Learning to implement Structured Text for Pump Control using B&R Industrial Automation's Automation Studio is a useful skill for PLC programmers working in Water & Wastewater. This guide walks through the fundamentals with clear explanations and an illustrative example that you can adapt to a simulator or test bench.
The example uses B&R Industrial Automation terminology and references controller families such as X20 CPU series and X90 Mobile. Confirm the exact instructions, data types, firmware requirements, and licensing in the current vendor documentation before choosing hardware or deploying a project.
The Structured Text approach is particularly well-suited for Pump Control because complex calculations, data manipulation, advanced control algorithms, and when code reusability is important. This combination allows you to leverage powerful for complex logic while managing the typical challenges of Pump Control, including pressure regulation and pump sequencing.
Throughout this guide, you'll find step-by-step implementation guidance, an illustrative code example, and a verification checklist specific to Water & Wastewater. Whether you're programming your first Pump Control exercise or transitioning from another PLC platform, use the material as a starting point and validate it in your exact Automation Studio version and controller environment.
B&R Industrial Automation Automation Studio for Pump Control
Automation Studio is a programming environment associated with B&R Industrial Automation controller families such as X20 CPU series, X90 Mobile, APC2100. This guide uses Structured Text terminology from the supplied guide dataset, but controller capabilities and language support can change by model, firmware, software edition, and license.
Verify Before You Start:
- The selected controller supports the required Structured Text constructs
- The project version matches the installed Automation Studio release
- Required communications, motion, safety, and simulation options are licensed
- Firmware and device-description files are compatible with the project
- The vendor manuals used for the design match the exact hardware revision
Application Planning:
For a Pump Control exercise, map the required inputs and outputs before writing logic. The example considers 5 sensor types, including Pressure transmitters, Flow meters, Level sensors, and 5 actuator types.
Control Equipment for Pump Control:
- Centrifugal pumps for high flow applications
- Positive displacement pumps for metering
- Submersible pumps for wet well applications
- Booster pump systems for pressure maintenance
Controller-family references used in this guide include:
- X20 CPU series: Confirm CPU, I/O, memory, communications, and Structured Text support in the current selection guide
- X90 Mobile: Confirm CPU, I/O, memory, communications, and Structured Text support in the current selection guide
- APC2100: Confirm CPU, I/O, memory, communications, and Structured Text support in the current selection guide
- APC3100: Confirm CPU, I/O, memory, communications, and Structured Text support in the current selection guide
Hardware Selection Checklist:
- Count local and remote I/O, including planned expansion
- Measure the required task and communications update rates
- Identify memory, data-retention, diagnostics, and cybersecurity requirements
- Treat safety functions as a separate, standards-led design activity
- Confirm lifecycle status, regional availability, licensing, and support
Source and Validation Note:
This page does not represent a vendor certification or a hardware acceptance test. Use current B&R Industrial Automation manuals, release notes, and safety documentation as the authority for product-specific behavior. Validate adapted logic in a simulator or isolated test setup before connecting it to equipment.
Investment Considerations:
For Pump Control projects, compare hardware, software licensing, training, engineering, test equipment, commissioning, spares, and ongoing support. Obtain current pricing and lifecycle information directly from the vendor or an authorized regional supplier.
Understanding Structured Text for Pump Control
Structured Text (ST) is a high-level, text-based programming language defined in IEC 61131-3. It resembles Pascal and provides powerful constructs for complex algorithms, calculations, and data manipulation.
Execution Model:
Code executes sequentially from top to bottom within each program unit. Variables maintain state between scan cycles unless explicitly reset.
