CIP and SIP Explained: Differences, Stages, and Application in Pure Water Systems
Purpose of cleaning in place and steaming in place, design requirements, relationship to RO membrane cleaning, and inline measurement.
CIP Cleans, SIP Sanitizes
- CIP (Clean-in-Place): cleaning of internal surfaces without dismantling. It works through flow velocity, temperature, chemistry, and contact time.
- SIP (Steam-in-Place): sanitization or sterilization of lines with steam without dismantling. It depends on slope, condensate drainage, and dead-leg-free design.
- Sequence: CIP first, then SIP. SIP after inadequate CIP can increase corrosion and rouging issues.
- In pure water systems, it has three meanings: CIP final rinsing of equipment with WFI and PW; steam sanitization of the distribution loop and storage vessel; and chemical cleaning of RO membranes.
See our system validation and qualification and engineering solutions pages for qualification and design.
CIP and SIP Side by Side
| CIP | SIP | |
|---|---|---|
| Purpose | Remove residue | Microbial control: sanitization or sterilization |
| Medium | Detergent solution, hot water, rinse water | Steam. Pharmaceutical engineering literature requires clean steam wherever steam or condensate contacts a critical surface |
| Governing factors | Agent type and concentration, temperature, contact time, flow velocity | Temperature (121 °C in ISPE presentation), steam reaching all surfaces, condensate removal |
| Design requirement | All internal surfaces must be wetted; cleaning agent must flow continuously and not pool at low points | Line sloped to drain condensate; drain at low point; no dead legs within the SIP boundary |
| Verification | Flow, concentration, temperature, and time logging; rinse water conductivity and clarity | Heat distribution, condensate drainage; clean steam quality tests |
| Sensor requirement | Compatibility of CIP chemistry and temperature with sensor wetted parts | Resistance to steam temperature and pressure |
CIP Stages and Design Rules
Typical stages
- Pre-rinse: clean water is circulated through the line by a centrifugal pump and sent to drain.
- Detergent circulation: the solution is heated to the circuit temperature and circulated for the duration required by the procedure.
- Drainage: once cleaning finishes, the solution is discharged to waste.
- Final rinse: water is passed through for a defined time until no residue remains.
- Disinfection (if required): a sanitant is added via a dosing pump and may be left in the lines until the next production run.
Design principles
- High-turbulence, high-flow solution in piping circuits; full wetting with low-energy spray in lightly soiled vessels; high-energy dynamic spray devices in heavily soiled or large-diameter vessels.
- The solution supply unit, supply pump, spray device, return circuit, and return pump are the main components.
- Heating and chemical detergent increase effectiveness; flow velocity must remain high enough to carry dissolved particles away from the surface.
- Fully automated CIP includes a PLC, balance tanks, sensors, valves, heat exchangers, and data acquisition; flow, detergent concentration, temperature, and wash time are monitored continuously.
- Well-designed CIP allows one section of the plant to be cleaned while another is in production and reduces water and chemical consumption.
WFI serves as the final rinse water in this chain: in WFI applications, it is used in the final rinsing of lyophilizers, filling lines, and autoclaves (sterile steam generation) to prevent bioburden residue. For details, see water for injection (WFI) systems and purified water (PW) systems.
SIP: Steam, Slope, and Condensate
Design requirements
- ASME BPE: lines sterilized by SIP must be sloped so that condensate drains by gravity, and drain points must be marked. The recommended minimum slope is 1.0% (GSD2).
- ASME BPE: no dead legs shall exist within the SIP boundary.
- USP ⟨1231⟩: if a system is to be sanitized with steam, careful sloping and low-point drainage are critical for condensate removal and sanitization success.
- Flexible elements (hoses, etc.) are selected to be compatible with cleaning and SIP conditions.
Steam quality and rouging
- Clean steam is defined in the USP monograph: it is generated by evaporating purified water without droplet entrainment and is used wherever steam or condensate contacts a critical surface. Quality control is performed on the condensate.
- In validation practice, non-condensable gases, dryness value, and superheat tests according to EN 285 are applied for clean steam.
- ASME BPE: poorly drained clean steam headers, pressure gradients, and SIP after inadequate CIP can increase corrosion and rouging formation; condensate can accumulate behind poorly sequenced valves. Details: rouging and derouging.
Slope, drainage, and dead-leg figures for hygienic design are covered in hygienic design and dead legs; the comparison of hot water, ozone, and chemical sanitization is in PW and WFI loop sanitization.
RO Membrane CIP: When and How
In a pure water line, RO CIP differs from hygienic piping CIP: it removes fouling and scaling from the membrane. Values are from an RO membrane manufacturer's technical manual and vary by membrane model.
Cleaning triggers and steps
- Trigger: 10% drop in normalized permeate flow; 5% – 10% increase in normalized salt passage; 10% – 15% increase in normalized pressure drop.
- Six steps: solution make-up, low-flow pumping, circulation, soaking (approximately 1 hour; 10 – 15 hours for difficult fouling), high-flow pumping (30 – 60 minutes), and flushing.
- Flushing: with RO permeate or deionized water; pre-filtered raw or feed water is not used.
- Stages cleaned separately: stages are cleaned individually so that foulants removed from the first stage are not pushed into the second stage.
- Sequence: typically alkaline cleaning first; acid cleaning is started first only when calcium carbonate or iron oxide is present.
Equipment and sanitization
- Cleaning solution pH ranges between 1 and 13; a stainless steel (316) or non-metallic composite pump, polypropylene or fiberglass-reinforced plastic tank, 5 – 10 micron polypropylene cartridge filter, and corrosion-resistant materials are used. Line velocity is kept at or below 3 m/s.
