Advanced
PLC CIP (Clean-in-Place) Systems for Food & Beverage: Structured Text Programming Guide
Implement a complete CIP clean-in-place system — with multi-step wash sequences, chemical concentration control, temperature/flow validation, and regulatory compliance logging in Structured Text.
What Is CIP (Clean-in-Place)?
CIP (Clean-in-Place) is the automated method of cleaning the interior surfaces of pipes, vessels, and equipment without disassembly. It's mandatory in food, beverage, dairy, pharmaceutical, and brewery industries where hygiene standards require validated, repeatable cleaning cycles.
Why CIP Matters
CIP Process Flow
A standard CIP cycle follows this sequence:
Step 1: PRE-RINSE (Water flush — remove loose debris)
│ 5-10 min, ambient temp, drain to waste
▼
Step 2: CAUSTIC WASH (NaOH — dissolve fats/proteins)
│ 15-20 min, 70-80°C, 1.5-2.0% concentration
▼
Step 3: INTERMEDIATE RINSE (Water — flush caustic)
│ 5-10 min, verify pH < 8.5
▼
Step 4: ACID WASH (HNO₃ or H₃PO₄ — remove minerals)
│ 10-15 min, 60-70°C, 0.5-1.0% concentration
▼
Step 5: FINAL RINSE (Water — flush acid)
│ 5-10 min, verify pH 6.5-7.5, conductivity < 100 µS/cm
▼
Step 6: SANITIZE (Hot water or peracetic acid)
│ 10-20 min, 85°C+ or 200 ppm PAA
▼
Step 7: DRAIN/BLOWDOWN (Air blow to drain remaining liquid)
2-5 min
CIP Data Structures
TYPE CIP_StepType : (
CIP_IDLE,
CIP_PRE_RINSE,
CIP_CAUSTIC_WASH,
CIP_INTERMEDIATE_RINSE,
CIP_ACID_WASH,
CIP_FINAL_RINSE,
CIP_SANITIZE,
CIP_DRAIN,
CIP_COMPLETE,
CIP_FAULT
);
END_TYPETYPE CIP_StepParams :
STRUCT
StepName : STRING(25);
Duration : TIME; // Minimum step duration
TargetTemp : REAL; // °C setpoint
TempTolerance : REAL; // ±°C
ChemConcentration: REAL; // % target
ConcTolerance : REAL; // ±%
FlowRateMin : REAL; // L/min minimum flow
DrainToWaste : BOOL; // TRUE = drain, FALSE = return to tank
RecordRequired : BOOL; // TRUE = log for FDA audit
END_STRUCT;
END_TYPE
TYPE CIP_ProcessData :
STRUCT
Temperature : REAL; // °C actual
FlowRate : REAL; // L/min
Conductivity : REAL; // µS/cm (chemical detection)
pH : REAL; // pH of return flow
Concentration : REAL; // % calculated from conductivity
Pressure : REAL; // bar
TotalVolume : REAL; // Liters used in current step
END_STRUCT;
END_TYPE
TYPE CIP_BatchRecord :
STRUCT
RecipeID : INT;
CircuitName : STRING(30);
StartTime : DATE_AND_TIME;
EndTime : DATE_AND_TIME;
StepCount : INT;
AllStepsPassed : BOOL;
OperatorID : STRING(20);
StepResults : ARRAY[1..8] OF CIP_StepResult;
END_STRUCT;
END_TYPE
TYPE CIP_StepResult :
STRUCT
StepName : STRING(25);
Duration : TIME;
AvgTemp : REAL;
MinTemp : REAL;
MaxTemp : REAL;
AvgConc : REAL;
AvgFlow : REAL;
Passed : BOOL;
FailReason : STRING(50);
END_STRUCT;
END_TYPE
CIP Recipe Configuration
PROGRAM CIP_RecipeSetup
VAR
// Standard dairy CIP recipe (7 steps)
Recipe : ARRAY[1..7] OF CIP_StepParams;
END_VAR// Step 1: Pre-Rinse
Recipe[1].StepName := 'PRE_RINSE';
Recipe[1].Duration := T#8m;
Recipe[1].TargetTemp := 40.0;
Recipe[1].TempTolerance := 5.0;
Recipe[1].FlowRateMin := 200.0;
