 .29 .00 12.29 16.24 289.07
"'° 40 25 27 12755.78 .00 .00 .03 1.99 .28
41 27 28 558.42 .04 .00 .35 3.56 7.20
42 28 0 558.42 .29 .00 12.25 16.22 288.38
ear 43 27 29 12197.35 .00 .00 .03 1.90 .26
44 29 30 557.76 .04 .00 .35 3.56 7.19
45 30 0 557.16 .29 .00 12.23 16.20 287.75
46 29 31 11639.59 .00 .00 .03 1.81 .24
Am 47 31 32 557.16 .04 .00 .35 3.56 7.17
48 32 0 557.16 .29 .00 12.20 16.18 287.17
49 31 33 11082.43 .00 .00 .02 1.73 .22
50 33 34 556.61 .04 .00 .35 3.55 7.16
51 34 0 556.61 .29 .00 12.18 16.17 286.65
52 33 35 10525.82 .00 .00 .02 1.64 .20
Am53 35 36 556.11 .04 .00 .35 3.55 7.15
54 36 0 556.11 .29 .00 12.15 16.15 286.17
55 35 31 9969.71 .00 .00 .02 1.55 .18
56 37 38 555.67 .04 .00 .35 3.55 7.14
"" 57 38 0 555.67 .29 .00 12.13 16.14 285.15
58 31 39 9414.04 .00 .00 .02 1.47 .16
59 39 40 555.27 .04 .00 .35 3.54 7.13

DATE . June 10 1995 PAGE NO. 6
JOB NAME = Caap Lejeune Diffuser 36 Ports 3.75 inch Ports 30 MGD
Inft
all
60 40 0 555.27 .29
61 39 41 8858.77 .00
62 41 42 554.92 .04
63 42 0 554.92 .29
64 41 43 8303.85 .00
65 43 44 554.61 .04
66 44 0 554.61 .28
67 43 45 7749.25 .00
68 45 46 554.34 .04
69 46 0 554.34 .28
70 45 41 7194.91 .00
11 47 48 554.10 .04
72 48 0 554.10 .28
73 47 49 6640.81 .00
74 49 50 553.90 .04
.75 50 0 553.90 .28
76 49 51 6086.90 .00
77 51 52 553.74 .04
78 52 0 553.74 .28
79 51 53 5533.17 .00
80 53 54 553.60 .04
81 54 0 553.60 .28
82 53 55 4979.57 .00
83 55 56 553.49 .04
84 56 0 553.49 .28
85 55 57 4426.08 .00
86 57 58 553.40 .04
87 58 0 553.40 .28
88 57 59 3872.69 .00
89 59 60 553.33 .04
90 60 0 553.33 .28
91 59 61 3319.36 .00
92 61 62 553.28 .04
93 62 0 553.28 .28
94 61 63 2766.08 .00
95 63 64 553.24 .04
96 64 0 553.24 .28
97 63 65 2212.84 .00
98 65 66 553.22 .04
99 66 0 553.22 .28
100 65 67 1659.62 .00
101 67 68 553.21 .04
102 68 0 553.21 .28
103 61 69 1106.41 .00
104 69 70 553.20 .04
105 70 0 553.20 .28
106 69 71 553.20 .00
107 71 72 553.20 .04
108 72 0 553.20 .28
.00 12.12 16.13 285.37
.00 .01 1.38 .14
.00 .35 3.54 7.12
.00 12.10 16.12 285.04
.00 .01 1.29 .13
.00 .35 3.54 7.11
.00 12.09 16.11 284.14
.00 .01 1.21 .11
.00 .35 3.54 7.10
.00 12.08 16.10 284.48
.00 .01 1.12 .10
.00 .35 3.54 7.10
.00 12.07 16.09 284.26
.00 .01 1.03 .08
.00 .35 3.54 7.09
.00 12.06 16.09 284.07
.00 .01 .95 .07
.00 .35 3.53 7.09
.00 12.05 16.08 283.91
.00 .01 .86 .06
.00 .35 3.53 7.09
.00 12.04 16.08 283.78
.00 .00 .78 .05
.00 .35 3.53 . 7.08
.00 12.04 16.08 283.67
.00 .00 .69 .04
.00 .35 3.53 7.08
.00 12.04 16.07 283.59
.00 .00 .60 .03
.00 .35 3.53 7.08
.00 12.03 16.07 283.53
.00 .00 .52 .02
.00 .35 3.53 7.08
.00 12.03 16.07 283.48
.00 .00 .43 .02
.00 .35 3.53 7.08
.00 12.03 16.07 283.45
.00 .00 .34 .01
.00 .35 3.53 7.08
.00 12.03 16.07 283.42
.00 .00 .26 .01
.00 .35 3.53 7.08
.00 12.03 16.07 283.41
.00 .00 .17 .00
.00 .35 3.53 7.08
.00 12.03 16.07 283.41
.00 .00 .09 .00
.35 3.53 7.08
.00 12.03 16.07 283.41
1, 1,
JUNCTION NUMBER DEMAND GRADE LINE ELEVATION PRESSURE
1 .00 14.65 1.00 5.91
2 .00 14.23 1.00 5.73
3 .00 14.57

