Female NPT Thread, 1/4”-3” 1000 CWP (psig), Cold Non-Shock. (See referenced P/T chart)
150 psig Saturated Steam.
Vacuum Service to 29 inches Hg.
MSS SP-110 Compliant.
Designed, cast, machined, assembled, and 100% factory tested in USA.
FEATU R ES
• Investment cast components
• Reinforced seats
• Blowout-proof stem design
• Adjustable packing gland
• Stainless steel lever and nut
7
8
2
5
6
1
11
10
• Fire safe to API 607 (requires -24 sux)
• Meets NACE MR0175 (2000) & MR0103 (2012)
• CSA CGA 3.16-M88 (Requires “GS” sux)
• NSF/ANSI/CAN 61 Section 8, Annex G (1/4” to 2”)
• NSF/ANSI 372 - Drinking Water System Components - Lead Content
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 Connection1/2” to 2”
-T -01-BSPT (Tapered) Thread Connection1/2” to 3”
-02-Stem Grounded1/2” to 3”
9
B
4
3
A
-04-2-1/4” Stem Extension (Carbon Steel, Zinc Plated)1/2” to 2”
-08-90º Reversed Stem1/2” to 2”
-11-Therma-Seal™ Insulating Tee Handle1/4” to 2”
-14-Side Vented Ball (Uni-Directional)3/8” to 3”
-24-
Graphite Packing, PTFE Body Seal,
RPTFE Bearing (API 607, 6th Edition, ISO 10497:2010)
1/2” to 3”
-27-SS Latch- Lock Lever & Nut3/8” to 3”
-30-Cam-Lock and Grounded1/2” to 2”
STANDARD MATERIAL LIST
PARTMATERIAL
Stem packingMPTFE
1
Stem bearingRPTFE
2
A276-3 16SS (1/4” to 2”, except 1-1/4”)
Ball
3
Seat (2)RPTFE (2 ” & smaller); RTFM (3”)
4
Retainer
5
GlandA276-3 16 Stainless Steel
6
StemA276-3 16 Stainless Steel
7
Lever nut304 Stainless Steel
8
Body SealRPTFE (1/2” to 3”)
9
BodyA351-CF8M
10
Lever and gripSS w/vinyl
11
A276-3 16SS or A351-CF8M stainless (1-1/4”)
A351-CF8M stainless (3 ”)
*LEAD FREE: The wetted surfaces of this product shall contain no more than 0.25% lead by weighted average. Complies with Federal Public Law 111-380. ANSI 3rd party approved and listed.
REV. 18JUL19
Customer Service (704) 841-6000industrial.apollovalves.comA-18
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.