• 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 1-1/2”
-19-Lock Plate (Suggest using 92 Series)1/4” to 2”
-24-
-45-Less Lever & Nut1/4” to 2”
-60-Grounded Ball & Stem3/4” to 2”
Graphite Packing, PTFE Body Seal, RPTFE Bearing
(Fire Safe API 607, 6th Edition, ISO 10497:2010)
Pressure/Temperature Ratings -
Page M-14, Graph No. 13 (1/4” to 1”)
Page M-13, Graph No. 11 (1-1/4” to 2”)
1/4” to 2”
DIMENSIONS
PART NO.SIZEABCDEWT.
93-101-011/4 ”0.381.142.181.633.680.56
93-102-013/8”0.381.142.181.633.680.56
93-103-011/2”0.381.142.181.633.680.56
93-104-013/4”0.501.352.661.753.680.79
93-105-011”0.631.513.031.934.681.27
93-106-011 -1/4”0.811.793.622.094.682.26
93-107-011-1/2”1.001.964.002.715.503.57
93-108-012”1.252.084.712.928.005.94
STANDARD MATERIAL LIST
PARTMATERIAL
1Lever and gripSteel, zinc plated w/vinyl
2Stem packingMPTFE
3Stem bearingRPTFE
4Ball
5 Seat (2)RPTFE
6 RetainerA108-C S
7Gland nutA108-C S
8StemA108-CS zinc plated
9Lever nut (Screw 1/4” to 1/2”)Steel, zinc plated
10BodyA108-C S
ASTM A108, Carbon Steel, Chrome Plated or
ASTM A276, Type 316 Stainless Steel
Customer Service (704) 841-6000industrial.apollovalves.comC-6
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.