P. 1 

# OAR Box 1147 Prepped by Ollie Stewart



## Document

Number: 

# 174 ) IV-E-4

7 Docket Number: 

# A-87-1 1

Printed 4/22/20082:42:56

PM Sheet 174 of 242UNITE D STATE S ENVIRONMENTA L PROTECTIO N AGENC Y AN N ARBOR . MICHIGA N 4810 5

MA Yi OFFIC E O F AI R AN D FIADIATIO N



### MEMORANDU

M SUBJECT : Meeting o f SA E J28 5 Tas k Forc e o n Nozzl e Geometry Specification s FROM : Joh

n W . Mueller , Mechanica l Enginee r ji/yUi'//Ity'tyC^ Standard s Developmen t an d Suppor t Braryc

n ' / TO : :HRU : 

### Publi c Docke t A-87-1 1

Joh n F . Anderson , Senio r Projec t Manage r Standard s Developmen t an d Suppor t Branc h 

# P/UO n Apri l 14 , 198 8 I attende d th e firs t meeting o f the SA E J28 5 tas k forc e on nozzl e geometr yspecifications . Th e purpos e o f thi s tas k forc e i s t o revis e the SA E recommende d specification s for nozzl e geometr yi n ligh t o f EPA' s onboard refueling proposal . Th e meeting began wit ha discussio n o f th e objective s o f the tas k force . Afte r a length ydiscussio n o f nozzl e geometry issue s i t wa s decide d tha t th e group' s mai n objectiv e shoul d be t o defin e a mor e complet e se t o f recommende d spou t dimension s t o replac e the presen t SA E J28 5 specifications . Whil e othe r objective s wer e discussed , suc ha s defining specification s fo r automati c shutof f respons e tim e a i overpressur e shutoff , th e tas k forc e decide d ths t suchproject s ar e beyon d the scop e o f th e presen t effort s an d tha t onlythe nozzl e spou t shoul d be deal t wit ha t thi s ti*ne . Following th

e definitio n o f th e group' s objectives , Mik e Harriga n o f Ford hande d ou t som e informatio n (include d a s a n attachment ) on tes t o f nozzl e design on wor k For d ha s done concerning th e influenc e refuelin

g an d discusse d i t briefly . Rober tP. 3



### Thompso n o f Stan t then discusse d hi s handou t concerning fue l dispensing nozzl e evaluatio n (included a s an attachment) . Finally , John Aube r o f Borg-Warne r Automotiv e presente d a propose d nozzl e spou t configuratio n (included a s a n attachment) . Befor e th e meeting adjourne d i t wa s decide d tha t the nex t step wa s t o evaluat e the four spou t configuration s propose d thu s far an d t o arrive a t a singl e compromise d se t o f specification s fo r commen t an d evaluation . Attachment sP. 4 Oilmen' s Trvc h Tsa^kt

Inc . Smit h Meie rInc . Vtedw • fiool Ce . Wllco , inc . ®teri/regfgfer5 p AnMor' s inc . Do cPetroleu m System s Inc . EQulpmsnfSaiesCo.ln c GlasgowEquipmen t Service , Inc . Huiue i Ei-juipment Co . Oilmen' E Truc k

Tank s l/ic . 10 1 -M0tor*/raafstar $ 

## Ticke t Prlrtfirie'&teGd * Ace Tan k An d Equipmen t Co . Amtfiar'slnc , Browni e Tan KMtg . Co . Decfel^eyf " Splem s Inc . Ostarma n Weldin g £Tan k Serv.. Inc . Oove rCorp ; Rotar

