shyamshins
Mechanical
- May 4, 2012
- 53
Dear members
This is an agitator seal handling ISO BUTYL BENZENE at 50kg/cm2 while design press. is 45kg/cm2. This seal is operating since last 10 yrs. but has started to fail within last 8 months. It has failed 3 times within a gap of 4 months repeatedly.
Liquid handled is ISO BUTYL BENZENE. Stationary face is of silicon carbide which has deposits on face except the area where carbon (Rotary face) comes in contact with Stationary silicon carbide face, is it because oil they are using has developed sludge in tank as they are using API PLAN 54?
Rotary carbon face is of antimony impregnated. It has pitting marks at it I.D. of which I have attached photographs, is it because this agitator is operating at 50 kg/cm2 more than designed press. and operators are not keeping flushing fluid press. 2kg more than operating press.? is this causing carbon face to move up axially and touch sleeve? can this be the reason pitting marks are developed as operator is complaining that oil goes inside reactor and they have to refill there flushing tank.
O rings for rotary and stationary face are made of VITON and I have observed that they get hardened. Also they are pilled off from inside diameter which is same for rotary and stationary o ring.
Anti rotation pin of Silicon carbide face comes out from back of face and this face has deposits for which I have attached photographs.
Flushing fluid used is SAE 40 oil and they use thermenol oil in outer housing where I have found black sludge accumulated why is this sludge formed?temp. of flushing fluid when it enters seal is 32 degree celcius and at outlet is 34 degree celcius. Temp. in agitator is 200 degree celcius.
[highlight #A40000]CAN SOMEONE HELP ME ISSOLVING THIS SEAL PROBLEM AS THERE ARE 3NOS. OF SEAL AND THEY ARE FAILING WITH A GAP OF 3 MONTHS.[/highlight]
This is an agitator seal handling ISO BUTYL BENZENE at 50kg/cm2 while design press. is 45kg/cm2. This seal is operating since last 10 yrs. but has started to fail within last 8 months. It has failed 3 times within a gap of 4 months repeatedly.
Liquid handled is ISO BUTYL BENZENE. Stationary face is of silicon carbide which has deposits on face except the area where carbon (Rotary face) comes in contact with Stationary silicon carbide face, is it because oil they are using has developed sludge in tank as they are using API PLAN 54?
Rotary carbon face is of antimony impregnated. It has pitting marks at it I.D. of which I have attached photographs, is it because this agitator is operating at 50 kg/cm2 more than designed press. and operators are not keeping flushing fluid press. 2kg more than operating press.? is this causing carbon face to move up axially and touch sleeve? can this be the reason pitting marks are developed as operator is complaining that oil goes inside reactor and they have to refill there flushing tank.
O rings for rotary and stationary face are made of VITON and I have observed that they get hardened. Also they are pilled off from inside diameter which is same for rotary and stationary o ring.
Anti rotation pin of Silicon carbide face comes out from back of face and this face has deposits for which I have attached photographs.
Flushing fluid used is SAE 40 oil and they use thermenol oil in outer housing where I have found black sludge accumulated why is this sludge formed?temp. of flushing fluid when it enters seal is 32 degree celcius and at outlet is 34 degree celcius. Temp. in agitator is 200 degree celcius.
[highlight #A40000]CAN SOMEONE HELP ME ISSOLVING THIS SEAL PROBLEM AS THERE ARE 3NOS. OF SEAL AND THEY ARE FAILING WITH A GAP OF 3 MONTHS.[/highlight]