DAB = June 10 1995 PAGE NO. 7
JOB NAME a Cup Lejeune Diffuser 36 Ports 3.75 inch Ports 30 MOD
4 .00 14.15
'°'°' 5 .00 14.50
6 .00 14.08
7 .00 14.43
00 8 .00 14.01
9 .00 14.36
10 .00 13.95
11 .00 14.30
12 .00 13.89
13 .00 14.24
14 .00 13.84
°"" 15 .00 14.19
16 .00 13.78
17 .00 14.14
18 .00 13.74
19 .00 14.09
20 .00 13.69
21 .00 14.05
00
22 .00 13.65
23 .00 14.01
24 .00 13.61
- 25 .00 13.97
26 .00 13.58
27 ,00 13.9.4
28 .00 13.54
29 .00 13.91
30 .00 13.51
31 .00 13.88
00 32 .00 13.49
33 .00 13.86
34 .00 13.46
AMA 35 .00 13.83
36 .00 13.44
37 .00 13.81
38 .00 13.42
00
39 .00 13.80
40 .00 13.40
41 .00 13.78
42 .00 13.39
43 .00 13.77
44 .00 13.37
00 45 .00 13.75
46 .00 13.36
41 .00 13.74
48 .00 13.35
49 .00 13.73
50 .00 13.34
51 .00 13.73
00 52 .00 13.33
53 .00 13.72
54 .00 13.33
55 .00 13.71
0510
56 .00 13.32
57 .00 13.71
58 .00 13.32

DAB = June 10 1995 PAGE NO. 8
JOB NAME = Cup Lejeune Diffuser 36 Ports 3.75 inch Ports 30 MGD
PIO
Mil
59 .00 13.71
60 .00 13.32
61 .00 13.70
62 .00 13.31
63 .00 13.70
64 .00 13.31.
65 .00 13.70
66 .00 13.31
67 .00 13.70
68 .00 13.31
69 .00 13.70
70 .00 13.31
71 .00 13.70
72 .00 13.31
m"' THE NET SYSTEM DEMAND = .00
SUMMARY OF INFLOft$(+) AND OUTFLOWS(-) FROM FIXED GRADE NODES
PIPE NUMBER FLOWRATE
1 20106.69
3-573.48
6-571,84
9 -570.28
12-568.81
me 15-567.43
18-566.13
21-564.91
�., 24 -563.76
27 562.70
30-561.71
33-560.79
36 -559.93
39-559.15
42-558.42
�•. 45-557.76
48-557,16
51-556.61
ram54-556,11
57-555.67
60-555.27
63-554.92
66 -554.61
69 -554, 34
72-554.10
nw 75 -553, 90
78-553.74
81-553.60
84-553.49
87-553.40
90-553.33
93-553.28
96 -553.24
99-553.22
102-553.21

DATE = June 10 1995 PAGE NO. 9
JOB NAME = .Caep Lejeune Diffuser 36 Ports 3.75 inch Ports 30 RGD
n
105
108
-553.20
-553.20
THE NET FLOW INTO THE SYSTEM FROM FIXED GRADE NODES . 20106.69
THE NET FLOW OUT OF THE SYSTEM INTO FIXED GRADE NODES =-20106.69