Recipe[1].DrainToWaste := TRUE;
Recipe[1].RecordRequired := TRUE;
// Step 2: Caustic Wash
Recipe[2].StepName := 'CAUSTIC_WASH';
Recipe[2].Duration := T#20m;
Recipe[2].TargetTemp := 75.0;
Recipe[2].TempTolerance := 3.0;
Recipe[2].ChemConcentration := 1.5;
Recipe[2].ConcTolerance := 0.3;
Recipe[2].FlowRateMin := 250.0;
Recipe[2].DrainToWaste := FALSE;
Recipe[2].RecordRequired := TRUE;
// Step 3: Intermediate Rinse
Recipe[3].StepName := 'INTER_RINSE';
Recipe[3].Duration := T#7m;
Recipe[3].TargetTemp := 40.0;
Recipe[3].TempTolerance := 10.0;
Recipe[3].FlowRateMin := 200.0;
Recipe[3].DrainToWaste := TRUE;
Recipe[3].RecordRequired := TRUE;
// Step 4: Acid Wash
Recipe[4].StepName := 'ACID_WASH';
Recipe[4].Duration := T#15m;
Recipe[4].TargetTemp := 65.0;
Recipe[4].TempTolerance := 3.0;
Recipe[4].ChemConcentration := 0.8;
Recipe[4].ConcTolerance := 0.2;
Recipe[4].FlowRateMin := 250.0;
Recipe[4].DrainToWaste := FALSE;
Recipe[4].RecordRequired := TRUE;
// Step 5: Final Rinse
Recipe[5].StepName := 'FINAL_RINSE';
Recipe[5].Duration := T#8m;
Recipe[5].TargetTemp := 25.0;
Recipe[5].TempTolerance := 10.0;
Recipe[5].FlowRateMin := 200.0;
Recipe[5].DrainToWaste := TRUE;
Recipe[5].RecordRequired := TRUE;
// Step 6: Sanitize (hot water)
Recipe[6].StepName := 'SANITIZE';
Recipe[6].Duration := T#15m;
Recipe[6].TargetTemp := 85.0;
Recipe[6].TempTolerance := 2.0;
Recipe[6].FlowRateMin := 200.0;
Recipe[6].DrainToWaste := FALSE;
Recipe[6].RecordRequired := TRUE;
// Step 7: Drain
Recipe[7].StepName := 'DRAIN';
Recipe[7].Duration := T#3m;
Recipe[7].TargetTemp := 0.0;
Recipe[7].FlowRateMin := 0.0;
Recipe[7].DrainToWaste := TRUE;
Recipe[7].RecordRequired := FALSE;
END_PROGRAM
CIP Step Executor
Core Sequence Engine
FUNCTION_BLOCK FB_CIP_Controller
VAR_INPUT
CMD_Start : BOOL;
CMD_Abort : BOOL;
CMD_Skip : BOOL; // Skip current step (supervisor)
ProcessData : CIP_ProcessData;
Recipe : ARRAY[1..7] OF CIP_StepParams;
TotalSteps : INT := 7;
END_VAR
VAR_OUTPUT
CurrentStep : CIP_StepType;
StepNumber : INT;
StepName : STRING(25);
StepTimeRemaining : TIME;
SupplyPumpCmd : BOOL;
ReturnPumpCmd : BOOL;
HeatCmd : BOOL; // Steam valve
CausticValve : BOOL; // Chemical injection
AcidValve : BOOL;
DrainValve : BOOL;
SupplyValve : BOOL;
ReturnValve : BOOL;
AirBlowValve : BOOL;
CycleComplete : BOOL;
CycleFault : BOOL;
FaultMessage : STRING(50);
BatchRecord : CIP_BatchRecord;
END_VAR
VAR
StepTimer : TON;
ConditionsMet : BOOL;
TempOK : BOOL;
ConcOK : BOOL;
FlowOK : BOOL;
StepStarted : BOOL := FALSE;
QualifyTimer : TON;
QualifyTime : TIME := T#30s; // Conditions must hold 30s
// Step result tracking
TempSum : REAL;
TempMin : REAL;
TempMax : REAL;
ConcSum : REAL;
FlowSum : REAL;
SampleCount : DINT;
END_VAR// ── Abort handling ──
IF CMD_Abort THEN
CurrentStep := CIP_FAULT;
SupplyPumpCmd := FALSE;
ReturnPumpCmd := FALSE;
HeatCmd := FALSE;
CausticValve := FALSE;
AcidValve := FALSE;
DrainValve := TRUE; // Safe drain
FaultMessage := 'OPERATOR ABORT';
CycleFault := TRUE;
RETURN;
END_IF;
CASE CurrentStep OF
CIP_IDLE:
