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246<br />

CIP supply- 2"<br />

CIP return- 2"<br />

1,2,3,4<br />

2<br />

Pulse<br />

upper seat<br />

to leak<br />

port<br />

1,2,3,4<br />

TK1<br />

1<br />

Mixproof<br />

valve with<br />

seat lifter<br />

T<br />

CS<br />

CIP flush line<br />

Pulse<br />

lower seat<br />

to leak<br />

port<br />

CS CS<br />

4<br />

3<br />

3<br />

TK2<br />

FIGURE 9 Rising stem mixproof valves, applied three-per-vessel, provide automated control of all<br />

product and CIP fluids and isolation of all fluid streams. Aprocess requiring recycle to the source<br />

vessel would require afourth mixproof valve. The solid and dashed lines and numbered arrow heads<br />

define the CIP sub-circuits described in the narrative.<br />

CIP supply- 2"<br />

Bleed<br />

valve<br />

open<br />

CIP return- 2"<br />

T<br />

1,2,3,4<br />

Pulse<br />

bleed<br />

valve<br />

1,2,3,4<br />

2<br />

TK1<br />

T<br />

1<br />

3<br />

3<br />

CS<br />

Pulse<br />

bleed<br />

valve<br />

CIP flush line<br />

Bleed<br />

open<br />

valve<br />

4<br />

T<br />

TK2<br />

T<br />

4<br />

Seiberling<br />

FIGURE 10 Diaphragm valves in valve assemblies can be applied to isolate product and CIP fluids<br />

and provide the identical operating capability of Figure 1or9.The solid and dashed lines and<br />

numbered arrow heads define the CIP sub-circuits described in the narrative.<br />

T<br />

4

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