yLit ; Emerso n Electric/Brook s Equipmen t Sale s Co . Inc . G fi G Oi l Equipmen t Broker s GlasgowEquipmen t Service . Inc . HC S Petroleu m Equip . Inc . Hollowa yWeldin g & Pipin g Co . Horne rEquipmen t Co . Uqui d Control s Corp . Parke rHannifi n Corp. / Ei s Div . scuii yEiecroni cSystem s Tripitod s Ine . ©esoHne--full-6©rv©/8el f -eerve/vopoi ' R<5>€©v
f y Ae e Tan k Ant fequipmen t Co . America' s $vc . Sta . Suppl ya Mg . APS - Pel^eu m Equipmen t M . Carde riit fysirl wInc . Callowinc . Concept Communication s Co . Davi s Safes Co. , Inc . Dawn Duin/ i 3plo» i lity . DecPeiwteu m Sjwm s Inc . Determa n Weldin g $, Taft k Serv. , Inc . DoverCofp.Opwdiv . B8Wgmerpri$e s Eastern Technologie s Ltd . fmc o Wheato n Inc . Equipmen t Sale s Co . Inc . Q & G o n Equipmen t BroKsr s GDNNortf e Gilbarco Inc . Glasgo wEquipmen t Service , Inc . Harc o Industries . Jnc, HC S Petroleu m Equip . Inc . Hollowa yWeldin g & Pipin g Co . Horne rEquipmen t Co . HuskyCorp . Aee IMA/ WEquipmen t C o •Allie d Piaatic a foe. ealc fan k Procuct * ft*'Ma* attribute * In e HubCt/Pcodslfic . KPlneustrt w Jjjnmaf cDivisio n Witc

o Corporal ! M cNe d Corp . National-Spence rin c Patte rHannifi n Cotpvpiewsoi v Charle s C.ParH , Co . Sunshin e Jr . Stores inc .

; Inc . Balcran k product s isaa y- Way Co. JulianAssociates . Inc . KP Industrie s McNei l Corp .

MurtfHWJ ? - NATIONA L PETROLEU M NEW S 

# mi Aintiiur' s free , DG $ Pot^eteuff l Syetem e ln§ . Easter n Technologie s Lld , • GlasgowEqylpmen tService , Inc . una i ruin s iroustfl u " H C 8 Petroleu m Equip . Ino . Hollowa yWeldin g & Pipin g Co . Home requipmen tCo . Neptun e Measuremen tc a Oilman' s Tfue k

Tank e Ine . Southwest Pun©

Co . H7SM®t©fi.Trek® t Ac s Tan k tad Equipmen

t Co . Amlhor'slnc . BeaudfiauEiectraflfCsjne . gcewnieTaAkMlg.Ce . De cPetroleu m System s Inc . Detarma n Weldin g & Tan k Serv. , Inc . Dresse rIndustrie s Inc . Cealei n TWiwtoyie a Ltd . Emar&o n Electric/Brooks Equipmen t Sale s Co . Inc . Glasgo wEquipmen t Servica , Inc . HC S Paliukiuii i Eijuij-) . Int . Hollowa yWgyin g ft Pipin g Co Home rEquipment Co . Uqui d Control s Corp . Nftotun e Measuremen t Co . Neptun e WocisgromOn t Co . Oilmen' s Truc k

Tank s Inc . Smit h Mete rInc . lokhetmUorp . Vcodo rneolC* . 

### 16 2 Mirrors , Windehleld/sid s Amthor'f i Ine. Genera l Electri cPlastics Genera l Electri cPlastics Geiieut l 3-Jentllii ; Safel yEquip . Cu . K-DUmpCo . Farte rHannifi n Corp. /

Si s Div . 18 3 Monitors . 

## Oxyg©n/co2/-*9tc . Arg o Instruments Inc . Capita l Control s Co . Inc . EiuujWIigdluiilii u Emhar t Industrie s Inc . Lyn n Products Co . Inc . MS A Nationa l Draege rInc . noseflwun t Analytica l Sansidynf l Inc . 18 4 Mufflsrs/failoip& s Amthor' s Inc . i vi n (..na.. . i ,,t.-o,„ . h:, , iRPCOlrtq . L H . Lyn n Industrie s Inc . M eNeilCorp . Mornso n Bros . Ue . Oilmen' s Truck

Tank a Ine . Private Rranr

t Sflrviro e In r" * Radfqr d Equipment Compan y Richard s Industries Inc . Richard s Industries O

fUtah , Inc . Willia m ftisHnlph ACr

t in r Seyiert h Mfg. , Inc . Sunsto M Jr . Stores Inc . Tim s OaringfiilaInc. Tripilrtftfi RIn n Vltan a Corp . CfWi H Inc . Wei l Sarvfce Products Corp . 

