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How to Read a PFD and a P&ID: A Guide for Owners and Managers

Two drawings come up in almost every review of a process plant: the process flow diagram (PFD) and the piping and instrumentation diagram (P&ID). Owners, investors and operations managers are asked to comment on both, often without having been shown how to read them.

This guide reads one small example on both drawings: a section that heats a feed liquid with steam before it enters a reactor. The same heater appears on the PFD and on the P&ID, so you can see what each drawing adds.

The two drawings in one sentence each

  • A PFD shows how the process works. It has the main equipment, the main streams and their flows, temperatures and pressures.
  • A P&ID shows how the plant is built and controlled. It has every pipe, valve and instrument, and the control loops that connect them.

Reading the PFD

Process flow diagram of a feed heating section. Feed from storage enters feed tank T-101, feed pump P-101 sends it through steam heater E-101, and it leaves for reactor R-101. Low pressure steam enters the heater and condensate leaves. A stream table lists flow, temperature and pressure for five numbered streams.
Figure 1. Example PFD of a feed heating section, with its stream table. Select the drawing to open it full size.

Read a PFD in four steps.

  1. Follow the main flow. It normally runs left to right. Here the feed enters tank T-101, pump P-101 raises its pressure, heater E-101 warms it, and it leaves for reactor R-101.
  2. Identify the equipment. Each item has a tag. The letter gives the type and the number identifies the item.
  3. Look up each stream. The numbers in diamonds refer to columns in the stream table.
  4. Check that it balances. What goes into each item must come out.

Table 1. Common equipment tag letters

LetterEquipmentOn the example
T or TKStorage tankT-101, feed tank
PPumpP-101, feed pump
EHeat exchangerE-101, feed heater
RReactorR-101, on another sheet
V or DPressure vessel or drumNone
CColumn or compressorNone

Letters vary between companies, so check the legend sheet that comes with the drawings.

Using the stream table

The stream table is where a PFD can be checked with a calculator. On the example:

  • Mass. The feed is 6,250 kg/h in streams 1, 2 and 3. Nothing is added or lost. The steam in stream 4 equals the condensate in stream 5, at 350 kg/h.
  • Pressure. The pump raises the feed from 0 to 4.0 barg. The heater takes 0.5 bar of that, leaving 3.5 barg to reach the reactor.
  • Heat. The feed is heated from 20°C to 80°C. With a heat capacity of 2.0 kJ/kg·K, that needs 6,250 × 2.0 × 60 = 750,000 kJ/h, or 208 kW. The steam supplies 350 kg/h × 2,133 kJ/kg = 746,550 kJ/h, or 207 kW. The two agree.

If these checks fail on a real PFD, ask why before the drawing is used for anything else.

What the PFD leaves out

The PFD has no valves, no instruments and no pipe sizes. It does not show how the outlet temperature is held at 80°C or what happens if it rises. Those answers are on the P&ID.

Reading the P&ID

Piping and instrumentation diagram of feed heater E-101. The process line has an isolation valve on each side of the heater, a temperature transmitter TT-101 and a relief valve PSV-102 on the outlet. Controller TIC-101 receives the temperature signal and positions steam control valve TV-101, which fails closed. The steam line has pressure gauge PI-201, and condensate leaves through steam trap ST-201. Each line carries a line number.
Figure 2. Example P&ID of the same heater, E-101. Select the drawing to open it full size.

The heater is the same item as on the PFD. The P&ID adds everything needed to build, operate and maintain it.

Table 2. Symbols on the example P&ID

SymbolTag on the exampleWhat it is
CirclePI-201, TT-101An instrument mounted in the field, on or near the pipe
Circle inside a squareTIC-101A function in the control system, seen on the control room screens
Two triangles, point to pointNot taggedA manual valve, used here to isolate the heater
Two triangles with an actuator on topTV-101A control valve, positioned by a signal
Angled valve with a springPSV-102A pressure relief valve, which opens by itself at its set pressure
Square with a diagonalST-201A steam trap, which lets condensate out and holds steam in
Solid lineDN50-P-1003A pipe
Dashed line with an arrowNoneAn instrument signal, pointing to the device that receives it

Reading an instrument tag

Instrument tags follow the ISA-5.1 standard. The first letter is what is measured. The letters after it say what the device does. The number identifies the loop.

Table 3. Instrument tag letters used on the example

TagFirst letterFollowing lettersMeaning
TT-101T, temperatureT, transmitterMeasures temperature and sends it to the control system
TIC-101T, temperatureI, indicator; C, controllerDisplays the temperature and controls it
TV-101T, temperatureV, valveThe valve that the temperature loop moves
PI-201P, pressureI, indicatorA pressure gauge read at the pipe
PSV-102P, pressureS, safety; V, valveA pressure relief valve

Other common first letters are F for flow and L for level. Everything with the number 101 belongs to one control loop.

Tracing a control loop

A control loop has three parts: a measurement, a controller and a final element. Follow the dashed lines and their arrows.

  1. TT-101 measures the temperature of the feed leaving the heater.
  2. TIC-101 compares it with the set point of 80°C.
  3. TV-101 opens to admit more steam if the feed is too cold and closes if it is too hot.

The note "FC" beside the valve means fail closed. If instrument air or the signal is lost, the valve shuts and the steam stops. For a heater that is the safe direction. Every control valve should show its failure position, and each one is worth asking about in a review.

Reading a line number

Each pipe has a line number that links the drawing to the line list and the piping specification.

Table 4. The parts of line number DN50-P-1003

PartMeaningOther examples on the drawing
DN50Nominal pipe size, 50 mm (2 inch)DN40 steam, DN25 condensate
PService: processLS, low pressure steam; C, condensate
1003Sequence number of the line1004 after the heater

The number changes from 1003 to 1004 across the heater because the fluid conditions change. Full line numbers often add a piping class and an insulation code. Formats differ between companies.

Five questions to ask in a P&ID review

You do not need to be an engineer to ask useful questions. On the example:

  1. Can this equipment be isolated for maintenance? Yes on the process side, with a manual valve on each side of the heater.
  2. What protects it from overpressure? PSV-102. If both manual valves are shut with steam on, the trapped liquid heats and expands, and the relief valve opens at 6.0 barg.
  3. Where does the relief go? The drawing says "to safe location". Ask where that is.
  4. What happens on loss of air or power? TV-101 fails closed and heating stops.
  5. How does the operator know something is wrong? TIC-101 shows the temperature in the control room. This drawing has no high temperature alarm, which is a fair point to raise.

Side by side

Table 5. What each drawing shows for the same heater

ItemPFDP&ID
Heater E-101Shown, with dutyShown
Flows, temperatures, pressuresStream tableKey values only
Pipe sizes and line numbersNot shownEvery line
Manual valvesNot shownShown
Control loopNot shownTT-101, TIC-101, TV-101
Relief valve and steam trapNot shownPSV-102, ST-201

The example is simplified for teaching. A real P&ID of this heater would also show drains, vents, a bypass around the control valve and insulation. For where these drawings fit in a project, see What a FEED Package Contains.

Takeaway. Use the PFD to check that the process balances, and the P&ID to check that the plant can be operated, maintained and kept safe. On both, start by following one line from end to end.

The drawings are illustrative examples and are not for construction. Symbols and tag formats vary between companies and standards.

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