// All outputs off
SupplyPumpCmd := FALSE;
ReturnPumpCmd := FALSE;
HeatCmd := FALSE;
CausticValve := FALSE;
AcidValve := FALSE;
DrainValve := FALSE;
AirBlowValve := FALSE;
CycleComplete := FALSE;
CycleFault := FALSE;
IF CMD_Start THEN
StepNumber := 1;
CurrentStep := CIP_PRE_RINSE;
StepStarted := FALSE;
SampleCount := 0;
END_IF;
CIP_PRE_RINSE:
StepName := Recipe[1].StepName;
SupplyPumpCmd := TRUE;
SupplyValve := TRUE;
DrainValve := Recipe[1].DrainToWaste;
ReturnValve := NOT Recipe[1].DrainToWaste;
HeatCmd := ProcessData.Temperature < Recipe[1].TargetTemp;
// Validate conditions
TempOK := ABS(ProcessData.Temperature - Recipe[1].TargetTemp) <= Recipe[1].TempTolerance;
FlowOK := ProcessData.FlowRate >= Recipe[1].FlowRateMin;
ConditionsMet := TempOK AND FlowOK;
// Timer only counts while conditions are met
StepTimer(IN := ConditionsMet, PT := Recipe[1].Duration);
StepTimeRemaining := Recipe[1].Duration - StepTimer.ET;
// Track stats
IF ConditionsMet THEN
SampleCount := SampleCount + 1;
TempSum := TempSum + ProcessData.Temperature;
END_IF;
IF StepTimer.Q OR CMD_Skip THEN
StepTimer(IN := FALSE, PT := T#0s);
StepNumber := 2;
CurrentStep := CIP_CAUSTIC_WASH;
SampleCount := 0;
END_IF;
CIP_CAUSTIC_WASH:
StepName := Recipe[2].StepName;
SupplyPumpCmd := TRUE;
ReturnPumpCmd := TRUE;
SupplyValve := TRUE;
ReturnValve := TRUE;
DrainValve := FALSE;
CausticValve := TRUE; // Inject caustic
HeatCmd := ProcessData.Temperature < Recipe[2].TargetTemp;
TempOK := ABS(ProcessData.Temperature - Recipe[2].TargetTemp) <= Recipe[2].TempTolerance;
ConcOK := ABS(ProcessData.Concentration - Recipe[2].ChemConcentration) <= Recipe[2].ConcTolerance;
FlowOK := ProcessData.FlowRate >= Recipe[2].FlowRateMin;
ConditionsMet := TempOK AND ConcOK AND FlowOK;
StepTimer(IN := ConditionsMet, PT := Recipe[2].Duration);
StepTimeRemaining := Recipe[2].Duration - StepTimer.ET;
IF StepTimer.Q OR CMD_Skip THEN
CausticValve := FALSE;
StepTimer(IN := FALSE, PT := T#0s);
StepNumber := 3;
CurrentStep := CIP_INTERMEDIATE_RINSE;
END_IF;
CIP_INTERMEDIATE_RINSE:
StepName := Recipe[3].StepName;
SupplyPumpCmd := TRUE;
SupplyValve := TRUE;
DrainValve := TRUE;
ReturnValve := FALSE;
CausticValve := FALSE;
HeatCmd := FALSE;
// Rinse until conductivity drops (caustic flushed)
TempOK := TRUE;
FlowOK := ProcessData.FlowRate >= Recipe[3].FlowRateMin;
ConditionsMet := FlowOK AND (ProcessData.Conductivity < 200.0);
StepTimer(IN := ConditionsMet, PT := Recipe[3].Duration);
StepTimeRemaining := Recipe[3].Duration - StepTimer.ET;
IF StepTimer.Q OR CMD_Skip THEN
StepTimer(IN := FALSE, PT := T#0s);
StepNumber := 4;
CurrentStep := CIP_ACID_WASH;
END_IF;
CIP_ACID_WASH:
StepName := Recipe[4].StepName;
SupplyPumpCmd := TRUE;
ReturnPumpCmd := TRUE;
SupplyValve := TRUE;
ReturnValve := TRUE;
DrainValve := FALSE;
AcidValve := TRUE;
HeatCmd := ProcessData.Temperature < Recipe[4].TargetTemp;
TempOK := ABS(ProcessData.Temperature - Recipe[4].TargetTemp) <= Recipe[4].TempTolerance;
ConcOK := ABS(ProcessData.Concentration - Recipe[4].ChemConcentration) <= Recipe[4].ConcTolerance;