DATE = June 10 1995 PAGE NO. 1
JOB NAME = Capp Lejeune Diffuser 36 Ports 4 inch Ports 30 KGD
a. FLOWRATE IS EXPRESSED IN GPM AND PRESSURE IN PSIG
rart
MaII
NIM
A SUMMARY OF THE ORIGINAL DATA FOLLOWS
PIPE NO. NODE NOS. LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED GRADE
(FEET) (INCHES)
1 0 1 4300.0 51.2 120.0 1.00 17.60
2 1 2 6.0 8.0 120.0 1.80
3 2 0 1.0 4.0 120.0 3.00 1.00
4 1 3 10.0 51.2 120.0 .50
5 3 4 6.0 8.0 120.0 1.80
6 4 0 1.0 4.0 120.0 3.00 1.00
1 3 5 10.0 51.2 120.0 .50
8 5 6 6.0 8.0 120.0 1.80
9 6 0 1.0 4.0 120.0 3.00 1.00
10 5 7 10.0 51.2 120.0 .50
11 7 8 6.0 8.0 120.0 1.80
12 8 0 1.0 4.0 120.0 3.00 1,00
13 7 9 10.0 51.2 120.0 .50
14 9 10 6.0 8.0 120.0 1.80
15 10 0 1.0 4.0 120.0 3.00 1.00
16 9 11 10.0 51.2 120.0 .50
11 11 12 6.0 8.0 120.0 1.80
18 12 0 1.0 4.0 120.0 3.00 1.00
19 11 13 10.0 51.2 120.0 .50
20 13 14 6.0 8.0 120.0 1.80
21 14 0 1.0 4.0 120.0 3.00 1.00
22 13 15 10.0 51.2 120.0 .50
23 15 16 6.0 8.0 120.0 1.80
24 16 0 1.0 4.0 120.0 3.00 1.00
25 15 17 10.0 51.2 120.0 .50
26 17 18 6.0 8.0 120.0 1.80
27 18 0 1.0 4.0 120.0 3.00 1.00
28 17 19 10.0 51.2 120.0 .50
29 19 20 6.0 8.0 120.0 1.80
30 20 0 1.0 4.0 120.0 3.00 1.00
31 19 21 10.0 51.2 120.0 .50
32 21 22 6.0 8.0 120.0 1.80
33 22 0 1.0 4.0 120.0 3.00 1.00
34 21 23 10.0 51.2 120.0 .50
35 23 24 6.0 8.0 120.0 1.80
36 24 0 1.0 4.0 120.0 3.00 1.00
37 23 25 10.0 51.2 120,0 .50
38 25 26 6,0 8.0 120.0 1.80
39 26 0 1.0 4.0 120.0 3.00 1.00
40 25 27 10.0 51.2 120.0 .50

