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Commissioning and Qualification 343<br />

1. Think about what you expect to see before testing. If you do not see what you<br />

expect, investigate and understand why.<br />

2. Do not tweak, changes should be based on engineering principles. As described<br />

in point 1, you must understand what is happening and the root cause of any<br />

problem before implementing achange or modification.<br />

3. Test your data for consistency.<br />

4. Avoid using software to correct hardware mistakes.<br />

Investigate and Understand Why<br />

The first example below of something gone wrong actually violates the first two<br />

principles above. But the root cause (for the far reaching effects it had) was the<br />

violation of the first principle.<br />

Some background information on the CIP system for Project Bisnecessary<br />

first. The CIP tank and process vessel both have 0.2 m mhydrophobic vent filters.<br />

The process vessel vent is closed during most of the CIP to protect the filter from<br />

moisture (and plugging). The prerinse and final rinse are performed once through<br />

with water from the CIP tank (fed from a58 Cwater supply). The post-rinse is once<br />

through and fed using a 65 8 C water supply. The supply-water feed rate was<br />

increased during the upgrade of the system between Project Aand B. An air<br />

blow of the supply piping, acircuit drain, and arinse of the CIP supply tank follow<br />

alkaline and acid washes. The supply pump has avariable speed drive, but speed is<br />

fixed for agiven circuit. Flow control isvia acontrol valve. Aflow-deviation alarm<br />

of 5% will shut down the CIP (after atime delay). The supply-pump dischargepressure<br />

transmitter is used to detect an empty CIP tank and shutdown the CIP<br />

(after atime delay).<br />

Proper pump speeds were determined for each circuit during circuit flushing<br />

(as described previously). The engineer performed functional testing by running<br />

the circuit automatically.The engineer noticed that with the previously determined<br />

pump speeds, flow rates were higher than anticipated and flow-deviation failures<br />

occurred. At that point he should have investigated why the predetermined pump<br />

speeds were not working as expected. Instead he lowered the pump speeds and<br />

was able to finish all functional testing successfully for most of the circuits before<br />

leaving the project.<br />

Just as OQ was about to start, low-flow-deviation failures started to occur in<br />

circuits cleaned by one of the two CIP skids. Trends of previous (apparently<br />

successful) CIP runs were reviewed. The pump discharge pressure showed<br />

dramatic pressure swings corresponding to CIP tank level changes. This indicated<br />

that the CIP tank vent filter was likely plugged. Current failed runs did not exhibit<br />

this trend. Inspection of the CIP tank manway revealed that it was not bolted down.<br />

This was allowing the tank to vent via the manway.<br />

Further investigation revealed that the CIP tank vent was too small (and in a<br />

bad location) and that when 658 Cwater was added to the tank (via spray balls),<br />

flashing occurred and the vent filter was plugged with wet steam. The CIP tank was<br />

being pressurized when it was filled adding pressure to the CIP supply pump<br />

suction. Aredesign of the CIP vent line corrected the venting problem. Pump<br />

speeds were returned to the values determined during the manual flushing.<br />

However, other issues began to occur.

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