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286<br />

3" Stub end<br />

w/150# flange<br />

2A<br />

1<br />

3<br />

Plan view<br />

2B<br />

FIGURE 5 Instrument holder connections.<br />

Solids Charge Nozzles/Chutes<br />

Solids charge nozzles and chutes can be achallenge to clean. By their nature they are<br />

always heavily soiled after use. They can, however,becleaned like vertical tanks by<br />

applying falling films of CIP solution, initiated from properly positioned bubbletype<br />

sprays.<br />

The use of asplit butterfly valve for contained solids transfers has become<br />

quite popular in bulk pharmaceutical processing. Vendors of these devices offer<br />

special adaptors fitted with spray devices that allow for CIP of their solids<br />

handling valves.<br />

REACTOR CLEANING CIRCUITS<br />

As previously stated, in the design of API CIP systems, it should be agoal of the<br />

designer to use as much of the process piping and equipment as possible to<br />

distribute the cleaning solution.<br />

& Thereisalong-standing “rule of thumb” that lines should be flushed at arate of<br />

5ft/sec. This rule of thumb was developed by early workers with CIP systems<br />

comprised primarily of glass pipe. Simple observations of flow in lines of 1 1 ⁄ 2 to<br />

3in. in diameter, inextensive circuits, indicated the need for a5ft/sec velocity<br />

to ensure that the flow is highly turbulent and will sweep air from long<br />

horizontal runs, that it will flood vertical runs in adownflow regime, and<br />

that it will sweep gas pockets out of vertical tees.<br />

Obtaining 5ft/sec is not always possible, but this is agood starting point for<br />

evaluating the system. The designer is usually confronted with the fact that the<br />

system uses Teflon-lined pipe of four different sizes, as shown in Table 3.<br />

In the design of reactor systems between 300 and 4000 gal, the most typical<br />

liquid transfer line is generally 2in. Consequently, there is an upper limit to how<br />

much liquid can be distributed at any one time because of the limitations of the<br />

piping components and the characteristics of the process transfer pump.<br />

8"I.d.<br />

Side view<br />

1<br />

3<br />

Tube spray<br />

2A 2B<br />

Temperature<br />

probe<br />

1-1/2" Stub end<br />

w/150# flange<br />

Two -3"stub ends<br />

w/150# flanges<br />

Cerulli<br />

Pressure<br />

instruments<br />

with seals

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