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298<br />

aprogram will make this approach less useful. Properly operating centrifugal<br />

pumps, the most common type used, can be verified by sound, in combination with<br />

observation of flow and pressure data, for pumps that are affected by air in the<br />

supply stream, or through failing seals, will cavitate, and perhaps cause substantial<br />

vibration in the attached piping. The appearance and sound of spray ricochet in a<br />

vessel being spray CIP’d will provide areliable though not definitive indication of<br />

proper supply pressure, and uniform delivery of CIP fluids.<br />

Historic Operating Trends<br />

Much of the CIP control software in current use provides for the acquisition and<br />

storage of operating data for the important variables including level, pressure, flow,<br />

supply and return temperatures, and conductivity or resistivity. Prior to beginning<br />

field troubleshooting of areported or confirmed operational problem, it can be very<br />

helpful to obtain ahistorical trend, if available, for the circuit or system involved.<br />

Trending data may be available for<br />

& CIP supply flow rate<br />

& CIP supply temperature<br />

& Steam supply temperature control valve position<br />

& Steam header pressure<br />

& CIP supply temperature<br />

& CIP return temperature<br />

& Chemical supply source tank level<br />

& Chemical feed header pressure (if applicable)<br />

& Circuit system fills volume set point (volume of solution in circuit)<br />

& CIP supply conductivity set point<br />

& Conductivity return resistivity set point<br />

& Water additions during the recirculated wash.<br />

Interpretation of Trending Data<br />

Some examples of operating problems that areview of trending data may be<br />

beneficial include<br />

Repeated water addition during acycle as the result of low level in aCIP recirculation<br />

tank (or air separation tank) will dilute the chemical solution and thus cause<br />

reduced conductivity.<br />

Water addition may be the result of CIP circuit hydraulic imbalance, as the result of a<br />

failing return pump (generally seal or suction side leak). AU-Bend transfer<br />

leak, an improperly tightened or positioned return hose or spool piece<br />

installation may cause either loss of solution, and hence level, or incorporation<br />

of air in the supply to pumps.<br />

Supply flow problems of alow or high flow nature and may be attributed to one of<br />

many issues. The alarm may be intermittent rather than continuous. The<br />

historical trend data can provide information as to when the intermittent<br />

alarm occurs, or at what point flow control has been lost.<br />

PROGRAM FAILS TO START<br />

Rush<br />

Most CIP programs are initiated by asequence of manual operations which include<br />

selection of ( i )the equipment to be cleaned, ( ii) the selection of the applicable CIP

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