Core Advantages for Pump Control:
- Powerful for complex logic: Critical for Pump Control when handling intermediate control logic
- Excellent code reusability: Critical for Pump Control when handling intermediate control logic
- Compact code representation: Critical for Pump Control when handling intermediate control logic
- Good for algorithms and calculations: Critical for Pump Control when handling intermediate control logic
- Familiar to software developers: Critical for Pump Control when handling intermediate control logic
Why Structured Text Fits Pump Control:
Pump Control systems in Water & Wastewater typically involve:
- Sensors: Pressure transmitters for discharge and suction pressure, Flow meters (magnetic, ultrasonic, or vortex), Level transmitters for tank or wet well level
- Actuators: Variable frequency drives (VFDs) for speed control, Motor starters (DOL or soft start), Control valves for flow regulation
- Complexity: Intermediate with challenges including Preventing cavitation at low suction pressure
Control Strategies for Pump Control:
- constant: Maintain fixed speed or output
- pressure: PID control to maintain discharge pressure setpoint
- flow: PID control to maintain flow rate setpoint
Programming Fundamentals in Structured Text:
Variables:
- declaration: VAR / VAR_INPUT / VAR_OUTPUT / VAR_IN_OUT / VAR_GLOBAL sections
- initialization: Variables can be initialized at declaration: Counter : INT := 0;
- constants: VAR CONSTANT section for read-only values
Operators:
- arithmetic: + - * / MOD (modulo)
- comparison: = <> < > <= >=
- logical: AND OR XOR NOT
ControlStructures:
- if: IF condition THEN statements; ELSIF condition THEN statements; ELSE statements; END_IF;
- case: CASE selector OF value1: statements; value2: statements; ELSE statements; END_CASE;
- for: FOR index := start TO end BY step DO statements; END_FOR;
Best Practices for Structured Text:
- Use meaningful variable names with consistent naming conventions
- Initialize all variables at declaration to prevent undefined behavior
- Use enumerated types for state machines instead of magic numbers
- Break complex expressions into intermediate variables for readability
- Use functions for reusable calculations and function blocks for stateful operations
Common Mistakes to Avoid:
- Using = instead of := for assignment (= is comparison)
- Forgetting semicolons at end of statements
- Integer division truncation - use REAL for decimal results
- Infinite loops from incorrect WHILE/REPEAT conditions
Typical Applications:
1. PID control: Directly applicable to Pump Control
2. Recipe management: Related control patterns
3. Statistical calculations: Related control patterns
4. Data logging: Related control patterns
Understanding these fundamentals prepares you to implement effective Structured Text solutions for Pump Control using B&R Industrial Automation Automation Studio.
Implementing Pump Control with Structured Text
Pump control systems use PLCs to regulate liquid flow in industrial processes, water treatment, and building services. These systems manage pump operation, protect equipment, optimize energy use, and maintain process parameters.
This walkthrough demonstrates practical implementation using B&R Industrial Automation Automation Studio and Structured Text programming.
System Requirements:
A typical Pump Control implementation includes:
Input Devices (Sensors):
1. Pressure transmitters for discharge and suction pressure: Critical for monitoring system state
2. Flow meters (magnetic, ultrasonic, or vortex): Critical for monitoring system state
3. Level transmitters for tank or wet well level: Critical for monitoring system state
4. Temperature sensors for bearing and motor monitoring: Critical for monitoring system state
5. Vibration sensors for predictive maintenance: Critical for monitoring system state
Output Devices (Actuators):
1. Variable frequency drives (VFDs) for speed control: Primary control output
2. Motor starters (DOL or soft start): Supporting control function
3. Control valves for flow regulation: Supporting control function
4. Isolation valves (actuated for remote operation): Supporting control function
5. Check valves to prevent backflow: Supporting control function
Control Equipment:
- Centrifugal pumps for high flow applications
- Positive displacement pumps for metering
- Submersible pumps for wet well applications
- Booster pump systems for pressure maintenance
Control Strategies for Pump Control:
- constant: Maintain fixed speed or output
- pressure: PID control to maintain discharge pressure setpoint
- flow: PID control to maintain flow rate setpoint
- level: Control tank/wet well level within band
Implementation Steps:
Step 1: Characterize pump curve and system curve
In Automation Studio, characterize pump curve and system curve.
Step 2: Size VFD for application (constant torque vs. variable torque)
In Automation Studio, size vfd for application (constant torque vs. variable torque).
Step 3: Implement primary control loop (pressure, flow, or level)
In Automation Studio, implement primary control loop (pressure, flow, or level).
Step 4: Add pump protection logic (minimum flow, temperature, seal)
In Automation Studio, add pump protection logic (minimum flow, temperature, seal).
Step 5: Program lead/lag sequencing with alternation
In Automation Studio, program lead/lag sequencing with alternation.
Step 6: Implement soft start/stop ramps for smooth operation
In Automation Studio, implement soft start/stop ramps for smooth operation.
B&R Industrial Automation Function Design:
B&R is famous for mapp Technology: a library of pre-engineered FBs covering motion (mapp Motion), robotics (mapp Robotics), HMI (mapp View), alarming (mapp Alarm), recipes (mapp Recipe), data logging (mapp Logger), auditing (mapp Audit), and cybersecurity (mapp Security). OEMs build atop mapp components rather than reimplementing. Private libraries of OEM-specific FBs are common, maintained in versioned Automation Studio libraries.
Common Challenges and Solutions:
1. Preventing cavitation at low suction pressure
- Solution: Structured Text addresses this through Powerful for complex logic.
2. Managing minimum flow requirements
- Solution: Structured Text addresses this through Excellent code reusability.
3. Coordinating VFD speed with system pressure
- Solution: Structured Text addresses this through Compact code representation.
