What is good value for MTBR of DGS ? 3 yrs ? 5 yrs ? 10 yrs ?
Do any one have MTBR records for DGS in Refinery/Gas plant/Petrochemical plant compressors ?
We are facing repeated bearing and motor failure for Canned Motor Pumps in Sour Water Service duties.
Pumps are as per API 685. Average head is 30 meter, Flow 20m3/hr and fluid temp. 50 Deg C.
During design stage, EPC contractor considered sour water as a clean service. But practically...
For 5% and 10% Caustic @ 40 Deg C application which is the best (Optimum) flushing plan ?
We can not use plan 32. Plan 11/62 are in use but still problem of crystalisation and seal failure exist.