FlowOK := ProcessData.FlowRate >= Recipe[4].FlowRateMin;
ConditionsMet := TempOK AND ConcOK AND FlowOK;
StepTimer(IN := ConditionsMet, PT := Recipe[4].Duration);
StepTimeRemaining := Recipe[4].Duration - StepTimer.ET;
IF StepTimer.Q OR CMD_Skip THEN
AcidValve := FALSE;
StepTimer(IN := FALSE, PT := T#0s);
StepNumber := 5;
CurrentStep := CIP_FINAL_RINSE;
END_IF;
CIP_FINAL_RINSE:
StepName := Recipe[5].StepName;
SupplyPumpCmd := TRUE;
SupplyValve := TRUE;
DrainValve := TRUE;
ReturnValve := FALSE;
AcidValve := FALSE;
HeatCmd := FALSE;
// Must achieve clean rinse: conductivity AND pH
FlowOK := ProcessData.FlowRate >= Recipe[5].FlowRateMin;
ConditionsMet := FlowOK AND
(ProcessData.Conductivity < 100.0) AND
(ProcessData.pH > 6.5 AND ProcessData.pH < 7.5);
StepTimer(IN := ConditionsMet, PT := Recipe[5].Duration);
StepTimeRemaining := Recipe[5].Duration - StepTimer.ET;
IF StepTimer.Q OR CMD_Skip THEN
StepTimer(IN := FALSE, PT := T#0s);
StepNumber := 6;
CurrentStep := CIP_SANITIZE;
END_IF;
CIP_SANITIZE:
StepName := Recipe[6].StepName;
SupplyPumpCmd := TRUE;
ReturnPumpCmd := TRUE;
SupplyValve := TRUE;
ReturnValve := TRUE;
DrainValve := FALSE;
HeatCmd := ProcessData.Temperature < Recipe[6].TargetTemp;
TempOK := ProcessData.Temperature >= (Recipe[6].TargetTemp - Recipe[6].TempTolerance);
FlowOK := ProcessData.FlowRate >= Recipe[6].FlowRateMin;
ConditionsMet := TempOK AND FlowOK;
StepTimer(IN := ConditionsMet, PT := Recipe[6].Duration);
StepTimeRemaining := Recipe[6].Duration - StepTimer.ET;
IF StepTimer.Q OR CMD_Skip THEN
HeatCmd := FALSE;
StepTimer(IN := FALSE, PT := T#0s);
StepNumber := 7;
CurrentStep := CIP_DRAIN;
END_IF;
CIP_DRAIN:
StepName := Recipe[7].StepName;
SupplyPumpCmd := FALSE;
ReturnPumpCmd := FALSE;
DrainValve := TRUE;
AirBlowValve := TRUE; // Air blow to clear lines
HeatCmd := FALSE;
StepTimer(IN := TRUE, PT := Recipe[7].Duration);
StepTimeRemaining := Recipe[7].Duration - StepTimer.ET;
IF StepTimer.Q THEN
AirBlowValve := FALSE;
DrainValve := FALSE;
StepTimer(IN := FALSE, PT := T#0s);
CurrentStep := CIP_COMPLETE;
END_IF;
CIP_COMPLETE:
SupplyPumpCmd := FALSE;
ReturnPumpCmd := FALSE;
HeatCmd := FALSE;
CausticValve := FALSE;
AcidValve := FALSE;
DrainValve := FALSE;
AirBlowValve := FALSE;
CycleComplete := TRUE;
StepName := 'COMPLETE';
CIP_FAULT:
SupplyPumpCmd := FALSE;
ReturnPumpCmd := FALSE;
HeatCmd := FALSE;
CausticValve := FALSE;
AcidValve := FALSE;
DrainValve := TRUE;
CycleFault := TRUE;
END_CASE;
END_FUNCTION_BLOCK
Chemical Concentration Control
Maintaining the correct chemical concentration is critical for cleaning effectiveness:
FUNCTION_BLOCK FB_CIP_ChemDosing
VAR_INPUT
Enable : BOOL;
TargetConc : REAL; // % (e.g., 1.5% NaOH)
ActualConc : REAL; // % from conductivity calculation
TankVolume : REAL; // Liters in CIP tank
ReturnFlow : REAL; // L/min return from circuit
END_VAR
VAR_OUTPUT
DosingPumpCmd : BOOL;
DosingPumpSpeed : REAL; // 0-100%
ChemTankLow : BOOL;
ConcentrationOK : BOOL;
END_VAR
VAR
Error : REAL;
Integral : REAL := 0.0;