4. Handling pump cycling with varying demand
- Solution: Structured Text addresses this through Good for algorithms and calculations.
Safety Considerations:
- Dry run protection using flow or level monitoring
- Overtemperature protection for motor and bearings
- Overload protection through current monitoring
- Vibration trips for mechanical failure detection
- Emergency stop with proper system depressurization
Performance Metrics:
- Task and I/O timing: Record minimum, average, and maximum values under a defined test load
- Accuracy: Define an acceptable tolerance and compare it with calibrated reference measurements
- Throughput: Count completed cycles over a fixed interval and record rejected or incomplete cycles
- Fault response: Measure detection, safe-state, alarm, and recovery behavior for each test case
- Resource use: Record memory, communications load, and diagnostic-buffer behavior
B&R Industrial Automation Diagnostic Tools:
Automation Studio integrated debugger with breakpoints in every IEC language,System Diagnostics Manager — System-wide runtime health with historical retention,mapp View Diagnostic pages — ready-made diagnostic overlays for machine operators,ARsim integrated simulator — full offline machine testing without hardware,Motion commissioning via mapp Motion oscilloscope — waveform view during axis tuning,Task Class Monitor — per-task cycle time, jitter, and deadline violation tracking,System Designer — topology view of controllers, X2X modules, and powerlink devices,Logger module (mapp Logger) for structured event capture with severity classification,Online comparison between running controller and project — finds out-of-sync changes,mapp Audit — full audit trail of operator actions (GAMP 5 / 21 CFR Part 11 aligned)
Use the monitoring and diagnostic functions available in your Automation Studio version, and record the software, firmware, hardware, workload, and test procedure with every result.
B&R Industrial Automation Structured Text Example for Pump Control
Illustrative Structured Text example for Pump Control using B&R Industrial Automation terminology. Adapt the syntax to your Automation Studio release, compile it, and verify it in an isolated test environment before use on equipment.
(* B&R Industrial Automation Automation Studio - Pump Control Control *)
(* Structured Text Implementation for Water & Wastewater *)
(* B&R projects follow strict Hungarian-style naming with prefixes (b for *)
PROGRAM PRG_PUMP_CONTROL_Control
VAR
(* State Machine Variables *)
eState : E_PUMP_CONTROL_States := IDLE;
bEnable : BOOL := FALSE;
bFaultActive : BOOL := FALSE;
(* Timers *)
tonDebounce : TON;
tonProcessTimeout : TON;
tonFeedbackCheck : TON;
(* Counters *)
ctuCycleCounter : CTU;
(* Process Variables *)
rPressuretransmitters : REAL := 0.0;
rCentrifugalpumps : REAL := 0.0;
rSetpoint : REAL := 100.0; (* Illustrative value; replace with a reviewed requirement *)
END_VAR
VAR CONSTANT
(* Water & Wastewater Process Parameters *)
C_DEBOUNCE_TIME : TIME := T#500MS;
C_PROCESS_TIMEOUT : TIME := T#30S; (* Illustrative value; verify for the process *)
C_BATCH_SIZE : INT := 50; (* Illustrative value; replace with a reviewed requirement *)
END_VAR
(* Input Conditioning *)
tonDebounce(IN := bStartButton, PT := C_DEBOUNCE_TIME);
bEnable := tonDebounce.Q AND NOT bEmergencyStop AND bSafetyOK;
(* Main State Machine - Pattern: State machines on B&R are typically impl *)
CASE eState OF
IDLE:
rCentrifugalpumps := 0.0;
ctuCycleCounter(RESET := TRUE);
IF bEnable AND rPressuretransmitters > 0.0 THEN
eState := STARTING;
END_IF;
STARTING:
(* Ramp up output - Gradual start *)
rCentrifugalpumps := MIN(rCentrifugalpumps + 5.0, rSetpoint);
IF rCentrifugalpumps >= rSetpoint THEN
eState := RUNNING;
END_IF;
RUNNING:
(* Pump Control active - Pump control systems use PLCs to regulate liquid f *)
tonProcessTimeout(IN := TRUE, PT := C_PROCESS_TIMEOUT);
ctuCycleCounter(CU := bCyclePulse, PV := C_BATCH_SIZE);
IF ctuCycleCounter.Q THEN
eState := COMPLETE;
ELSIF tonProcessTimeout.Q THEN
bFaultActive := TRUE;
eState := FAULT;
END_IF;
COMPLETE:
rCentrifugalpumps := 0.0;
(* Log production data - Data logging uses mapp Data and mapp Trend components — configured rather than coded. Structured logging of process variables, machine events, operator actions, and alarm history is handled by mapp components that write to local SD, networked SQL databases, or cloud endpoints. For regulated industries, mapp Audit provides GAMP 5 / 21 CFR Part 11 aligned electronic records. *)
eState := IDLE;
FAULT:
rCentrifugalpumps := 0.0;
