Page 245 - Root Cause Failure Analysis
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Seals and Packing    233

                     tion. The following recommendations for  seal startup apply to  most  types of  seal
                     installations and will improve their life if followed:
                             Caution the electrician not to run the equipment dry while checking motor
                             rotation. A slight turnover will not hurt the seal, but operating at full speed
                             for several minutes under dry conditions will destroy or severely damage
                             the rubbing faces.
                             The stuffing box  always should be  vented before startup, especially with
                             centrifugal pumps. Even if the pump has a flooded suction, it is still possible
                             that air may be trapped in the top of the stuffing box after the pump’s initial
                             liquid purge.
                             Where cooling or  bypass  recirculation taps  are  incorporated in  the  seal
                             gland, piping must be connected to or from these taps before startup. These
                             specific environmental-control features must be used to protect the organic
                             materials in the seal and to ensure proper performance.
                             Cooling lines should be left open at all times. This is especially true when
                             hot product passes through off-line standby equipment, commonly done so
                             that additional product volume or equipment change can be achieved easily.
                             often by simply pushing a button.
                             At the end of each day when hot operational equipment is shut down, it is
                             best to leave the  cooling water on long enough for the seal area to cool
                             below the temperature limits of the organic materials in the seal.
                             Before startup, face-lubricated seals must be connected from the source of
                             lubrication to the tap openings in the seal gland. For double seals, it is nec-
                             essary  for the  lubrication feed  lines to be  connected to the  proper ports
                             before  startup for  both  circulatory and  dead-end  systems. This  is  very
                             important because all types of double seals depend on the controlled pres-
                             sure and flow of the sealing fluid to function properly. Even before the shaft
                             is  rotated, the  sealing  liquid pressure  must  exceed the  product pressure
                             opposing the seal. Be sure a vapor trap does not prevent the lubricant from
                             promptly reaching the seal face.
                             Thorough warm-up procedures include a check of all steam piping arrange-
                             ments to be sure that all are connected and functioning. Products that solid-
                             ify when cool must be fully melted before startup. It is advisable to leave all
                             heat sources on  while the system is shut down to ensure that the product
                             remains in  the  liquid state. This facilitates quick startups and equipment
                             switchovers that may be required during a production cycle.
                             Thorough chilling  procedures  are  necessary  for  some  applications; for
                             example,  applications  involving  liquefied  petroleum  gas  (LPG).  LPG
                             always must be kept in a liquid state in the seal area, and startup usually is
                             the most critical time. Even during operation, the recirculation line piped to
                             the  stuffing box might need to be run through a cooler to overcome fric-
                             tional heat generated at the seal faces. LEG requires a stuffing-box pressure
                             greater than the vapor pressure of the product at pumping temperature. A 25
                             to 50 psi differential is generally desired.
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