- Cleaning temperature must not drop below 15 °C, as kinetics slow significantly. Tank volume is sized based on the empty pressure vessel volume plus the connecting pipe volume.
- Sanitization: a hydrogen peroxide and peracetic acid mixture is diluted with RO permeate to 0.2% (by weight) peroxide and circulated below 25 °C for 20 minutes; biocidal efficacy and membrane life are more favorable at pH 3 – 4. Free chlorine, chlorine dioxide, and combined chlorine are not recommended.
- In heat-sanitizable RO elements, hot water is raised to approximately 80 °C and held for 60 – 90 minutes; transmembrane pressure must remain below 1.7 bar. This is the preferred method in pharmaceutical and food plants, as it is easy to validate and requires no chemical storage or rinsing.
- In biologically active waters, chemical sanitization is performed every 3 – 5 days in summer and approximately every 7 days in winter; frequency is site-specific.
For EDI system design following RO, see EDI system selection and EDI systems.
Sensor Selection in CIP and SIP Lines: Hamilton
The values below are taken from Hamilton product documentation. Compatibility varies by model.
| Measurement | Sensor | Temperature and pressure | CIP / SIP |
|---|---|---|---|
| Conductivity (ultrapure water, WFI) | Conducell UPW | 0 – 130 °C, 10 bar | Autoclave, CIP, SIP compatible; USP 645 compliant |
| Conductivity (process, CIP solution) | Conducell 4US-T150 | -20 – 135 °C, 6 bar | CIP/SIP compatible |
| Conductivity (high pressure) | Conducell 4USF-VV | Up to 20 bar | Autoclave, CIP, SIP compatible |
| pH | EasyFerm Plus | Autoclave 130 °C, SIP 140 °C, 6 bar | CIP, SIP, autoclave |
| pH, ORP | Polilyte Plus | 0 – 130 °C; 10 bar (H, HB, PHI glasses) | CIP/SIP and autoclave |
| pH (aggressive media) | ChemoTrode | 0 – 130 °C, 6 bar | CIP/SIP |
| Dissolved oxygen | OxyFerm FDA | 0 – 130 °C, 4 bar | Autoclave, CIP, SIP |
| Dissolved oxygen | OxyGold G | 0 – 130 °C, 12 bar | Autoclave, CIP, SIP; OxyGold B is CIP only (0 – 100 °C) |
| Mounting (flow) | FlexiFit housing | -10 – 140 °C, 0 – 16 bar(g) | Autoclavable, CIP/SIP compatible |
- CIP rinse-out validation: a conductivity sensor verifies that rinse water has dropped to the target conductivity (listed among Hamilton Conducell applications).
- Sensor selection depends on whether the process is CIP or SIP and on cycle frequency: PHI glass on EasyFerm Plus is recommended for frequent SIP/autoclaving, and HB glass for frequent CIP.
- The Retractex housing family includes a connection option featuring the patented HyCIP cleaning principle: Retractex housing.
For conductivity and temperature measurement in ultrapure water and WFI loops, see online analyzers; for an overview of Hamilton products, see the Hamilton page.
Sources: CIP lecture notes (pharmaceutical validation); ASME BPE-2019 (SD-2.4.3, SD-3.1.2.2, Table D-2-2); USP 37 ⟨1231⟩; Boeke and Le Brun, Practical Pharmaceutics; RO membrane manufacturer technical manual; Hamilton product documentation.
Frequently Asked Questions About CIP and SIP
CIP, SIP, their differences, RO membrane cleaning, and CIP/SIP-compatible sensors.
What is CIP?
CIP (Clean-in-Place) is the cleaning of the internal surfaces of pipes, vessels, process equipment, and fittings without dismantling them. Previously, closed systems were disassembled and cleaned manually; CIP makes cleaning faster, less labor-intensive, and more repeatable. Its purpose is to remove residues from process systems.
What is SIP?
SIP (Steam-in-Place) is the sanitization or sterilization of the same lines with steam without dismantling them. ASME BPE requires lines sterilized by SIP to be sloped so that condensate drains by gravity and requires that no dead legs exist within the SIP boundary. Steam is referred to in an ISPE ozone guideline presentation as sterilization at 121 °C.
What is the difference between CIP and SIP?
CIP is cleaning: it removes residue with detergent and hot water through flow velocity, temperature, chemistry, and contact time. SIP is microbial control: it performs sterilization or sanitization with steam. In practice, CIP is applied first, followed by SIP; ASME BPE notes that SIP applied after inadequate CIP can create corrosion mechanisms and make remediation methods more difficult.
When does an RO membrane require CIP?
An RO membrane manufacturer's technical manual recommends cleaning elements when normalized permeate flow drops by 10%, when normalized salt passage increases by 5% to 10%, or when normalized pressure drop increases by 10% to 15%. Waiting too long may prevent cleaning from restoring performance and shortens the interval between cleanings. The manual also requires checking causes such as pretreatment or recovery first.
How is post-CIP rinsing verified?
The conductivity and residual chemistry of the rinse water are monitored. Hamilton Conducell conductivity sensors are listed for CIP rinse-out validation applications and are CIP/SIP compatible. In advanced CIP systems, rinse water clarity can be monitored near the return point with an infrared absorption or scattered-light sensor, and sanitant concentration can be monitored with an inline photometer.
Do Hamilton sensors withstand CIP and SIP?
In Hamilton's product documentation, Conducell UPW (0 – 130 °C, 10 bar), EasyFerm Plus pH (SIP 140 °C, autoclave 130 °C, 6 bar), ChemoTrode pH, Polilyte Plus pH, and OxyFerm and OxyGold G dissolved oxygen sensors are specified as CIP/SIP compatible. OxyGold B is CIP compatible. Compatibility varies by model; temperature and pressure limits are the values specified on the product pages.
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