## FUfflJiui , 

## 6/-d4uipnlerl ! Allen-Morrison , Inc . DurToughs Corp . CPTCorp . Owre e Da

vSlstems . Inc . EricayMfg.Co . Pilot Corp . 0\

America . Mktg . Oiv . Shur o Mfg . Corp . Standar d fiefHoefaticn Co. , Inc . Westinghous e Electri cCo . 

## 16SOiiBurnd fNd22ids ^' Altai'Muufeu < Berks' ? Sve . CONCEP TCO i DCIMatatin c I.T.W . fuiiBo r Mode m Malal F ShuraMlg.Con * SouiWan d Disi r ValvelinoffllC e Warre n Stea l $ t Wai l Servic

a P n 193Qi!°I F 

## iquipme i Amenta' s 3vw. » Chsmica l Centr

e Dove rCofp . Op E 8 WEntsiprl s trniwdiflcopor, ' Enquip . Inc . Enyiranetic

a !n. c G&dCorp . ittMrtlSosntit . GSosgo wE^i'tpp. 6rou<3wate rTec i Hollowa yWeWir . HVfi S PfOfiUflS . iTH E INFLUENC E O F DISPENSE R NOZZL E DESIG NONREFUELIN

G 

## 1 J +- 4/>F-*>Z&5~ ~M. *"/f/» y M . J . HARRIGA

N- (W+eJ

«T~ Wto - > -*> * ^ ' ' D . L . CRAGG S FOR D MOTOR COMPAN

Y

1 - biDESIGNE D EXPERIMEN T T O DETERMINE WHAT PARAMETER S CONTRO L QUALIT Y O F REFUELIN G FIRS T STEP : BROA D SCREENIN

G EXPERIMEN

T BLOCKE D PARTIA

L FACTORIA

L DESIG N 1 3 PARAMETER S IN3 2 RUN S INCLUDE S TH E EFFEC T O F NOZZLE S A S A NENVIRONMENTA

L FACTOR

• OP W II AUNLEADE D
• EMCO-WHEATO

NA-400 0 STAGE I I VAPO R RECOVERY
• EMCO-WHEATO

NA-200 0 UNLEADE D
• EMCO-WHEATO

NA-200 0 WIT H IMPROVE D SPOUT
• HUSKY I + X UNLEADE D

b >FUEL FILLE RPIP E DIMENSIONS FO REXPERIMENTA

L DESIG N SYMBO L DESCRIPTIO N FILLE RPIP E DESIG N NUMBE R t 1 2 3 4 5 6 7 8 9 1 0 1 1 1 2 1 3 1 4 1 5 1 6 1 7 1 8 1 9 2 0 2 1 2 2 2 3 2 4 2 5 2 6 2 7 2 8 2 9 3 0 3 1 3 2 B Restricto r opening offse t C Distanc e t o firs t bend a Pip e inle t angl e D 2 Mid-pip e diamete r F Lengt ho f ru

n D 3 Pip e outle t diamete r E 2 Tota l drop heigh t 7 Inclin e o f lon g run < 5 Inclin e o f majo r drop ADept ht o restricto r V Ven t diamete r 0 Fille r opening dept h belo wfue l a t shutof f Nozzl e designs : OPW Emco-Wheato n Unleade d Emco-Wheato n Stag e I I Emco-Wheato n Improve d Husk yUnleade d -

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o X o o o X o o o X o o o X o o o X o o o X o o o X o o o X o o X X o o 0

