A growing reference of industrial automation terms — written by working engineers, with real plant context, not Wikipedia copy-paste.

Process control fundamentals

PIDProportional · Integral · Derivative

The most common control algorithm in process industries. Three terms that adjust the output based on present error (P), accumulated past error (I), and rate of change (D).

Cascade ControlTwo-loop control

An outer (master) loop manipulates the setpoint of an inner (slave) loop. Used when the slave responds faster to disturbances than the master can react.

FeedforwardPredictive control

Acts on a measured disturbance BEFORE it affects the process variable. Pairs with feedback PID for tight setpoint tracking.

Process Gain (Kp)Steady-state ratio

Change in process variable per unit change in controller output, at steady state. The first parameter you need to tune any loop.

Dead TimeTheta (θ)

Time delay between a controller output change and the first observable response in the process variable. Loops with high θ/τ ratio are notoriously hard to tune.

Integral WindupSaturation issue

When a PID controller saturates and the integral term keeps accumulating error. Anti-windup logic (back-calculation, conditional integration) is mandatory in any production controller.

Functional safety

SILSafety Integrity Level

Quantitative measure of risk reduction by a Safety Instrumented Function. Levels 1–4. Most plants need SIL 2; high-hazard processes need SIL 3.

SIFSafety Instrumented Function

The full chain — sensor + logic solver + final element — that performs one specific safety action (e.g. trip a reactor on high temperature).

SISSafety Instrumented System

Per IEC 61511, the SIS is independent from the BPCS. Different controllers, different I/O, different cabinets. Triconex, DeltaV SIS, Allen-Bradley GuardLogix are common.

PFDavgProbability of Failure on Demand

Average probability that a SIF won”t perform its safety function when called upon. SIL 2 requires PFDavg between 10⁻³ and 10⁻². Lower is better.

HAZOPHazard & Operability Study

Structured review of how a process can deviate from intended operation. The starting point of any functional safety project.

LOPALayer of Protection Analysis

Determines how much risk reduction the existing IPLs (Independent Protection Layers) provide and what gap a SIF must fill.

OT cybersecurity

IEC 62443OT cybersecurity standard

The international standard for industrial cybersecurity. Defines security levels, foundational requirements, and zone/conduit architecture.

Purdue ModelPERA — 1992

Hierarchical reference architecture (Levels 0–5) for industrial control systems. Still the foundation of every OT segmentation strategy.

OTOperational Technology

Hardware/software that detects or causes change through monitoring/control of physical devices. PLCs, DCS, SCADA — distinct from IT (servers, networks, business apps).

Industrial DMZLevel 3.5

Isolated network zone that mediates all data flows between IT (Level 4-5) and OT (Levels 0-2). Patch servers, historians, jump hosts live here.

Industrial communication

Modbus TCPPort 502

The simplest, most ubiquitous industrial protocol. Request/response polling over standard TCP/IP. 50–500 ms typical scan rates.

PROFINETSiemens-led

Three classes: standard TCP, Real-Time (RT, ~10ms), Isochronous Real-Time (IRT, <1ms). Dominant in European motion control.

EtherNet/IPRockwell-led

Industrial Ethernet built on CIP (Common Industrial Protocol). Class 1 cyclic implicit messaging for real-time data; Class 3 for explicit messaging.

OPC UAUnified Architecture

Platform-independent, secure, semantically rich industrial protocol. Replacing OPC Classic. Includes PubSub for cloud-native architectures.

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