Female NPT Thread, 1/4” to 1” 2000 CWP (psig), 1-1/4” to 2” 1500 CWP (psig), Cold Non-Shock.
150 psig Saturated Steam.
Vacuum Service to 29 inches Hg.
MSS SP-110 Compliant.
FEATU R ES
• Fire safe to API 607 (requires -24 sux)
• Investment cast body
• Reinforced seats and seals
• Blowout-proof stem design
• Adjustable packing gland
• Meets NACE MR0175 (2000) & MR0103 (2012)
• Compact
• AAR Approval No. E989054
OPTIONS AVAILABLE
(MORE INFORMATION IN SECTION J)
• Minimum quantities apply
• To specify an option, replace the “0 1” sta ndard sux with th e sux of the option.
• To specify multiple options, replace the “ 01” sux with the d esire d suxes i n the
numer ical order shown below. NOT E: Not all suxes c an be combined to gether.
(SUFFIX)OPTIONSIZES
-01Standard ConfigurationAll
-02-Stem Grounded1/4” to 2”
-04-2-1/4” Stem Extension (Carbon Steel, Zinc Plated)1/4” to 2”
-07-Steel Tee Handle1/4” to 2”
-08-90º Reversed Stem3/4” to 2”
-14-Side Vented Ball (Uni-Directional)1/4” to 2”
-15-Wheel Handle, Steel1/4” to 2”
-16-Chain Lever - Vertical1” to 2”
-24-
-27-SS Latch- Lock Lever & Nut1/4” to 2”
-30-Cam-Lock Handle & Grounded1/4” to 2”
-32-SS Tee Handle & Nut1/4” to 2”
-39-SS Hi-Rise, Locking Wheel Handle, SS Nut1/2” to 1-1/2”
-40-Cyl-Loc & Grounded3/4” to 2”
-45-Less Lever & Nut1/4” to 2”
-47-SS Oval Latch-Lock Handle & Nut1/4” to 2”
-49-No Lubrication. Assembled Dry.1/4” to 2”
-57-Oxygen Cleaned1/4” to 2”
-58-Chain Lever - Horizontal1” to 2”
-60-Grounded Ball & Stem3/4” to 2”
-UA-AIS (American Iron & Steel) CompliantAll
Graphite Packing, PTFE Body Seal, RPTFE Bearing
(Fire Safe API 607, 6th Edition, ISO 10497:2010)
1/4” to 2”
RETAINER PINNED
1/4” & 3/8” ONLY
DIMENSIONS
PART NO.SIZEABCDEWT.
96-101-011/4 ”0.381.142.211.643.870.49
96-102-013/8”0.381.142.211.643.870.49
96-103-011/2”0.381 .142.211.643.870.49
96-104-013/4”0.501.332.701.783.870.76
96-105-011”0.631.513.032.004.781.21
96-106-011-1 /4”0.811.793.622.184.781.95
96-107-011-1/2”1.001.954.002.665.432.92
96-108-012”1.252.284.732.875.434.73
Customer Service (704) 841-6000industrial.apollovalves.comC-7
Pressure/Temperature Ratings -
Page M-14, Graph No. 14 (1/4” to 1”)
Page M-13, Graph No. 12 (1-1/4” to 2”)
STANDARD MATERIAL LIST
PARTMATERIAL
1Lever and grip304 SS w/vinyl
2Stem packingMPTFE
3Stem bearingRPTFE
4 BallA276-316
5 Seat (2)RPTFE
6 RetainerA276-316
7Gland nutA276-316
8StemA276-316
9Lever nut (Screw 1/4” to 1/2”)18-8 SS
10BodyA351-CF8M
REV. 18JUL18
FLOW DATA
FLOW DATA
The listed Cv “factors” are derived from actual flow testing, at Apollo’s Pageland, South Carolina factory. These tests were completed using standard
“o the shelf” valves with no special preparation and utilizing standard schedule 40 pipe. It should be understood that these factors are for the valve
only and also include the connection configuration. The flow testing is done utilizing water as a fluid media and is a direct statement of the gallons of
water flowed per minute with a 1 psig pressure dierential across the valve/connection unit. Line pressure is not a factor. Because the C
formula can be used to estimate flow of most media for valve sizing.
is a factor, the
v
FLOW OF LIQUID
Q = C
or ∆P =
V
(Q)2 (SpGr)
WHERE:
• Q = Flow in US gpm
• ∆P = Pressure drop (psig)
• SpGr = Specific gravity at flowing temperature
= Valve constant
• C
v
√
(C
∆P
SpGr
2
)
v
FLOW OF GAS
Q = 1360 C
or ∆P =
V
5.4 x 10
(∆P) (P
(SpGr) (T)
√
-7
(SpGr) (T) (Q)
2)
(Cv)2 (P2)
WHERE:
• Q = Flow in SCFH
• ∆P = Pressure drop (psig)
• SpGr = Specific gravity (based on air = 1.0)
• P2 = Outlet pressure–psia (psig + 14.7)
• T = (temp. °F + 460)
= Valve constant
• C
v
CAUTION: The gas equation shown, is valid at very low pressure drop ratios.
The gas equation is NOT valid when the ratio of pressure drop (∆P) to inlet
NOTE: Only use the gas equation shown if (P1-P2)/P1 is less than 0.02.