X 0 0 0 X 0 X 0 0 0 X 0 X 0 0 X 0 0 X 0 0 0 X 0 0 0 X 0 X 0 0 0 0 0 X 0 0 X 0 0 X 0 0 0 X Specifie d o r Derive d Dimension s D\ Inle t diamete r Restricto r opening diamete r E\ Heigh t o f firs t drop fiInclude d angl e a t firs t bend R Ben

d radi i (t o centerline ) Tape r angl e a t transition s t o smalle r diameter s 50. 0 m m 21. 0 m m A s Derive d A s Derive d 10 0 m m 30 °

- 3EXPERIMENTAL CONDITION S •FLO W RAT E CONTROLLE D AT PUM P - •FUE L VOLATILITY •FUEL , TAN

K AN D PIP E TEMPERATUR E •FILLE R PIP E AN

D TAN K ATTITUD E - •FUE L SUPPLY 1 TO 2 0 GALLON S PE R MINUT E +/ " 1/ 8 GPM ) 13+/"- 5 ps i RVP ROOM TEMPERATUR E - 73. 8 +/-1.3°¥ FIXTURE D T O +/-.5DEGRE E O F IN-CA R POSITIO

N DIRECTL Y FRO

M 5 5 GALLO

NDRUM S / -f '^ * 

# &.<L 7

- 4 - T l 0 0EXPERIMENTA L TECHNIQU

E

• INSER TNOZZL

ET O TH EFULLES TEXTEN

TPOSSIBL EAN

D LATCHE

D O NTH EPIP EOPENING
• ALIGNNOZZL

EPERPENDICULART O TH EGROUN

D I NTH

EPIP EOPENING
• OPERAT

ENOZZL

EWIT H TH ETRIGGERLATCHE

D A TTH EHIGHES TFLO

WRAT ESETTIN G
• CONTRO

LFLO WRAT EA TTH EPUM P
• MAK ESHUTOF

FMEASUREMENT

S BASE D O NAUTOMATI

C NOZZL

ESHUTOF

F
• MAK EAL LFIL LQUALITY AN D SHUTOF

FMEASUREMENT

S WIT H HAND S OFFTH

ENOZZLES

- 5 - T l C OCRITERI A FO RMEASUREMENT S

• FILL : HIGHES T FLO W RAT E DURIN

G STEAD Y STAT E FIL L WHER E N O FUE L LEAVE S TH E PIP E

• SHUTOFF : HIGHES T FLO W RAT E A T AUTOMATI C NOZZL E SHUTOF F WHER E N O FUE L LEAVE S TH E PIP E NOTE : Fil l an

d shutof f ar e treate d a s two totall ydifferen t phenomenon . Thu s i t i s possibl e t o hav e a maximu m acceptabl e shutof f a t a highe r flowrat e than i s acceptabl e fo r stead ystat e filling .

6 -EFFEC T O F NOZZL E DESIG NONFIL L RAT E j (1 6 Pipes ) | FIL L | SHUTOF F OP W x | 13.0 6 | 10.1 4 | s

4.6 9 4.3 2 EMC O UNLEADE D

x | s 10.7 8 | 5.1 0 6.5 5 | 4.4 6 EMC O IMPROVE D x | s 10.9 7 7.9 5 4.5 8

3.2 1 HUSKY |

x | s j 10.6 6 | 2.0 5 | 6.7 2 | 4.0 1 | | ( 8 Pipes ) | FIL L | SHUTOF F
j (2 4 pipes ) | FIL L | SHUTOF F OP W x | 11.0 6 | 7.5 0 |
OPW x | 12.7 2 | 9.4 1 | s

3.8 6 3.3 6

s 4.4 5 4.5 6 Emc o Stag e I I |

x | s j 9.8 7 | 2.2 5 | 5.6 9 | 4.0 8 |
Emc o Improve d | x | s j 10.4 0 | | 7.7 9 | 4.0 4 |P.1 2 

