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
• Zinc Phosphate corrosion protection
• Adjustable packing gland
• Meets NACE MR0175 (2000) & MR0103 (2012) with SS trim
• Compact
STANDARD MATERIAL LIST
PARTMATERIAL
Lever and gripSteel, zinc plated w/vinyl
1
Stem packingMPTFE
2
Stem bearingRPTFE
3
Ball
4
Seat (2)RPTFE
5
RetainerA108-C S
6
Gland nutA108-C S
7
StemA108-C S
8
Lever nut (Screw 1/4” to 1/2”)Steel, zinc plated
9
BodyA216-WCB
10
ASTM A108, Carbon Steel, Chrome Plated or
ASTM A276, Type 316 Stainless Steel
VAR I ATIONS AVAI L AB LE
• 92-140 Series (316 SS Ball & Stem)
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
-P -01 -BSPP (Parallel) Thread Connection1/4” to 2”
-T -01-BSPT (Tapered) Thread Connection1/4” to 2”
-02-Static 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”
-10-SS Lever & Nut1/4” 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”
-46-Latch Lock Lever - Lock in Closed Position Only1/2” to 2”
-47-SS Oval Latch-Lock Handle & Nut1/4” to 2”
-48-SS Oval Handle1/4” to 2”
-50-2-1/4” CS Locking Stem Extension3/4” to 2”
-58-Chain Lever - Horizontal1” to 2”
-60-Grounded Ball & Stem3/4” to 2”
-65-Multifill Seat s & Graphite Packing1/4” to 2”
-UA-AIS (American Iron & Steel) CompliantAll
Graphite Packing, PTFE Body Seal, RPTFE Bearing
(Fire Safe API 607, 6th Edition, ISO 10497:2010)
Pressure/Temperature Ratings -
Page M-14, Graph No. 14 (1/4” to 1”)
Page M-13, Graph No. 12 (1-1/4” to 2”)
1/4” to 2”
DIMENSIONS
PART NO.SIZEABCDEWT.
92-101-011/4 ”0.381.142.211.643.870.49
92-102-013/8”0.381.142.211.643.870.49
92-103-011/2”0.381.142.211.643.870.49
92-104-013/4”0.501.342.701.783.870.76
92-105- 011”0.631.513.032.004.781.21
92-106-011 -1/4”0.811.793.622.184.781.95
92-107-011-1/2”1.001.954.002.695.432.92
92-108-012”1.252.284.732.915.434.73
Customer Service (704) 841-6000industrial.apollovalves.comC-5
REV. 18JUL19
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.