CF-Village-SP 980821 I
Pan-Tech Controls Co.
FRANK CLARK
I..... 2401 AVE. J, SUITE 200 METRO 817/640-3232
ARLINGTDN, TX 76006-6118 FAX 817/849-7933
CONSULTING ENGINEERS
Gary C. Hendricks, P.E.
Date: ~/~~
I
I-._ BadgerMeter
~ ·
r SU BM I ~ ~ AL DATA
I
F
r-
Badger Meter, Inc.
P.O. Box 581390
Tulsa, Oklahoma 741 58
(918) 836-8411
Telex: RCA 203605
I FLOW ELEMENTS SHEET I OF 1
IN~ IBY IDATEI REVISION SPEC: 13110
FLOW TUBES i ! i I CONTRACT: COPPELL
I I ! ! DATE:
! ! !
i ! ! ! P.O. .COPEL12
! i I ! B'~ :MR~
TYPE: VENTURI FLOW TUBE
SIZE: 56 INCH
BODY MTL.: CARBON STEEL
THROAT MTL.: 504 SS
ANNULAR CHAMBER: NO
THROAT DIAMETER: BELOW
MFG. TO CALCULATE DELTA-PRESS.: YES
FLOW RANGE: BELOW
MFG: BADGER
MODEL: BVT-U
F
LINE THROAT FLOW DELTA
F T.A~......NO.,. S.~..~E D..~..~ .............. R~.~.G.~ ER.E.SS.~. ~.~B.~.~ ~OCA.Z.!..~.N.
FE-4 5~" 15.565'" 0-20 MGD O-lO0" STAT. FLOW '¥PS VAULT
F
F
TULSA. OKLAHOMA 74158-1009 PC.' ~'[ / /~/[/~" /
1918) 836-8411 · TELEX: RCA 203605 D I F FERENT I AL ELEMENT
PRIMARY DATA/CALCUI_ATION SHEET
WATER CALCULATION - VOLUMETRIC FLOW
ENGLISH UNITS
n DATE 07FEB89
--' BADGER S. 0. NO. 942210
CUSTOMER GAR I CO
F CUSTOMER P.O. NO. 890.5-A 1-SB
USER CITY OF COPPELL, TX
' ' CONSULTING ENGR. GINN INC
n BADG'ER VENTURI DATA
BADGER VENTURI STYLE BVT-U SERIAL NO. c~4--... 1 .
NOMINAL SIZE 56 TAG
n THROAT DIA (IN.) 15.565 BODY MATERIAL CARBON STEEL
BETA RATIO .451 THROAT M,-.TE,~.IAL S504
TAP SiZE 1/2" FLANGE MATERIAL CARBON-STEEL
r TAP LOCATION iNTEGRAL
DIFFERENTIAL PRESSURE IS 1AO INCHES WAFER AT 20 MGD.
PR,__=URE IS 19.¢1 % OF DIFFERENTIAL.
? PERMANENT -,~mc -- LOSS
! PERMANENT PRESSURE LOSS IS 19.41 INCHES OF WATER AT 20
FLUID DATA
n FLU i D WATER OPER. SP. GR. l. 00055
' OPER. PRES. (PSIA) 125 BASE SP.GR. 1.0A055
OF'ER. TEMP. (F) 60 OPER. VISC. (CP) 1. i 19
n BASE TEMP. (F) ~0
FLOW DATA
MAX.FLOW (MGD) 20 PIPE REYNOLDS NO. 1156589.
r NORM. FLOW (MGD) 14 P IF'E P, EYNOLDS NO. 795472
CUSTOMER PIPELINE & FLANGE DATA
r NOM. PIPE SIZE 56 PIPE MATERIAL METAL
PIPE SCHED/CLASS UNKNOWN PIPE I.D. 54.5
FLANGE TYPE AWWA FLANGE RATING CL D
F
[ . APPLI CABLE DOCUMENTS:
I NSTALLAT I ON/APPROVAL PRODUCT I ON
REFERENCE: FLOW METER ENGINEERING HANDBOOK, C.F.CUSICK, ~SRD ED., 1961
n CERTIFIED CORRECT BY: DATE:
PREPARED BY :CD
F
ALL PROPRIETARY RIGHTS IN THE SUBJECT MATTER SHOWN ARE EXCLUSIVE PROPERTY OF BADGER METER. INC.