Kp : REAL := 10.0;
Ki : REAL := 0.5;
Tolerance : REAL := 0.2; // ±0.2%
END_VARIF NOT Enable THEN
DosingPumpCmd := FALSE;
DosingPumpSpeed := 0.0;
Integral := 0.0;
RETURN;
END_IF;
Error := TargetConc - ActualConc;
ConcentrationOK := ABS(Error) <= Tolerance;
IF Error > 0.05 THEN
// Need more chemical
DosingPumpCmd := TRUE;
Integral := Integral + (Error * Ki);
IF Integral > 40.0 THEN Integral := 40.0; END_IF;
IF Integral < 0.0 THEN Integral := 0.0; END_IF;
DosingPumpSpeed := (Error * Kp) + Integral;
IF DosingPumpSpeed > 100.0 THEN DosingPumpSpeed := 100.0; END_IF;
IF DosingPumpSpeed < 10.0 THEN DosingPumpSpeed := 10.0; END_IF;
ELSE
DosingPumpCmd := FALSE;
DosingPumpSpeed := 0.0;
Integral := 0.0;
END_IF;
END_FUNCTION_BLOCK
Circuit Routing — Valve Matrix
CIP systems serve multiple circuits (tank, filler, pasteurizer). A valve matrix routes cleaning solution to the selected circuit:
TYPE CIP_Circuit : (
CIRCUIT_NONE,
CIRCUIT_TANK_1,
CIRCUIT_TANK_2,
CIRCUIT_FILLER,
CIRCUIT_PASTEURIZER,
CIRCUIT_PIPING_RUN_A,
CIRCUIT_PIPING_RUN_B
);
END_TYPEFUNCTION_BLOCK FB_CIP_ValveRouting
VAR_INPUT
SelectedCircuit : CIP_Circuit;
CIP_Active : BOOL;
END_VAR
VAR_OUTPUT
// Supply side valves
V_Supply_Tank1 : BOOL;
V_Supply_Tank2 : BOOL;
V_Supply_Filler : BOOL;
V_Supply_Pasteur : BOOL;
V_Supply_PipeA : BOOL;
V_Supply_PipeB : BOOL;
// Return side valves
V_Return_Tank1 : BOOL;
V_Return_Tank2 : BOOL;
V_Return_Filler : BOOL;
V_Return_Pasteur : BOOL;
V_Return_PipeA : BOOL;
V_Return_PipeB : BOOL;
CircuitSelected : BOOL;
END_VAR
// Close all first
V_Supply_Tank1 := FALSE; V_Return_Tank1 := FALSE;
V_Supply_Tank2 := FALSE; V_Return_Tank2 := FALSE;
V_Supply_Filler := FALSE; V_Return_Filler := FALSE;
V_Supply_Pasteur := FALSE; V_Return_Pasteur := FALSE;
V_Supply_PipeA := FALSE; V_Return_PipeA := FALSE;
V_Supply_PipeB := FALSE; V_Return_PipeB := FALSE;
CircuitSelected := FALSE;
IF NOT CIP_Active THEN RETURN; END_IF;
CASE SelectedCircuit OF
CIRCUIT_TANK_1:
V_Supply_Tank1 := TRUE;
V_Return_Tank1 := TRUE;
CircuitSelected := TRUE;
CIRCUIT_TANK_2:
V_Supply_Tank2 := TRUE;
V_Return_Tank2 := TRUE;
CircuitSelected := TRUE;
CIRCUIT_FILLER:
V_Supply_Filler := TRUE;
V_Return_Filler := TRUE;
CircuitSelected := TRUE;
CIRCUIT_PASTEURIZER:
V_Supply_Pasteur := TRUE;
V_Return_Pasteur := TRUE;
CircuitSelected := TRUE;
CIRCUIT_PIPING_RUN_A:
V_Supply_PipeA := TRUE;
V_Return_PipeA := TRUE;
CircuitSelected := TRUE;
CIRCUIT_PIPING_RUN_B:
V_Supply_PipeB := TRUE;
V_Return_PipeB := TRUE;
CircuitSelected := TRUE;
END_CASE;
END_FUNCTION_BLOCK
FDA Compliance & Batch Records
For food safety, every CIP cycle must produce a verifiable batch record:
FUNCTION_BLOCK FB_CIP_BatchLogger
VAR_INPUT
StepActive : BOOL;
StepNumber : INT;
StepName : STRING(25);
Temperature : REAL;
Concentration : REAL;
FlowRate : REAL;
ConditionsMet : BOOL;
CycleComplete : BOOL;
END_VAR
VAR_OUTPUT
Record : CIP_BatchRecord;
END_VAR
VAR
TempMin : REAL := 999.0;
TempMax : REAL := -999.0;
TempSum : REAL := 0.0;
ConcSum : REAL := 0.0;
FlowSum : REAL := 0.0;