DATE = June 10 1995 PAGE NO. 2
JOB NAME = Canp hejeune Diffuser 36 Ports 4 inch Ports 30 KGD
41 27 28 6.0 8.0 120.0 1.80
42 28 0 1.0 4.0 120.0 3.00 1.00
43 27 29 10.0 51.2 120.0 .50
44 29 30 6.0 8.0 120.0 1.80
45 30 0 1.0 4.0 120.0 3.00 1.
46 29 31 10.0 51.2 120,0 .50
47 31 32 6.0 8.0 120.0 1.80
48 32 0 1.0 4.0 120.0 3.00 1.00
49 31 33 10.0 51.2 120.0 .50
50 33 34 6.0 8.0 120.0 1.80
51 34 0 . 1.0 4.0 120.0 3.00 •1.00
52 33 35 10.0 51.2 120.0 .50
53 35 36 6.0. 8.0 120.0 1.80
54 36 0 1.0 4.0 120.0 3.00 1.00
55 35 37 10.0 51.2 120.0 .50
56 37 38 6.0 8.0 120.0 1.80
57 38 0 1.0 4.0 120.0 3.00 1.00
58 37 39 10.0 51.2 120.0 .50
59 39 40 6.0 8.0 120.0 1.80
60 40 0 1.0 4.0 120.0 3.00 1.00
61 39 41 10.0 51.2 120.0 .50
62 41 42 6.0 8.0 120.0 1.80
63 42 0 1.0 4.0 120.0 3.00 1.00
64 41 43 10.0 51.2 120.0 .50
65 43 44 6.0 8.0 120.0 1.80
66 44 0 1.0 4.0 120.0 3.00 1.00
67 43 45 10.0 51.2 120.0 .50
68 45 46 6.0 8.0 120.0 1.80
69 46 0 1.0 4.0 120.0 3.00 1.00
70 45 47 10.0 51.2 120.0 .50
71 47 48 6.0 8.0 120.0 1.80
72 48 0 1.0 4.0 120.0 3.00 1.00
73 47 49 10.0 51.2 120.0 .50
74 49 50 6.0 8.0 120.0 1.80
75 50 0 1.0 4.0 120.0 3.00 1.00
76 49 51 10.0 51.2 120.0 .50
77 51 52 6.0 8.0 120.0 1.80
78 52 0 1.0 4.0 120.0 3.00 1.00
79 51 53 10.0 51.2 120.0 .50
80 53 54 6.0 8.0 120.0 1.80
81 54 0 1.0 4.0 120.0 3.00 1.00
82 53 55 10.0 51.2 120.0 .50
83 55 56 6.0 8.0 120.0 1.80
84 56 0 1.0 4.0 120.0 3.00 1.00
85 55 57 10.0 51.2 120.0 .50
86 57 58 6.0 8.0 120.0 1.80
87 58 0 1.0 4.0 120.0 3.00 1.00
88 57 59 10.0 51.2 120.0 .50
89 59 60 6.0 8.0 120.0 1.80
90 60 0 1.0 4.0 120.0 3.00 1.00
91 59 61 10.0 51.2 120.0 .50
92 61 62 6.0 8.0 120.0 1.80
93 62 0 1.0 4.0 120.0 3.00 1.00
94 61 63 10.0 51.2 120.0 .50
95 63 64 6.0 8.0 120.0 1.80

DATE = June 10 1995 PAGE NO. 3
JOB NAME Cann Lejeune Diffuser 36 Ports 4 inch Ports 30 KGD
Ole
96 64 0 1.0 4.0 120,0 3.00 1.00
97 63 65 10.0 51.2 120.0 .50
98 65 66 6.0 8.0 120.0 1.80
99 66 0 1.0 4.0 120.0 3.00 1.00
100 65 67 10.0 51,2 120.0 .50
101 67 68 6.0 8.0 120.0 1.80
102 68 0 1,0 4.0 120.0 3.00 1.00'
103 67 69 10.0 51,2 120.0 .50
104 69 70 6.0 8.0 120.0 1.80
105 70 ' 0 1.0 4.0 120.0 3.00 1.00
106 69 71 10.0 51.2 120.0 .50
107 71 72 6.0 8.0 120.0 1.80
108 72 0 1.0 4.0 120.0 3.00 1.00
AM JUNCTION NUMBER DEMAND ELEVATION CONNECTING PIPES
1 .00 1.00 1 2 4
2 .00 1.00 2 3
M 3 .00 .00 4. 5 7
4 .00 .00 5 6
5 .00 .00 7 8 10
6 .00 .00 8 9
"" 7 .00 .00 10 11 13
8 .00 .00 11 12
9 .00 .00 13 14 16
com 10 .00 .00 14 15
11 .00 .00 16 17 19
12 .00 .00 17 18
13 .00 .00 19 20 22
444
14 .00 .00 20 21
15 .00 .00 22 23 25
16 .00 .00 23 24
mem 17 .00 .00 25 26 28
18 .00 .00 26 27
19 .00 .00 28 29 31
04, 20 .00 .00 29 30
21 .00 .00 31 32 34
22 .00 .00 32 33
23 .00 .00 34 35 37
0" 24 .00 .00 35 36
25 .00 .00 37 38 40
26 .00 .00 38 39
mon 27 .00 .00 40 41 43
28 .00 .00 41 42
29 .00 .00 43 44 46
,,,a 30 .00 .00 44 45
31 .00 .00 46 47 49
32 .00 .00 47 48
33 .00 .00 49 50 52
AM
34 .00 .00 50 51
35 .00 .00 52 53 55
36 .00 .00 53 54
04 37 .00 .00 55 56 58
38 .00 .00 56 57
39 .00 .00 58 59 61