~ Box 581390
~L$~ OK~HOMA 74158-1009
(918) 836-8411 · TELEX: R~ 203605 D I FFERENT I AL ELEMENT
F SUPPLEMENTARY DATA SHEET
WATER CALCULATION - VOLUMETRIC FLOW
ENGLISH UNITS
n DATE 07FEB89
BADGER S.O.NO. 942210
CUSTOMER GARICO
nCUSTOMER P.O.NO. 8905-01-SB
USER CITY OF COPPELI_, TX
CONSULTING ENGR. GINN INC
n BAD~ER VENTURI DATA
BADGER VENTURI STYLE BUT-U SERIAL NO. 942210
NOMINAL SIZE 56 TAG
WORKING EQUATION FOR LIQUID FLOW
? GAL/HR AT BASE TEMPERATURE
QGH=340.11 (S) (FA> (D2> (FHM) (FGB) (FGF) ~ (EQ 15~ PG 95)
QGH = 8.33555 FHM = 10
S = .20592 FGB = .999~4
FA = .99984 FGF = 1.0001'7
F D2 = 1190.25
n REYNOLDS NO. EQUATION FOR LIQUID FLOW
GAL/HR AT BASE TEMPERATURE
nRD=52.654(QGHA)(GB)/(D) (U)~ . (ED 20, PS'97)
QGHA = 585553 D = 54.5
GB = 1.00055 U = 1.11957
DISCHARGE COEFFICIENT =.99078
ALL PROPRIETARY RIGHI~ IN THE SUBJECT MATTER SHOWN ARE EXCLUSIVE PROPERTY OF BADGER METER, INC.
P.O. BOX581390 BVT-U BADGER VENTURI TUBE
6116 F.A~T 15th STREET'
TULSA, OKLAHO MA 74158-100g
(918) 836-8411 · TELEX: RCA 203605 I NSTAI._LAT I ON D I MENS I 0NS
AND
MATER IALS OF CONSTRUCTION
(USE WITH DRAWING NO. CD-951085 Iss. o. 1)
DATE 07FEB89
BADGER S.O. NO. 942210
CUSTOMER GAR I CO
CUSTOMER P.O. NO. 8905-O!-SB
TX
USER CiTY OF COPPELL ... ,
CONSULTING ENSR. GINN INC -"
PRIMARY ELEMENT .54.5 X 15.565 BVT-U STYLE BADSER VENTURi
SERIAL NO(S) 942210
TAG INFO.
DESIGN DATA:
PRESSURE (PSIG) 12.5 ALLOWABLE STRESS <PSI) 10500
TEMPERATURE DEG. F. ~t,O CORROSION ALLOW ~IN) 0.000
MATERIAL/FINISH SPECIFICATIONS:
ENT.~EST. C/S - ASTM A285 OR A569 (OR EQUAL.)/AMERCOAT
S~'iNNING C/S - ASTM A285 OR A569 (OR EOUAL)/AMERCOAT 66
~' ' TYPE 504 (OR EQUAL~.-"PLAIN
THROAT S/S - ASTM A~79 OR A,~U, ,
E×IT CONE C/S - ASTM A2~5 OR A569 (OR E~UAL)/AMERCOAT
BUSHING S/S - AS'TM A479 OR A240~ TYPE 304 (OR EQUAL) /PLAIN
PRES.CONN. C/S - ASTM A!05 GR II OR A181 (OR EQUAL)/Ai'fiERCOAT 66
PLATE FLG. C/S - ASTM A285 GR C OR A515 GR 70 (OR EQUAL)/AMERCOAT 66
WELD I N~ SPEC I F I CAT IONS AND D I MENS I ONS
SBB =12I SBT =108 SOB =121 SFB =!21
BODY D I MENS i ONS:
A = 54.500 B = 15.565 C = .54.50 E = 5.17 F = 26.5
G = 11!.1 P = .575 R = 7.5 T = .216
FLANGE DIMENSIONS FLANGE RATING, (J) = CL D
H = 3&. K = 46.00 L = .~-"..5'~ M = i.625 N = 42.75A
U '= 1.62 V = 1.62
PRESSURE CONN. (THREADED) 1/2-14 NPT 3000 .ff, RATING'
QUANT I TY LOCAT I ON (DEGREES >
HIGH 1
LOW 1 90
TOLERANCES 5 PLACE DIMENSIONS +/- 0.001 IN/IN BUT NOT LESS THAN +/-0.005
2 PLACE DIMENSIONS +/- 0.002 IN/IN BUT NOT LESS THAN +/-0.0.50
1 PLACE DIMENSIONS +/- 0.00.5 IN/IN BUT NOT LESS THAN +/-0.100
ALL PROPRIETARY RIGHTS IN THE SUBJECT MATTER SHOWN ARE EXCLUSIVE PROPERTY OF BADGER METER. INC.
