Geyser IC · ABB Value Provider / Channel Partner · Measurement & Analytics
ABB ControlMaster

PID regulators and controllers

A shared platform for local control of temperature, pressure, flow, level, pH and other variables. Models mainly differ in size, I/O and control strategy capabilities.

Comparison

From CM10 to CMF310

FunctionCM10CM30CM50CMF310
Standard PID loopStrong capabilityStrong capabilityStrong capabilityStrong capability
Dual-loop / extended functionsLimitedYesYesYes
Cascade / ratio / feed-forwardBasic applicationsAvailableAvailableAvailable
Profiles / ramp-soakConfiguration-dependentStrong capabilityAvailableAvailable
Ethernet / MODBUSYesYesYesYes
Field installationIP66 front panelIP66 front panelIP66 front panelEntire enclosure IP66
When to use it / when to consider alternatives

Standalone controller or centralised control?

Standalone works well when
  • there are one or a few local loops
  • operation must continue without the PLC/DCS
  • a retrofit must avoid changes to central software
  • operators need a clear local interface
PLC/DCS is preferable when
  • many loops interact
  • complex sequences, interlocks and batch logic are required
  • historical data, cybersecurity and central management are priorities
  • maintenance must be coordinated at system level
Best practice

PID installation and commissioning

Correct input scaling

Before tuning, check range, linearisation, engineering units and sensor-failure behaviour.

Output matched to the final element

4–20 mA, time-proportioning, relay and motorised-valve outputs require different logic and timing.

Autotune under realistic conditions

The process must be sufficiently stable, and the test must be able to change the output safely.

Anti-reset windup

Manage output saturation and automatic/manual transfer to avoid large overshoots on return to control.

Sampling / filtering

Excessive filtering slows the loop. Noise and unstable sensors should not be addressed through tuning alone.

Check the valve before the PID

Stiction, deadband and an oversized control valve limit control more than any PID parameter.

ABB replacements

Commander → ControlMaster

Typical migrationABB identifies CM30 as a replacement for several 1/4 DIN Commander controllers, including C200, C300, C350/C355 and C360. CM15 replaces the C150 process indicator. Before quoting, we check I/O, profiles, maths, logic, communications and panel dimensions.
C200 → CM30C300 → CM30C350/C355 → CM30C360 → CM30C150 → CM15
ABB documentation

ABB datasheets and manuals

Download the documents for your model. Shared manuals, protocols and versions are identified in each document card.

CM30

Separate manuals for basic, standard and extended / dual-loop functions.

  • DS/CM30-IT · Rev. X · 11.2023 · IT
  • DS/CM30-EN · Rev. X · 10.2023 · EN
  • IM/CM/B-IT · Rev. U · 07.2021 · IT
  • IM/CM/B-EN · Rev. U · 07.2021 · EN
  • IM/CM/S-IT · Rev. U · 07.2021 · IT
  • IM/CM/S-EN · Rev. U · 07.2021 · EN
  • IM/CM/ED-IT · Rev. AB · 07.2021 · IT
  • IM/CM/ED-EN · Rev. AB · 07.2021 · EN

CM50

Available functions depend on the purchased configuration.

  • DS/CM50-IT · Rev. T · 07.2021 · IT
  • DS/CM50-EN · Rev. T · 07.2021 · EN
  • IM/CM/B-IT · Rev. U · 07.2021 · IT
  • IM/CM/B-EN · Rev. U · 07.2021 · EN
  • IM/CM/S-IT · Rev. U · 07.2021 · IT
  • IM/CM/S-EN · Rev. U · 07.2021 · EN
  • IM/CM/ED-IT · Rev. AB · 07.2021 · IT
  • IM/CM/ED-EN · Rev. AB · 07.2021 · EN
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Technical FAQ

Controller FAQ

CM10, CM30 or CM50?

CM10 is the most compact and suits standard loops. CM30 adds more I/O and cascade or profile functions. CM50 suits dual-loop control and more complex strategies.

When should I choose CMF310?

When the controller must be installed directly in the field without a dedicated cabinet. It is fully IP66/NEMA 4X and can be wall- or pipe-mounted.

Can CM15 control a valve?

CM15 is an indicator, not a PID controller. It supports alarms, totalisation, maths, logic and communications. Use CM10/30/50/CMF310 for PID control.

What does autotune do?

It estimates initial PID parameters. It provides a starting point; final tuning must be checked against actual process dynamics and valve limits.

When should cascade control be used?

When a slow primary variable can be controlled better through a faster secondary loop, such as temperature with an inner steam-flow loop.

When should feed-forward be used?

When a measurable disturbance affects the process and can be compensated before a setpoint error develops.

Standalone controller or PLC/DCS?

Standalone controllers suit a few local loops, retrofits and operational independence. PLC/DCS suits extensive logic, coordinated loops, historians and central management.