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.
Answer / carl_ellis
1) Tubing comes
- in different wall thicknesses and the pressure rating
varies with wall thickness.
- in different material grades of stainless steel. The
pressure rating can vary with material
Your vendor should be able to supply the rating of the
tubing as determined according to a national standard like
ASME B31.1 and ASME B31.1 Process Piping from which
allowable working pressures are calculated from an S value
of XX,XXX psi (YYY.YY MPa) for ASTM A269 tubing at –20 to
100°F (–28 to 37°C), as listed in ASME B31.3 and ASME B31.1.
A factor (different factor for different temperatures) is
used to calculate the reduced maximum pressure at elevated
temperatures.
An example is provided in the Swagelok tubing catalog on
pages 2 and 3 for their tubing (not your tubing).
http://www.swagelok.com/downloads/webcatalogs/EN/MS-01-181.PDF
You need to run the calculation for your vendor's tubing.
2) You need to refill the tubing and condensate pots with
water after the flush but before steam is applied, otherwise
the steam will damage the transmitter.
Carl Ellis
Measure First
64Kg/cm2 = 910 psig
500 Deg C = 932 Deg F
| Is This Answer Correct ? | 0 Yes | 0 No |
What is the difference between HMI and MMI?
A DP Endress and Hauser flow transmitter is always tripping pump at low flow. set point is 74 cubic meter/hr. Thorough impulse line flushing and zero calibration has been done, yet problem persists. What do you think is the problem and how do you rectify this fault?
why we use npn sensor in vibration monitoring system
what is the difference between(Flame proof/Explosion proof)& Fire proof instruments.Both are same or different & if different in which way because the transmitter which have approved ATEX flame proof enclouser but it use PTPE O ring & PTFE Head Gasket,so its (fire safe/fire proof)????????
what is the basic working principle of I/P and Positioner in any control valve.
for oil & gas industries which zone is normally preferred? why? give its example?
why the derivative in PID is always set to zero?
During the design and engineering of a process plant, a good designer should plan for ____________, ___________ and ____________ aspects of the plant
Dear all... I have 1 0-400 duplex type RTD, I connected the A side to the temperature indicator and B side to the PLC panel, but when I have observed then found that The PLC side temp has the variation. and it was distub to other RTD temp also. so what can I do.
HI friends.I am Surya a BTech in Electronics and Instrumentation Engineering.I am going to appear Relince Industries Ltd all India writen test very soon. so plz help me by sendind the probable questions about my subject.My mail ID is surya.barik@gmail.com.
why is the sleeve of the cable used for?
Calibration procedure for Electro magnetic Flow meter
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)