Differential pressure transmitter:

Article link: https://instrumentationtools.com/differential-pressure-transmitter-working-principle/

Question:

Q. Local gauge glass normal but remote level gauge showing high level, cause?

Possible Reasons:

  • Leaky bypass valve (pressure regulating valve)
  • Defective primary element (primary sensing element-diaphragm)
  • Defective transducer

Q. How to blow down DP cell sensing lines?

  1. Close low pressure sensing line valve.
  2. Close high pressure sensing line.
  3. Open bypass valve connecting L.P and H.P side.
  4. System ready for blowdown.
  5. Open low pressure side blowdown valve, wait for about 10 seconds, then close it.
  6. Open H.P side blowdown valve, wait for about 10 seconds, then close it.

Q. Boiler tube plugging:

.btp  .boiler tube pluging

Procedure:
  • Identify the defective tube when the boiler is pressurized, burner cut out.
  • Take permission from office.
  • Shut down boiler according to instruction manual, let it cool down, ventilate before entering.
  • Whole process may take 2/3 days depending on the severity of tube failure. Take preparation accordingly.
  • Prepare enclosed space entry permit, read, and understood by working personnel, have It signed by master.
  • Boiler is provided properly sized tube blanks, use them to blank off the tubes.
  • Tube needs to be blanked off on both end, clean tube ends.
  • Insert tube blanks by hammer, weld if necessary.
  • Fill up boiler with feed water and check for leakages under pressure.
  • Fire up boiler slowly according to instruction manual.

Control:

Boiler Auto combustion Control:

.acc  .bacc

MV= manipulated value (set point, process value difference)
PV=process value (measured value)
A/H=auto or hand
Description:

Initially, MV=SV, PV1=C.SP1, PV2=CSP2, a ≈ b, c ≈ d.
If steam demand ↑, MV↓
O/P of R/A Master Controller ↑, c↑ , a↑
c > d, d passes through LSS,
so no change in CSP1,
But a > b, ‘a’ passes through HSS,
CSP2↑, PV2↓ wrt CSP2
O/P of D/A Air flow controller ↓
ATC air damper opens more,
Combustion Air flow ↑, d↑,
d passes through LSS since d < c,
CSP1 ↑, PV1↓ wrt CSP1,
O/P of R/A Oil flow Controller ↑,
ATO oil control valve opens more,
Steam pressure restored to SV within a few cycles due to I-action of the Master controller. The control scheme above ensures that air is increased ahead of fuel to prevent fuel-rich condition when load ↑. And similarly, fuel will be decreased ahead of air to prevent fuel-rich condition when load ↓

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