(* Alarm handling uses mapp Alarm — a pre-engineered component with severity classes, group acknowledgement, historical archival, and operator-visible banner generation on mapp View HMIs. Alarm definitions live in structured configuration files rather than in code, simplifying translation into multiple operator languages. Integration with mapp Audit captures every acknowledgement for regulated industries. *)
IF bFaultReset AND NOT bEmergencyStop THEN
bFaultActive := FALSE;
eState := IDLE;
END_IF;
END_CASE;
(* Safety Override - Always executes *)
IF bEmergencyStop OR NOT bSafetyOK THEN
rCentrifugalpumps := 0.0;
eState := FAULT;
bFaultActive := TRUE;
END_IF;
END_PROGRAMCode Explanation:
- 1.Enumerated state machine (State machines on B&R are typically implemented using the mapp State Engine component (graphical state-chart editor) or as CASE-of-INT in ST with strongly-typed state enumerations. For complex machines with parallel sub-sequences, SFC is common. State transition logging via mapp Logger is standard practice and supports incident analysis weeks after the fact.) for clear Pump Control sequence control
- 2.Constants use clearly marked illustrative values that must be replaced with reviewed project requirements
- 3.Input conditioning with debounce timer prevents false triggers in industrial environment
- 4.STARTING state implements soft-start ramp - prevents mechanical shock
- 5.Process timeout detection flags a possible stuck condition for investigation
- 6.The final override illustrates a software permissive only; it is not a safety-rated function and must not replace a validated safety system
Best Practices
- ✓Follow B&R Industrial Automation naming conventions: B&R projects follow strict Hungarian-style naming with prefixes (b for BOOL, n f
- ✓B&R Industrial Automation function design: B&R is famous for mapp Technology: a library of pre-engineered FBs covering moti
- ✓Data organization: B&R uses IEC 61131-3 global variable lists, PROGRAM VAR sections, and strongly-t
- ✓Structured Text: Use meaningful variable names with consistent naming conventions
- ✓Structured Text: Initialize all variables at declaration to prevent undefined behavior
- ✓Structured Text: Use enumerated types for state machines instead of magic numbers
- ✓Pump Control: Use PID with derivative on PV for pressure control
- ✓Pump Control: Implement soft start ramps even with VFD (200-500ms)
- ✓Pump Control: Add flow proving before considering pump operational
- ✓Debug with Automation Studio: Use Automation Studio breakpoints in ST — available across all IEC lan
- ✓Safety: Dry run protection using flow or level monitoring
- ✓Use a compatible simulator or isolated test rig to test Pump Control logic before deployment
Common Pitfalls to Avoid
- ⚠Structured Text: Using = instead of := for assignment (= is comparison)
- ⚠Structured Text: Forgetting semicolons at end of statements
- ⚠Structured Text: Integer division truncation - use REAL for decimal results
- ⚠B&R Industrial Automation common error: Task class priority conflicts causing missed cycles in mid-priority application
- ⚠Pump Control: Preventing cavitation at low suction pressure
- ⚠Pump Control: Managing minimum flow requirements
- ⚠Neglecting to validate Pressure transmitters for discharge and suction pressure leads to control errors
- ⚠Insufficient comments make Structured Text programs unmaintainable over time
Related Certifications
Applying Structured Text to Pump Control using B&R Industrial Automation Automation Studio requires understanding the platform, the process, and the project's acceptance criteria. This guide has covered implementation structure, an illustrative code example, verification practices, and common pitfalls for a intermediate Pump Control exercise.
Use the practices outlined here to create a design that can be reviewed and tested. Define performance targets in the project requirements and confirm them with repeatable measurements.
Next Steps:
1. Check Sources: Read the current Automation Studio help, controller manual, release notes, and relevant standards
2. Practice Safely: Adapt the example in a simulator or isolated training setup
3. Review: Have the I/O map, state behavior, faults, and recovery steps reviewed
4. Test: Record normal, boundary, fault, restart, and communications test results
Structured Text Foundation:
Structured Text (ST) is a high-level, text-based programming language defined in IEC 61131-3. It resembles Pascal and provides powerful constructs for...
Project duration depends on scope, reviews, hardware availability, software and firmware versions, testing, commissioning, and site constraints. Remember: Use PID with derivative on PV for pressure control
For further learning, explore related topics including Recipe management, Wastewater treatment, and B&R Industrial Automation platform-specific features for Pump Control optimization.