F P.O. BOX 581390
6116 EAST 15th STREET
; TULSA, OKLAHOMA 74158-1009
;918) 836-8411 · TELEX: RCA 203605 D I FFERENT I AL METER
F FLOW VS DIFFERENTIAL CALCULATIONS
ENGI_ I SH UN I TS
BADGER S.O. 942210
r- DATE 07FEB8C?
I
: - CUSTOMER GAR I CO
E~_EMENT 54.500 X 1=.j.565 BADGER VENTURI
t" SERIAL N:] (S) 9~,2210
[. TAG INFO.
m' FLU I D WATER THROAT I.D. ( I N > 15. 56305
: OPER.TEMP. (F) 60.000 PIPE I.D. (IN) 54.5¢)000
OPER.PRES. (PSIA) 125.0000
n RESOLUTION 1.000 PERCENT OF MAXIMUM
· - DIFF.UNITS INCHES OF 68F WATER
F' FLOW D IFF FLOW D IFF FLOW D l FF FLOi4 D I Fi=
i (MSD> (IN) (MGD) (IN> (MOD> (IN> (MGD) ( IN>
n 20.00 100.0 19.80 98.01 1'9.60 96.0:,£ lC?. 40 94.09
19.20 92. 15 19.00 90.24 18.80 88.55 18.60 86.49
18.40 84.64 18.20 82.81 I8.00 81.00 i7.80 79.2!
,,,-. 17.60 77.4.'5, 17.40 75.68 !7 .20 "'"'x ..~. 95 ~'"'~. . O0 -'x -;..,, -. ~5.:: -.
~ 16.80 70.56 16.60 68.89 16.40 67.24 16.2~1> 65.61
16.00 65.99 15.80 62.40 15.60 6(i).8.5 ~.. 5.40 59. ~?,.
15.20 57.76 15.00 56..-'"5 14 .80 54 .76 14.6(i> 5,5·. 28
? 14.40 51.85 14.20 50.40 14.0A ~,9.00 '! .5.80 47.61
! 15.60 46.24 1.5.40 44.89 1.5.20 4.5.56 !5.00 4-2.24
12.80 40.95 12.~0 59.~8 12.40 38.44 12.20 57.21
? 12.00 56.00 11.80 .'54.81 11 60 5.5.64 11 4¢> ~..'. 48
11.20 .31.55 !1.00 .50.24 10.80 29. i6 10.60 28.09
10.40 27.04 10.20 26.01 10.00 25. A0 9.80(') 24.00
.,- 9.6(110 2'.5'. 04 9. 400 22.09 o,. 200 21. 16 9.00(] 20.25. ·
i 8. 800 19.56 8. 600 I8.49 8. 400 17.64 8. 200, !6.81
8. 000 1~. 00 7. 800 15.21 7. &O0 14.44 7. 400 1.5.69
7.200' 12.96 7.000 12.25 6,800 11.56 6.600 10.89
F- 6. 400 10.24 6. 200 9.610 6. 000 9. 000 5. 800 8.410
5. 600 7. 840 5. 400 7. 290 5. ~00 6. 760 5. 000 6. 250
4. 800 5. 760 4. 600 5. 290 4. 400 4. 840 4. 200 4. 410
~'. 4. 000 4. 000 5. 800 .5. 610 .5. 600 ~.~ 240 .5. 400 -.-."' 890
! 5. 200 2.5~0 3. 000 2. 250 2.800 1. 960 2. 600 1. 690
2. 400 I. 440 2. 200 1.210 2. 000 1. 000
ALL PROPRIETARY RIGHTS IN THE SUBJECT MATTER SHOWN ARE EXCLUSIVE PROPERTY OF BADGER METER, INC.
