what are the possible reasons if a control valve fails to open/close?
Answer / carl_ellis
I seen 10 to 20 causes for each of these categories, but
I've only listed one as an example.
Reasons for valve not closing or opening:
intentional or unintentional
- lack of energy - air/electric/hydraulic (Fuse blown)
- insufficient energy - (supply air regulator turned down)
- control system issue (control signal interlocked)
- positioner or I/P issue (locked in manual)
- actuator crippled (punctured diaphragm)
- positioner-to-actuator linkage/plumbing issue (tubing failed)
- actuator-to-valve linkage issue (sheared roll pin)
- valve trim damage
- foreign object blocking movement (how does all that junk
get in the piping in the first place?)
- change in design process conditions (actuator can't close
against increased line pressure)
Not all failures to actuate/move are faults - a valve could
be intentionally locked in place for safety reasons - access
to the piping/tank.
Tell 'em Carl sent you.
| Is This Answer Correct ? | 15 Yes | 0 No |
what is the basic working principle of I/P and Positioner in any control valve.
What is the use of gauge?
how can you change unit of totalizer in siemens mag 5000 flow meter?
What is possitive and negative feedback?
Single acting ON-OFF valve. it is air to open. when sov energized , valve will be open, so during that if air fail then what will be the condition of valve ( open or close ) ???
in instrumentation why we are using 4-20mA , why not voltage ? if somebody design a instrument which works on voltage then can we use that instrument?
what is the deluge ? How can its working?
In bimetallic temp. Gauges why does metal strip bend? Why do we use low expansion factor metal and high expansion factor metal in bimetaliv strip?
1 Answers Process Control Technologies,
What is two wire system and how it work
wt is cold junction compensation
I want to use 1/2 inch SS316 tube in my high pressure & temperature (64 kg/cm2 & 500 deg C)after condensate pot in pressure tranmistter. 1) Is it possible to use 1/2" ss316 tube in high pressure and temperature line. Tube manufacturer is local vendor. 2)On sarting the plant, We need to do system fluse that time condesate is not in the condesate pot so steam is directly contact with the tube. We have no exact calculation to know our tube is ok or nor at this time. pleae,reply.
how can we measure the level measurement with the help of pressure gauge?
Civil Engineering (5086)
Mechanical Engineering (4456)
Electrical Engineering (16639)
Electronics Communications (3918)
Chemical Engineering (1095)
Aeronautical Engineering (239)
Bio Engineering (96)
Metallurgy (361)
Industrial Engineering (259)
Instrumentation (3014)
Automobile Engineering (332)
Mechatronics Engineering (97)
Marine Engineering (124)
Power Plant Engineering (172)
Textile Engineering (575)
Production Engineering (25)
Satellite Systems Engineering (106)
Engineering AllOther (1379)