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Fail Position Of Control Valves
Started by sudheer, May 23 2010 10:35 PM
1 reply to this topic
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#1
Posted 23 May 2010 - 10:35 PM
Greetings
Fail positions of stripping steam control valves in various columns in our refinery were compared. It was observed that except in vacuum columns, all other stripping steam control valves are fail close. The stripping steam control valves of crude columns, side strippers, vacuum flashers (visbreakers), fractionators (Visbreakers) were fail close. Request forum members to give their views on why vacuum column stripping steam control valves are fail open.
thanks
Sudheer Pai
Fail positions of stripping steam control valves in various columns in our refinery were compared. It was observed that except in vacuum columns, all other stripping steam control valves are fail close. The stripping steam control valves of crude columns, side strippers, vacuum flashers (visbreakers), fractionators (Visbreakers) were fail close. Request forum members to give their views on why vacuum column stripping steam control valves are fail open.
thanks
Sudheer Pai
#2
Posted 24 May 2010 - 12:37 AM
Greetings
Fail positions of stripping steam control valves in various columns in our refinery were compared. It was observed that except in vacuum columns, all other stripping steam control valves are fail close. The stripping steam control valves of crude columns, side strippers, vacuum flashers (visbreakers), fractionators (Visbreakers) were fail close. Request forum members to give their views on why vacuum column stripping steam control valves are fail open.
thanks
Sudheer Pai
Fail position of a CV to be specified regarding the safety/economical point of views.In the case of "vacuum column stripping" safest mode for steam control valve is fail open to prevent vacuum formation during its control loop failure.
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