Badger Meter,
(~116 East 15th Street
Tulsa, Oklahoma 74158 (91'6) 836-8411
[-
INSTALLATION AND OPERATING INSTRUCTIONS FOR PRIMARY ELEMENTS
F -A. INSTALLATION
F- 1. General
[ Care must be exercised in installing flow elements. Although some.
elements are massive in appearance it must be remembered that they
~ are precision measurement devices and should be treated as such.
2. Lifting or Hoisting
a. Lift Trucks
Work only from the side of the primary element, never from the
end. Do not insert blade of fork lift into the primary element.
Do not roll the primary element.
b. Slings
Belt or chain slings are to be used only around the outside ot~
r- the primary element. Under no circumstances should the belt or
chain be passed through the interior of the primary element.
Use spreader bars when recommended. Use of hooks inserted into
F' flange bolt holes is not recon~nended.
c. Lifting Eyes
~ For large inser.t type primary elements it is reconeended that a
~ threaded eye bolt be screwed into the upper pressure tap hole
r- and the primary element lifted into place using this eye bolt.
I Remove eye bolt after primary element is securely bolted 'into
' pl ace.
F It is recommended that all full form style primary elements
, (e.g. PMT-U, PVFS) weighing over 50 pounds be ordered equipped
-' with lifting eyes and that these eyes be used with chain falls
r- and shackles when hoisting.
F
3. Ortentetton
;r- Pressure taps are marked Ht & Low. Refer to the tnstellatton draw-
~ lng for co~ect orientetton. A large arro~ (etther cast, stenciled,
or on a stainless steel nameplato) denotes flow direction.
F Before flanged untts are finally bolted down be sure the gaskets-
are properly pos. ttioned so no interference occurs within the flow
F stream.
Buttweld or plain end units should be carefully positioned both ID
and OD and properly supported until weldtng or end connections are
F sufficiently secure prevent
mtsal
ignments.
B. OPERATION
F 1. Primary differential producing elements are essentially passive
pieces of equipment. Consequently, their performance is a product
,r- of the appl t cart on.
2. The .pipe line should be cleaned at startul~ to prevent dirt from
F' entering the pressure taps. ..
3. Transmitter lines should be similarly cleaned and checked for leaks.
F4. In horizontal pipe runs the primary element should be installed such
· that the pressure connections are in a horizontal line.
F 5. Suspected measurement errors should be investigated starting at the
- receiver section and traced toward the primary element. Very rarely
does the malfunction originate within the primary element.
'F
F
SIGNATURE %
V "~"~ FLOW-RATE
TRANSMITTER SPECIFICATION SUMMARY SHEET B225-33
MODEL NUMBER SPECI~CA~ON
2408-33B.ABC-DEF-GHJ-KO0
~. INPUT RANGE E. F~NGE BOLT MATERIAL
~ ~ ~12~ ~O *S~nle~ Steel 17~ PH .............................. 2
~12~ ~0-72~ ~ ....................... 4 I~SS.S.~Kyn~B~ ......................... 0'
0-25 ~ 0-1~ p~d ......................... 5 F, ~LUNG MEDIUM
0-~ to0-~ prod .........................
0~ to 0-~ ~ 2~ Sil~ne .........................................
H~O
9
0-10 ~ 0-~ psid ......................... ......................... 0 ~uorolu~e .................................................... 2
OUTPUT SIGNAL
B. ~A~C PRESSURE RA~NG G'
1~ p~ (Range 2 ~) .............................. 1 Pm~on~toV~ ....................................
2~ ~i (Range 0,3.4.5.9) ....................... ~ H, LOCAL INDICA~ON
~ ~i (R~ge 0,3.4.5.9) .......................... 3 None ................................................ 0
13~ psi (R~ge 6 onN) .............................. 4 0-1~% Une~ Meter~G~.~ ........
~ psi (Range 0.2.3,4.5.9)
(Kynar ~ge oAly) ....................... ~ J, MOUN~NG BRAC~
N~e ..................................................... , ...... O"
C DIAPHRAGM MATERIAL ............................. 1 UnNem~ ~ Pipe Mount .........................