Samples : DINT := 0;
PrevStep : INT := 0;
END_VAR// ── New step started ──
IF StepNumber <> PrevStep THEN
// Save previous step results
IF PrevStep >= 1 AND PrevStep <= 8 AND Samples > 0 THEN
Record.StepResults[PrevStep].StepName := StepName;
Record.StepResults[PrevStep].AvgTemp := TempSum / DINT_TO_REAL(Samples);
Record.StepResults[PrevStep].MinTemp := TempMin;
Record.StepResults[PrevStep].MaxTemp := TempMax;
Record.StepResults[PrevStep].AvgConc := ConcSum / DINT_TO_REAL(Samples);
Record.StepResults[PrevStep].AvgFlow := FlowSum / DINT_TO_REAL(Samples);
Record.StepResults[PrevStep].Passed := TRUE;
END_IF;
// Reset accumulators
TempMin := 999.0;
TempMax := -999.0;
TempSum := 0.0;
ConcSum := 0.0;
FlowSum := 0.0;
Samples := 0;
PrevStep := StepNumber;
END_IF;
// ── Accumulate data while step runs ──
IF StepActive AND ConditionsMet THEN
Samples := Samples + 1;
TempSum := TempSum + Temperature;
ConcSum := ConcSum + Concentration;
FlowSum := FlowSum + FlowRate;
IF Temperature < TempMin THEN TempMin := Temperature; END_IF;
IF Temperature > TempMax THEN TempMax := Temperature; END_IF;
END_IF;
// ── Finalize record ──
IF CycleComplete THEN
Record.StepCount := StepNumber;
Record.AllStepsPassed := TRUE;
// Check all steps passed
FOR i := 1 TO Record.StepCount DO
IF NOT Record.StepResults[i].Passed THEN
Record.AllStepsPassed := FALSE;
END_IF;
END_FOR;
END_IF;
END_FUNCTION_BLOCK
Safety Interlocks
PROGRAM CIP_SafetyInterlocks
VAR
// Critical interlocks
ProductionActive : BOOL; // Process equipment in production mode
CIP_Requested : BOOL;
CIP_Permitted : BOOL;
ChemTankLevel_NaOH : REAL; // % level
ChemTankLevel_Acid : REAL;
CIP_TankLevel : REAL;
SupplyPressureOK : BOOL;
ReturnFlowPresent : BOOL;
SafetyMessage : STRING(50);
END_VARCIP_Permitted := TRUE;
SafetyMessage := '';
// ── Never CIP while in production! ──
IF ProductionActive THEN
CIP_Permitted := FALSE;
SafetyMessage := 'PRODUCTION ACTIVE - CIP BLOCKED';
END_IF;
// ── Chemical tank levels ──
IF ChemTankLevel_NaOH < 10.0 THEN
CIP_Permitted := FALSE;
SafetyMessage := 'CAUSTIC TANK LOW';
END_IF;
IF ChemTankLevel_Acid < 10.0 THEN
CIP_Permitted := FALSE;
SafetyMessage := 'ACID TANK LOW';
END_IF;
// ── Water supply ──
IF CIP_TankLevel < 20.0 THEN
CIP_Permitted := FALSE;
SafetyMessage := 'CIP WATER TANK LOW';
END_IF;
END_PROGRAM
Summary
CIP programming is one of the most demanding PLC applications in food and beverage manufacturing. It combines sequential step control (7+ wash phases), PID chemical dosing for precise concentration management, multi-circuit valve routing for cleaning different equipment, and FDA-compliant batch recording for every cycle. The key design principle is that the CIP timer only counts while all conditions (temperature, concentration, flow rate) are simultaneously met — this guarantees that every second of claimed wash time was actually effective. Combined with robust safety interlocks that prevent CIP during production, this architecture produces a system that is safe, repeatable, and audit-ready.