# Stant

Fue l Dispensing Nozzl e Evaluatio n 1 4 Marc h198 8

Fiel d Surveyo f Servic e Statio n Nozzle s 1 Fue l Dispensing Nozzl e Survey2 Appendi x A3 Appendi x B 9 Appendi x C 1 0P.1 3 

# Stant FIELD SURVE Y O F SERVIC E STATIO NNOZZLE S Nozzl e Shut-of f Signal , Vacuum : X=7.1 8 kP a C T =0.95 8 kP a (Ful l fil l rate ) Nozzl e Diameter : X=0.18 4 in . O " =0.00 5 in . (SA E Recommendation : 13/1 6 in . (0.912 5 t o 0.840) )

Vacuu mSigna l Nozzl e Diamete r Servic e Statio n (kPa ) (in^ J Amoc o " 871 3 0.81 6 U T 5 1 J n fil'' 

### OP W 9. 0 0.813 n

### oit r °' 815 

### 0.81 2 7. 5 0.812 n u 

### ' 0 i 

### 0.81 2 °' 818 

### 0.81 3 0.81 3 0.81 4 °* 813 

### 0.81 5 °* 813 

### 0.81 5 °' 813 

### 0.81 0 0,833 

### 0.81 2 °* 828 

### 0.83 2 °' 825 

### 0.81 0 °' 815 

### 0.80 8 °* 813 

### 0.81 2 °' 814 

### 0.81 2 0.81 5 0,813 

### 0.81 0 0.81 0 0.81 2 °' 810 

### 0.82 0 °' 811 

### 0.81 6 0



### - 812 

### ^ 8 

### -0.81 5 °- 817 

### 0- 8 

### -0.81 5 °- 812 

### 0.81 3 Note : Eac hpressur e represent s thre e trial s fo r a nozzle . I t shoul d be note d ther e wa s littl e measurabl e variatio n betwee n trial s fo r eac hnozzle . Shel l (1 ) OPW , Husk

y Bonde d OPW Unite d OPW , Hus Shel l (2 ) Husk y Mobi l Viking »k

y

Clar k Emc o Wheato n Shel l (3 ) OP W Maratho n Emco,Hu s Checke r OP W k

y 6. 5

7. 0 5.2 5 7. 5 7. 5 8. 0 7. 0 7. 0 6. 5 6. 0 7. 5 9. 0 8. 0 5.7 5 6. 5 6.2 5 7. 5 7. 0 7. 5P.1 4 Pg . I 

# SlCKH t4/12/8 8

Liqui d , FlowRat e gal/min . 3 5 8 1 0 1 3 1 5 1 8 Liqui d , FlowRat e gal/min . 3 5 8 1 0 1 3 1 5 1 8 Fue l

Nozzl e Emc o W 4. 7 4. 4 6. 1 6. 5 7. 6 8. 9 9. 5 Nozzl e Emc o W 2. 8 2. 8 3. 6 4. 0 3. 6 3. 8 3. 9 D 1

1 Lspensin

g Noz z Nozzl e Shut Ai r Nozzl e 2 OPW 1 4. 9 7. 0 7. 0 8. 4 7. 3 7. 2 8. 2 FlowInt o Nozzl e 2 OP W 1 4. 0 4. 6 5. 9 6, 5 5. 0 5. 1 4. 8 l e 

## of f Survey Vacuum , Nozzl e OP W 2 5. 2 6. 7 7. 2 8. 0 9. 0 9. 1 9. 5 *<,ty p

### kPa 2 

### 3

Sensing Por t Nozzl e OP W 2 3. 8 5. 2 5. 6 5. 6 6. 9 6. 0 6. 5 3 

# , u Nozzl e

OP W 3 6. 0 6. 4 7. 7 9. 2 8. 4 9. 6 8. 7 min . Nozzl e OP W 3 3. 6 4. 0 4. 5 5. 5 5. 5 5. 5 4. 5 4

4

-



### Liqui d Dispensed : M S 495 7 Carburato r Calibratio n Fluid ; Se e Appenxi x B 2 The averag e o f 1 0 trial s fo r eachnozzl e a t eac hflowrat e i s listed ; Se e Appendi x A .