DATE = June 10 1995 PAGE NO. 4
JOB MAHE = Cup Lejeune Diffuser 36 Ports 4 inch Ports 30 MGD
40 .00 .00 59 60
41 .00 .00 61 62 64
42 .00 .00 62 63
43 .00 .00 64 65 61
44 .00 .00 65 66
45 .00 .00 67 68 10
46 .00 .00. 68 69
47 .00 .00 10 11 73
48 .00 .00 11 72
49 .00 .00 73 74 76
50 .00 .00 74 75
51 .00 .00 76 77 79
52 .00 . .00 17 78
53 .00 .00 79 80 .82
54 .00 .00 80 81
55 .00 .00 82 83 85
56 .00 .00 83 84
57 .00 .00 85 86 88
58 .00 .00 86 81
59 .00 .00 88 89 91
60 .00 .00 89 90
61 .00 .00 91 92 94
62 .00 .00 92 93
63 .00 .00 94 95 97
64 .00 .00 95 96
65 .00 .00 97 98 100
66 .00 .00 98 99
67 .00 .00 100 101 103
68 .00 .00 101 102
69 .00 .00 103 104 106
10 .00 .00 104 105
11 .00 .00 106 107
72 .00 .00 107 108
OUTPUT SELECTION: ALL RESULTS ARE OUTPUT EACH PERIOD
THIS SYSTEM HAS 108 PIPES WITH 72 JUNCTIONS , 0 LOOPS AND 37 YGNS
THE RESULTS ARE OBTAINED AFTER 4 TRIALS KITH AN ACCURACY = .00155
PIPE NO. NODE NOS. FLOKRATE BEAD LOSS PUMP HEAD MINOR LOSS VELOCITY HL/1
1 0 1 22142.64 3.35 .00 .18 3.45 .78
2 1 2 636.10 .05 .00 .46 4.06 9.17
3 2 0 636.10 .27 .00 12.28 16.24 268.05
4 1 3 21506.54 .01 .00 .09 3.35 .74

DATE r June 10 1995 PAGE O. 5
JOB NAKB . Cup Lejeune Diffuser 36 Ports 4 inch Ports 30 KGD
5 3 4 633.79 .05 .00 .46 4.05 9.10
6 4 0 633.79 . .27. .00 12.19 16.18 266.25
7 3 5 20872.74 .01 .00 .08 3.25 .70
8 5 6 631.61 .05 .00 .45 4.03 9.05
9 6 0 631.61 .26 ..00 12.11 16.12 264.56
10 5 7 20241.14 .01 .00 .08 3.15 .66
11 7 8 629.55 .05 .00 .45 4.02 8.99
12 8 0 629.55 .26 .00 12.03 16.07 262.96
13 7 9 19611, 59 .01 .00 .07 3.06 .62
14 9 10 627.60 .05 .00 .45 4.01 8.94
15 10 0 627.60 .26 .00 11.96 16.02 261.46
16 9 11 18983.99 .01 .00 .07 2.96 .59
11 11 12 625.78 .05 .00 .45 3.99 8.89
18 12 0 625.78 .26 .00 11.89 15.98 260.05
19 11 13 18358.21 .01 .00 .06 2.86 .55
20 13 14 624,06 .05 .00 .4t 3.98 8.85
21 14 0 624.06 .26 .00 11.82 15.93 258.73
22 13 15 17734.15 .01 .00 .06 2.76 .52
23 15 16 622.46 .05 .00 .44 3.97 8.81
24 16 0 622.46 .26 .00 11.76 15.89 257.50
25 15 17. 17111. 69 .00 .00 .06 2.67 .48
26 17 18 620.96 .05 .00 .44 3.96 8,77
21 18 0 620.96 .26 .00 11.71 15.85 256.36
28 17 19 16490. 73 .00 .00 .05 2.57 .45
29 19 20 619.57 .05 .00 .44 3.95 8.73
30 20 0 619.57 .26 .00 11.65 15.82 255.29
31 19 21 15871.16 .00 .00 .05 2.47 .42
32 21 22 618,27 .05 .00 .44 3.95 8.70
33 22 0 618.27 .25 ,00 11.60 15.78 254.30
34 21 23 15252.89 .00 .00 .04 2.38 .39
35 23 24 617.07 .05 .00 .43 3.94 8.67
36 24 0 617.07 .25 .00 11.56 15.75 253.39
37 23 25 14635.82 .00 .00 .04 2.28 .36
38 25 26 615.97 .05 .00 .43 3.93 8.64
39 26 0 615.97 .25 .00 11.52 15.73 252.55
40 25 21 14019.85 .00 .00 .04 2.18 .33
41 27 28 614.95 .05 .00 .43 3.92 8.61
42 28 0 614.95 .25 .00 11.48 15.70 251.78
43 27 29 13404.90 ,00 .00 .03 2.09 .31
44 29 30 614.01 .05 .00 .43 3.92 8.59
45 30 0 614.01 .25 .00 11.45 15.68 251.07
46 29 31 12790.89 .00 .00 .03 1.99 .28
47 31 32 613,16 .05 .00 .43 3.91 8,56
48 32 0 613.16 .25 .00 11.41 15.65 250.43
49 31 33 12177.73 .00 .00 .03 1.90 .26
50 33 34 612.39 .05 .00 .43 3.91 8.54
51 34 0 612.39 .25 .00 11.38 15.63 249.84
52 33 35 11565.33 .00 .00 .03 1.80 .23
53 35 36 611.69 .05 .00 .43 3.90 8.53
54 36 0 611.69 .25 .00 11.36 15.62 249.31
55 35 37 10953.64 .00 .00 .02 1.71 .21
56 37 38 611.07 .05 .00 .43 3.90 8.51
57 38 0 611.07 .25 .00 11.34 15.60 248.84
58 37 39 10342.58 .00 .00 .02 1.61 .19
59 39 40 610.51 .05 .00 .42 3.90 8.50

