Product Handbook 2026 - Volume 2

Pipeline ancillaries Ball valves

10

Pressure/temperature limits

Pressure psi g

0

145

290

435

580

725

356 302 212 122 32 -4

-20 0 50 100 150 180

* Steam Service: For steam applications cavity filler is not recommended.

Steam saturation curve *

0

10

20

30

40

50

Pressure bar g

The product must not be used in this region.

A - B Virgin PTFE TFM 1600

For valves with clamp connections, the maximum operating conditions could be limited by the type of clamp selected. For further information, consult Spirax Sarco.

Body design conditions

49.6 bar

720 psi

PMA Maximum allowable pressure

50 bar g @ 109 °C 725 psi g @ 228 °F

TMA Maximum allowable temperature

180 °C @ 0 bar g

356 °F @ 0 psi g

Minimum allowable temperature

-20 °C

-4 °F

PMO Maximum operating pressure for saturated steam service *

7 bar g

102 psi

TMO Maximum operating temperature

180 °C @ 0 bar g

356 °F @ 0 psi g

Minimum operating temperature

-20 °C

-4 °F

D PMX Maximum differential pressure is limited to the PMO Designed for a maximum cold hydraulic test pressure of

75 bar g

1088 psi g

7.3.119

Technical data Leakage test procedure to ISO 5208 (Rate A)/EN 12266-1 (Rate A)

Materials comply with: - FDA CFR title 21 paragraph 177, section 1550. - USP23 Class VI

Stem seal and seat

Flow characteristic

Modified linear

10.3 106

Port

True port design

Torque value Size

Kv values Size

2½"

3"

4"

2½"

3"

4"

N m

110

130

145

Kv

680

860

1950

The torque figures shown are for a valve at maximum operating pressure that is operated frequently. Valves that are subject to long static periods, may require greater break-out torque.

For conversion: Cv (UK) = Kv x 0.963 Cv (US) = Kv x 1.156

TI-P182-06 CMGT Issue 8

Page 2 of 6

M80i ISO Stainless Steel Ball Valve for Sanitary Applications

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