Sizing the Flow Setpoint: Velocity, Not Litres per Minute
A single FlowRateMin in L/min is the most common thing to get wrong on a multi-circuit system. Cleaning is driven by wall shear, which follows velocity and bore: the floor is around 1.5 m/s in the return pipework, with little gained above roughly 2.1 m/s. So 250 L/min is about 2.3 m/s in 2-inch tube and barely 1.0 m/s in 3-inch. Serve a 2-inch filler loop and a 3-inch silo main from one recipe and one is being rinsed, not cleaned — and the batch record will not say so. Store bore per circuit and qualify the step on m/s. Tanks invert this: a static spray ball is a coverage device, sized near 35–40 L/min per metre of circumference at roughly 1.7–2 bar (25–30 psi) at the ball, and needs a pressure ceiling — pushed harder it atomises instead of forming the falling film that wets the wall.
Where you measure decides what you can claim
Put the qualifying temperature element on the return. Supply-side qualification lets you log 85 °C while the far end of a filler loop sits fifteen degrees cooler. And interlock the steam valve to proven flow, not step state: heating a static line flashes the water, blows a gasket, and on a plate exchanger bakes soil onto the plates you came to clean.
Pre-rinse has a temperature ceiling nobody writes on the P&ID: much above 55 °C, protein in the residual product coagulates and bonds to the wall, which is why pre-rinse is usually run at 40–50 °C. Juniors raise pre-rinse temperature to shorten the heat-up before caustic; the burn-on surfaces weeks later as a failing swab.
Conductivity Lies in Two Directions
Temperature compensation in most transmitters is a linear coefficient near 2 %/°C referenced to 25 °C, derived for dilute aqueous solutions — not 1.5 % NaOH at 78 °C. Calibrating a toroidal sensor in a bucket at ambient and trusting it hot costs several tenths of a percent.
Worse, conductivity counts ions and is not specific to NaOH — so carbonate and the dissolved soil that recovered caustic accumulates get counted as if they were caustic. Across a shift, free alkalinity falls while the reading does not follow it down: the sensor says 1.6 %, titration says 1.1 %. Titrate once per shift and hold that entry in the PLC with an expiry — if the last verified titration predates the SOP interval, block the caustic step or flag every record it produces.
Interlocks That Prevent Contamination, Not Just Collisions
Blocking CIP during production is the easy half. The dangerous case is chemical reaching a product circuit that is not in CIP — a valve-position problem. Interlock on feedback, never command: a commanded-closed return valve with a seized actuator routes 75 °C caustic into a full silo while your command bit reports normal.
Mix-proof (double-seat) valves make separation physical: two independent seals with a leakage chamber vented to atmosphere between them, so a failed seat drips to drain rather than into product. Their seat-lift function, which cleans the seat faces during CIP, should be pulsed, not held — sustained lift admits cleaning fluid faster than the leakage chamber's drain can clear it, so vendors specify a timed pulse. One-shot pulse, mandatory rest interval, one valve per manifold.
Dead legs are the silent failure. The 2D rule (branch length under twice the branch's own inside diameter, measured from the inner wall of the main) is mechanical, but the PLC owns the branches that break it — sample valves, drain points, instrument tees. Pulse those open during caustic.