# Stan t

Appendi x A Nozzl e Evaluatio n
Emc o Wheato n OPW OP W OPW Tes t Fixtur e A l A 2 A 3 A 4 A S P.1 5



## "T rg. JP.1 6 

# Stan t 4/12/8 8 Ps . 4

A l Nozzle : # 

### 1 Emc o Wheato n FlowRat e gal/mi n 3 5 8 1 0 1 3 1 5 1 8 FlowRat e gal/min . 3 5 8 1 0 1 3 1 5 1 8 1

5. 0 5. 0 5. 0 6. 5 8. 0 10 . 19 . Tria l 2. 8 2. 8 3. 6 4. 0 3. 6 5. 8 3. 9 2 4. 0 5. 0 6. 0 6. 5 8. 0 9. 0 9. 0


# n V

a 3 4. 5 4. 5 6. 0 6. 5 7. 5 9. 0 9. 5 A cuu m 4 4. 5 4. 5 6. 0 6. 5 7. 5 8. 0 9. 5 i r F l A t Nozzl e Shut-off , Tria l # 5 6 7 5. 0 4. 0 6. 0 6. 5 7. 5 8. 5 9. 5 5. 0 4. 0 6. 0 6. 5 7. 5 8. 5 9. 5
owTo Sensing L/mi n 4. 0

4. 0 6. 5 7. 0 7. 5 9. 0 10 . Por t kP a 8 5. 0 4. 5 6. 5 6. 5 8. 0 8. 0 10 . 9 5. 0 4. 5 7. 0 6. 0 7. 5 8. 0 9. 0 1 0 5. 0 4. 5 6. 0 6. 5 7. 0 8. 0 9. 0 X 4. 7 4. 4 6. 1 6. 5 7. 6 8. 9 9. 5 

# cr 0. 4 0. 3 0. 5 0. 2 0. 3 0. 5 0. 4

Nozzl e Diameter : 0.810j. n 

### .

# Stan t 4/12/8 8 Pg . 5
A2 Nozzle : # 1 OP

W Flo wRat e gal/mi n 

### 3 5 8 1 0 1 3 1 5 1 8 Flo wRat e gal/min . 3 

### 5 8 1 0 1 3 1 5 1 8 

### 1

5 . Q 

### 7. 0 7. 0 9. 0 7. 0 7. 0 77 0
Tri a 4. 0 

### 4. 6 5. 9 6. 5 5. 0 5. 1 4. 8 

### 2 5. 0 7. 0 7. 0 9. 0 7. 0 7. 0 7. 0 

## i 

## n Vacuu m

3 4 5. 0 4. 0 7. 0 7. 0 7. 0 7. 0 9. 0 9. 0 7. 0 7. 0 7. 5 7. 5 7. 5 8. 0 A t Noz z

Tria l 5 

### 5. 0 7. 0 7. 0 8. 0 7. 0 7. 5 8. 0 Ai r Flo wT o S

L/mi n l e Shut-off , # 

### 6 7 

### 5. 0 7. 0 7. 0 8. 0 7. 0 7. 0 8. 0 ensin g 

### 5. 0 7. 0 7. 0 8. 0 7. 0 7. 0 9. 0 Por t 

## kP a 

## 8 5. 0 7. 0 7. 0 8. 0 8. 0 7. 5 9. 0 

### 9 5. 0 7. 0 7. 0 8. 0 8. 0 7. 0 9. 0 1 0 

### 5. 0 7. 0 7. 0 8. 0 8. 0 7. 5 9. 0

- 

### X 4. 9 7. 0 7. 0 8. 4 7. 3 7. 2 8. 2 

# cr 0. 3 

### 0 0 0. 5 0. 4 0. 2 0. 8

Nozzl e Diameter : 0.81 4 in .