DATE = June 10 1995 PAGE NO. 6
JOB NAME = Caap Lejeune Diffuser 36 Ports 4 inch Ports 30 MGD
NMI
Fact
PIN
ala
MEI
OEM
60 40 0 610.51 .25 .00 11.31 15.59 248.42
61 39 41 9732.07 .00 .00 .02 1.52 .17
62 41 42 610.01 .05 .00 .42 3.89 8.48
63 42 0 610.01 .25 .00 11.30 15.57 248.05
64 .41 43 9122.06 . .00 .00 .02 1.42 .15
65 43 44 609.57 .05 .00 .42 3.89 8.47
66 44 0 609.57 .25 .00 11.28 15.56 247.72
67 43 45 8512.49 .00 .00 .01 1.33 .13
68 45 46 609.19 .05 .00 .42 3.89 8.46
69 46 0 609,19 .25 .00 11.27 15.55 247.43
70 45 47 7903.30 .00 .00 .01 1.23 .12
71 47 48 608.86 .05 .00 .42 3.89 8.45
72 48 0 608.86 .25 .00 11.25 15.54 247.18
73 47 49 7294.44 .00 .00 .01 1.14 .10
74 49 50 608.58 .05 .00 .42 3.88 8.45
75 50 0 608.58 .25 .00 11.24 15.54 246.97
76 49 51 6685.86 .00 .00 .01 1.04 .08
77 51 52 608.34 .05 .00 .42 3.88 8.44
78 52 0 608.34 .25 .00 11.23 15.53 246.79
19 51 53 6077.51 .00 .00 .01 .95 .07
80 53 54 608.15 .05 .00 .42 3.88 8.43
81 54 0 608.15 .25 .00 11.23 15.53 246.65
82 53 55 5469.36 .00 .00 .01 .85. .06
83 55 56 607.99 .05 .00 .42 3.88 8.43
84 56 0 607.99 .25 .00 11.22 15.52 246.53
85 55 57 4861.38 .00 .00 .00 .76 .05
86 57 58 607.86 .05 .00 .42 3.88 8.43
87 58 0 607.86 .25 .00 11.22 15.52 246.43
88 57 59 4253.51 .00 .00 .00 .66 .04
89 59 60 607.77 .05 .00 .42 3.88 8.42
90 60 0 607.77 .25 .00 11.21 15.52 246.36
91 59 61 3645.74 .00 .00 .00 .57 .03
92 61 62 607.70 .05 .00 .42 3.88 8.42
93 62 0 607.70 .25 .00 11.21 15.51 246.31
94 61 63 3038.05 .00 .00 .00 .47 .02
95 63 64 607.65 .05 .00 .42 3.88 8.42
96 64 0 607.65 .25 .00 11.21 15.51 246.27
97 63 65 2430.40 .00 .00 .00 .38 .01
98 65 66 607.62 .05 .00 .42 3.88 8.42
99 66 0 607.62 .25 .00 11.21 15.51 246.25
100 65 67 1822.78 .00 .00 .00 .28 .01
101 67 68 607.60 .05 .00 .42 3.88 8.42
102 68 0 607.60 .25 .00 11.21 15.51 246.23
103 67 69 1215.18 .00 .00 .00 .19 .00
104 69 10 607.59 .05 .00 .42 3.88 8.42
105 70 0 607.59 .25 .00 11.21 15.51 246.23
106 69 71 607.59 .00 .00 .00 .09 .00
107 71 72 607.59 .05 .00 .42 3.88 8.42
108 12 0 607.59 .25 .00 11.21 15.51 246.23
JUNCTION NUMBER DEMAND GRADE LINE ELEVATION PRESSURE
am 1 .00 14.07 1.00 5.66
2 .00 13.55 1.00 5.44
3 .00 13.97