FUNCTION_BLOCK FB_ChemInjectPermissive
(* Gates every chemical injection valve. Step state alone is NEVER
sufficient - if the supply pump trips mid-wash, dosing must stop. *)
VAR_INPUT
StepWantsChem : BOOL; // caustic or acid step is active
SupplyPumpRun : BOOL; // VFD / contactor RUN feedback, not the command
SupplyVelocity : REAL; // m/s, derived from flow and THIS circuit's bore
ReturnFlow : REAL; // L/min at the return magflow
CircuitLocked : BOOL; // routing FB proves exactly one circuit selected
ProdValvesClosed : BOOL; // ALL product-side valve FEEDBACKS prove closed
PanelInCIP : BOOL; // swing-bend / key-switch proving
END_VAR
VAR_OUTPUT
ChemEnable : BOOL;
BlockReason : STRING(40);
END_VAR
VAR
Established : TON; // velocity must hold before the first drop of chemical
Ridethrough : TOF; // tolerate a brief flow dropout, not a sustained one
END_VAREstablished(IN := SupplyPumpRun AND (SupplyVelocity >= 1.5) AND (ReturnFlow > 0.0),
PT := T#10s);
Ridethrough(IN := Established.Q, PT := T#3s);
ChemEnable := StepWantsChem
AND Ridethrough.Q
AND CircuitLocked
AND ProdValvesClosed
AND PanelInCIP;
IF StepWantsChem AND NOT ChemEnable THEN
IF NOT PanelInCIP THEN
BlockReason := 'SWING BEND NOT IN CIP POSITION';
ELSIF NOT ProdValvesClosed THEN
BlockReason := 'PRODUCT VALVE FEEDBACK NOT CLOSED';
ELSIF NOT CircuitLocked THEN
BlockReason := 'CIRCUIT ROUTING NOT CONFIRMED';
ELSE
BlockReason := 'FLOW/VELOCITY LOW - DOSING INHIBITED';
END_IF;
ELSE
BlockReason := '';
END_IF;
END_FUNCTION_BLOCK
What the Auditor Actually Asks For
Averages are what programs log and what auditors distrust: a 75.4 °C mean hides a four-minute sag to 62 °C when the steam header dipped. Log time in band, time out of band, excursion count, and the worst single excursion — plus a maximum step time, because a step that only accrues while conditions are met otherwise runs all night behind a failed steam valve.
FUNCTION_BLOCK FB_StepBandAudit
VAR_INPUT
StepRunning : BOOL;
InBand : BOOL; // the step's own ConditionsMet
ScanTime : TIME; // task period, e.g. T#100ms
MaxStepTime : TIME; // wall-clock watchdog for this step
END_VAR
VAR_OUTPUT
TimeInBand : TIME;
TimeOutBand : TIME;
Excursions : INT; // times the band was lost after first being reached
LongestOut : TIME; // worst single excursion
StepTimeout : BOOL; // never qualified - call maintenance, do not re-run
END_VAR
VAR
WallClock : TIME;
ThisOut : TIME;
PrevInBand : BOOL;
BandAchieved : BOOL;
END_VARIF NOT StepRunning THEN
TimeInBand := T#0s; TimeOutBand := T#0s; WallClock := T#0s;
ThisOut := T#0s; LongestOut := T#0s; Excursions := 0;
StepTimeout := FALSE; PrevInBand := FALSE; BandAchieved := FALSE;
RETURN;
END_IF;
WallClock := WallClock + ScanTime;
StepTimeout := WallClock > MaxStepTime;
IF InBand THEN
BandAchieved := TRUE;
TimeInBand := TimeInBand + ScanTime;
ThisOut := T#0s;
ELSIF BandAchieved THEN
// Ramp-up before the band is first reached is not an excursion;
// MaxStepTime is what catches a circuit that never gets there.
TimeOutBand := TimeOutBand + ScanTime;
ThisOut := ThisOut + ScanTime;
IF ThisOut > LongestOut THEN
LongestOut := ThisOut;
END_IF;
IF PrevInBand THEN
Excursions := Excursions + 1;
END_IF;
END_IF;
PrevInBand := InBand;
END_FUNCTION_BLOCK
Two habits close findings cheaply. Log a CRC of the recipe parameter block beside the recipe ID — "Recipe 4" proves nothing about which values it held at 03:00 last Tuesday. And attribute every skip or override to a user with a reason code, marking that record not-for-release. The PLC is also, in most architectures, not where the 21 CFR Part 11 record lives; it is the instrument feeding the historian or MES that holds the tamper-evident audit trail.
The record becomes evidence only when physical verification backs it: riboflavin coverage tests under UV at commissioning for every tank and spray device, ATP swabs at fixed post-CIP points against a site-set RLU limit, final-rinse water sampling. Run the riboflavin test before tuning a setpoint — no sequence logic fixes a spray ball aimed at the agitator shaft.