316 St~nle~ St~ ................................... ~ Un~a ~ Pipe ~unt for Kyn~ .......... 3
*Hutell~ C .................................................. 3 Univemal ~ Pipe Mount for R~ge 6 ..........
~ ........................................................... 4 Note 1 ~ Pi~e Mount w/90 ~qree rota~on ......... 6
T~taum ...................................................... 5 Note 1 ~ RaUPipe Mount ..................................... 7
D. PROCESS ~NGE & CONNEC~ON
BLOC~ MA~RIAL ~. CER~RCA~ON
C~mlum Plat~ C~A S~eel ................. ~ None ........................................................
~16 Stanless SI~I ...................................... 2 F.M. Appmv~
H~tel~y C .................................................. 3 ~pl~np~f/Dust Igni~on Proof ......... 1'
M~ ........................................................... 4 F.M. App~
Intdn~N Safe ...................................... 2
Kyn~ ........................................................... 6 CSA App~
Note 2 Aluminum .................................................. 7 ~plosionpmof ......................................... 3
Note 2 316 S~ni~ Stol ...................................... 8
'Required to meet N.A.C.E. specification MR41-75
~RRIERS FOR USE WI~ SIGNA~RE ~S~S FOR
IN~INSI~Y ~FE ~PLICA~
N~ 2= FOR ~ S~ A~TS ~10 E AL11 ONLY. ~~ I ~ I A 8 C 0
~ & ~ 31~, 31~47 x x x x
s~ 11~1~. 11~ x x
11~. 1~ . x x
~ ~ 1~, 1~, I~R) x x x x
T~
~ ~l~B, ~b13V-~B X X X X
~ ~11~111-S~S X ' X
~11~112-~ X X
~11&11~5 x X X X
W~ ~ X x x x
~ S~ ~~1~ (+24 ~ X X
~1~~ (-~ ~ X X
~1~1~ X X X X
~~ X X x x
~1~1~ X X X X
~1~ X X X x
~1~ x X X X '-
~I~ X X X X
~~ x X X X
~1~ x X- x X
~1~1~ X X X X
G~ x x x X
~Sl-~ x x i x x
I DP-TRANSMITTER ISHEET 1 Of i
iNO !BY iDATEI REVISION ISPEC: Z300
DIFFERENTIAL PRESSURE I I I I
FLOW TRANSMITTER I ! i I ICONTRACT:COPPELL
i ! i i IP.O. OPELI
TYPE: FLOW TRANSMITTER
PRIMARY ELEMENT: FLOW TUBE
ENCL: NEMA 4
ELEMENT TYPE: DIAPHRAM
MATERIAL:BODY': CARBON STL.
ELEMENT: 5i6 S.S.
RATING:OVERRANGE: 2000PSIG
BODY RATING:2OOOPSIG
PROCESS: WATER
PROCESS CONNECTION: 1/2"
DIFF. RANGE: O-25"N.C/O-120"W.C.
-
CALB. RANGE: O-IO0"W.C. (SEE NOTE) ..
OPTIONS: LOCAL INDICATOR: YES
INDICATOR SCALE: 0-20 MGD
MANIFOLD: DA SBZ-4$AF
TRANSITENT PROT.: NO
MOUNTING 8RKT.: 2" PIPE
OTHER: INTERGAL SQ. RT. EXTRACTOR
MFG: BRISTOL BABOCK '
MODEL: 2408-558-$22-111-2ii-0 WITH FOLLOWING
(1) FLOOR STAND OBRIEN FP40, (1) ENCL. OBRIEN
C217. (1) HEATER/STAT OBRIEN ESOBI
FLOW CALB.
FIT-4 0-20 MGD 0-100" STAT DISCH FLOW METER VAULT
NOTE: CALIBRATED DELTA PRESS. RANGE WILL BE PER ACTUAL CERTIFIED .
CALIBRATION SHEET PROVIDED BY PRIMARY SENSOR VENDER.