# Stan t 4/12/8 8 Pg . o
A 3 Nozzle : # 2 OP

W 

### FlowRat e gal/mi n 3 5 8 1 0 1 3 1 5 1 8 FlowRat e gal/mi n 3 5 8 1 0 1 3 1 5 1 8 1

4. 0 5. 0 7. 5 8. 0 9. 5 10 . 9? 0
Tri a 3. 8 5. 2 5. 6 5. 6 6. 9 6. 0 6. 5 2 4. 0 6. 0 7. 0 8. 0 9. 0 9. 0 10 .
1 # 1 5 , 7 . 7 , 8 , 9 , 9 , 9 . 3

. 0

. 0

. 0

. 0

. 0

. 0

. 5 Vacuu m 4 6. 0 7. 0 7. 0 8. 0 9. 0 9. 0 10 . Ai r Fl A t Nozzl e Shut-off ,

Tria l # 5 6 7 5. 0 6. 5 7. 0 8. 0 9. 0 9. 0 9. 0 5. 0 7. 0 7. 0 8. 0 9. 0 9. 0 9. 0
.o wTo Sensing L/mi n 5. 5

7. 0 8. 0 8. 0 9. 0 9. 0 9. 5 Por t kP a 8 6. 0 7. 0 

# •. o 8. 0 9. 0 9. 0 9. 5 9 5. 5 7. 5 7. 0 8. 0 9. 0 9. 0 10 . 1 0 6. 0 7. 0 7. 0 8. 0 9. 0 9. 0 9. 5

m 

### X 5. 2 6. 7 7. 2 8. 0 9. 0 9. 1 9. 3 

# c r 0.' . 

# o. : o. : o . 0. . 0. . 0. -

Nozzl e Diameter : 0.81 4 in .P.1 9 

# Stan t 4/12/8 8 Pg . 7
A 4 Nozzle : # 3 OP

W Flo wRat e gal/mi n 

### 3 5 8 1 0 1 3 1 5 1 8 Flo wRat e gal/min . 3 

### 5 8 1 0 1 3 1 5 1 8 

### 1

6. 0 6. 0 6. 0 9. 0 9. 0 9. 0 8.* 0
Tria l 5. 6 

### 4. 0 4. 5 5. 5 5. 5 5. 5 4. 5 

### 2 6. 0 6. 0 7. 0 9. 0 9. 0 9. 0 8. 0
# 1 

### 3 6. 0 6. 5 7. 5 9. 0 9. 0 9. 5 8. 5 Vacuu m

4 

### 6. 0 6. 0 7. 5 9. 0 9, 0 10 . 8. 5 Ai r F ] A t Nozzl e Shut-off , Tria l # 5 6 7 

### 6. 5 6. 5 8. 0 9. 5 9. 0 9. 5 9. 0 6. 0 6. 0 8. 0 9. 0 9. 0 9. 5 9. 0

.owT o Sens i L/mi n 

### 6. 0

6. 0 8. 0 9. 0 10 . 9. 5 9. 0

n g Por t kP a

8 

### 6. 0 7. 0 8. 0 9. 0 10 . 10 . 9. 0 

### 9 6. 0 7. 0 8, 0 10 . 10 . 10 . 9. 0 1 0 

### 6. 0 7. 0 9. 0 10 . 10 . 10 . 9. 0

- 

### X 6. 0 6. 4 7. 7 9. 2 9. 4 9. 6 8. 7 

# cr 0. 1 0. 4 0. 7 0. 4 0. 5 0. 3 0. 4

Nozzl e Diameter : 0.81 4 in ,P.2 0 

# c

z z z I/ Ia/t « n O O O •n o o
—e i a* a~\ 9 « «•> * 

# c Pg . 8



### Fue l Dispensing Nozzl e

Sea l 

# " 2 Sensing Por t



# L Vapou r Tub e

Tes t Procedure : Nozzl e Shut-of f Vacuum : 

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