DATE = June 10 1995 . PAGE O. 7
JOB BAKE = Caip Lejeune Diffuser 36 Ports 4 inch Ports 30 KGD
4 .00 13.46
5 .00 13.88
6 .00 13.38
7 .00 13.80
8 .00 13.29
9 .00 13.72
10 .00 13.22
11 .00 13.65
12 .00 13.15
13 .00 13.58
14 .00 13.08
15 .00 13.51
16 .00 13.02
17 .00 13.45
18 .00 12.96
19 .00 13.40
20 .00 12.91
21 .00 13.35
22 .00 12.86
23 .00 13.30
24 .00 12.81
25 .00 13.25
26 .00 12.77
27 .00 13.21
28 .00 12.73
29 .00 13.18
30 .00 12.70
31 .00 13.14
32 .00 12.66
33 .00 13.11
34 .00 12.63
35 .00 13.09.
36 .00 12.61
37 .00 13.06
38 .00 12.58
39 .00 13.04
40 .00 12.56
41 .00 13.02
42 .00 12.54
43 .00 13.00
44 .00 12.53
45 .00 12.99
46 .00 12.51
47 .00 12.97
48 .00 12.50
49 .00 12.96
50 .00 12.49
51 .00 12.95
52 .00 12.48
53 .00 12.95
54 .00 12.47
55 .00 12.94
56 .00 12.47
57 .00 12.93
58 .00 12.46

DATE = June 10 1995 PAGE NO. 8
JOB HAKE = Cup Lejeune Diffuser 36 Ports 4 inch Ports 30 KGD
59 .00 12.93
60 .00 12.46
61 .00 12.93
62 .00 12.46
63 .00 12.93
64 . .00 12.46
65 .00 12.93
66 .00 12.45
67 .00 12.92
68 .00 12.45
69 .00 12.92
70 .00 12.45
71 .00 12.92
72 .00 12.45
THE NET SYSTEM DEMAND = .00
SUMMARY OF IfFLONS (+) AND OUTFLOWS(-) FROM FIXED GRADE NODES
PIPE NUMBER FLOWRATE
1 22142.64
3-636.10
6-633.79
9-631.61
12-629.55
15-627.60
18-625.78
21-624.06
24-622.46
21-620.96
30-619.57
33-618.27
36-617.01
39-615.97
42-614.95
45-614.01
48-613.16
51-612.39
54-611.69
51-611.07
60-610.51
63-610.01
66-609.57
69-609.19
72-608.86
75-608.58
78-608.34
81-608.15
84-601.99
87-607.86
90-607.77
93-607.70
96 -607, 65
99-607.62
102-607.60

DATE = June 10 1995 • PAGE NO. 9
JOB MAHE = Cup Lejeune Diffuser 36 Ports 4 inch Ports 30 KGD
7
7
r1
n
105 -607.59
108 -607.59
THE HET FLOW INTO THE SYSTEM FROM FIXED GRADE BODES = 22142.64
THE NET FMB OUT OF THE SYSTEM INTO FIXED GRADE NODES =-22142.64