I.0 laY IDATEI REVISION ISPEC:
'm I CONTRACT:COPPELL
I I ! I IP.O. CO'PELI$ I
I i I I iBY MRB IAPPR I
DESCRIPTION
TYPE: E.S.T. LEVEL TRANSMITTER
CASE: MANF. STAND
MOUNTING: PIPE STAND
ENCL. CLASS: NEATHERPROOF
POWER SUPPLY: 24VDC EXTERNAL
OUTPUT SIGNAL: 4-20 MA
ELEMENT TYPE: DIAPHRAM
MATERIAL: BODY; CARBON STEEL
ELEMENT; ~16 SS
RATING: OVERRANGE: 2000 PSI
BODY RATING; 2000PSI
DIFF. RANGE: 0-25 TO 0-150 PSIG
CAL. RANGE: 4MA = 45.26PSIG (lO0 FT.). 20MA = 64.91PSI~ (~50
PROCESS: WATER
PROCESS CONN.:
OPTIONS:
LOCAL INDICATOR: YES
INDICATOR SCALE: 0-~00~
MANIFOLD: NO
TRANSITENT PROT: NO
OTHER:
MANUF: BRISTOL BABCOCK
MODEL: 2408-~0B-5~1-~1-£0
TAG Nq.,_ RANGE SERVICE ~OCATION
LIT-1 0-50 FI EST LEVEL EST
i
F
F'
RIC-NATI ,EE,~) BRII Ti3L
~ FLOW RATE)
nstruments/systems
· 0.2% Accuracy -
· Integral Square Root Extraction with Stable Zero i~P-'"'""~Ii~
· Inorganically Bonded Strain Gauge Sensing Element
· Wide Selection of Diaphragm and Process Flange Materials
· Optional integral meter for local indication ~
·Extemal Span and Zero Adjustments
· Adjustable Pulsation Damping '~
· Meets N.~.C.fi. Specifications MFI-OI-?$
· Factory Mutual and Canadian Standards Association Approval .~.~,..~..,.
INTRODUCTION
The Signature Flow Rate Transmitter brings unparalleled ex- ~s'--7
cellence to the measurement of flow when used in conjunc- ,' ·
lion with industry acceptable pdmary flow devices (i.e. odfice '.'f'j~- ~
cally bonded strain gauge element, highly accurate meuure- ~~,'~: = ' '
ments of differentials from 3' H20 to 900 PSI are obtain- ~,~ . ,
able. State-of-the-art CMOS technology permits conversion ~
~f the differential input signal to a square root output from 1% ,,~,,, _./ ,.
to 100% of input which provides 10 to 1 rangeability when .7~,~,,,,,_- ~.~.~
expressed in terms of flow. (See Figure 2 and accuracy .... ~,~ ~..-~~
merit of 6 to I turndown enhances transmitter versatility and ~,~,..~.
reduces required stock of spare units. Adjustable pulsation ..... ~,~ ~.~.....~..~.~ =.,,,, -
dampening is provided to suppress the effects of noisy pro- ,,=, ¥.._.~.:.:':.~.
cass conditions. Corrosive service requirements are easily
met by a broad selection of materials including: Tantalum
diaphragms and Kynar process flanges. 0.003" ~ick diaphra. Figure
gms increase corrosion life and provide structural integrity.
Compact desi and lightweight in addition to external zero .=, ~ ,.~, -.o., -.-=,, ~-,
and span adjustments, and conveniently located emectdcai '
terminals simplify installation and start-up of instrument '
loops. Integrally provided square root extraction and optional ;_
local analog meter reduce installation time and wiring cost. -~,.:
OPERATION -"'~ ·
The pressure sensing diaphragms are located in the process
housing, as shown in Figure 1. The differential pressure
across these diaphragms when hydraulically applied to the
inside and outside of a nesting capsular element creates a
force which causes it to move and deflect a strain beam. This
deflection causes a change in resistance in the two legs of .=., ~ , ~ ~. ~ ~ i.;~
the inorganically bonded semiconductor strain gage. The \
gages are electrically connected to the compensation board
temperature errors of the strain gage. The compensated sig- ,,.
nai is than amplified and converted to a two wire 4-20 mA
signal. '"
The base amplifier board and squ~re root function board ·
work as a team to amplify the compensated signal and con-
vert it to a two wire 4-20 mA signal ttmt is proportional to
.ow.
'
--Bri toi Babcock lnc,,